HomeMy WebLinkAboutDRC-2009-003583 - 0901a06880131fe4[yiy-ycryy^ogs^^
DENISON^/i
MINES
Denlson Mines (USA) Corp.
1050 17th Street, Suite 950
Denver, CO 80265
USA
Tel: 303 628-7798
Fax:303 389-4125
www.denisonmines.com
VIA FEDERAL EXPRESS
August 18, 2009
Mr. Dane Finerfrock, Executive Secretary
Utah Radiation Control Board
Utah Department of Environmental Quality
168 North 1950 West
P.O. Box 144810
Salt Lake City, UT 84114-4810
Dear Mr. Finerfrock:
T^.
Division cf
Radiation Control
•9 yy .cC/ ei_ieo3v"
Re: Renewal Application for Radioactive Materials License (RML) No.
UT1900479: Health Physics Interrogatories - Round 2; and Engineering
Comment Interrogatories - Round 1
Further to our letter of August 14, 2009, enclosed please find a CD containing an electronic
copy of Denison Mines (USA) Corp.'s. response to the above-captioned Interrogatories.
If you should have any questions or require additional information, please contact the
undersigned.
Yours very truly,
DENISON MINES (USA) CORP.
By:
David C Frydienlund
Vice President, Regulatory Affairs and Counsel
cc: Ron F. Hochstein
Harold R. Roberts
Steven D. Landau
David E. Turk
Denison Mines USA Corp
1050 17th Street Suite 950
DENISO Al Denver CO 80265
Ift1IES
Fax303 389-4125
www.denisonmines.com
August 14 2009
Mr Dane Finerfrock Executive Secretary
Utah Radiation Control Board
Utah Department of Environmental Quality
168 North 1950 West
P.O Box 144810
Salt Lake City UT 84114-4810
Dear Mr Finerfrock
Re Renewal Application for Radioactive Materials License RML No UT1900479
Health Physics Interrogatories --Round and Engineering Comment Interrogatories --
Round
This letter is in response to the Executive Secretarys correspondence of July 2009 received
by Denison Mines USA Corp Denison or DUSA on July 2009 with attached Health
Physics Interrogatories Round and Engineering Conmient Interrogatories Round
pertaining to the White Mesa Mills the Mills February 2007 License Renewal Application
the 2007 License Renewal Application
Each Interrogatory is shown in italics below followed by Denisons response to the question
and/or request for information
SECHON HEALTH PHYSICS INTEROGA TORIES -ROUND
INTERROGATORY STA TEMENT ALTERNATE FEED
Round One Interrogatory Statement 11 Provide the inspection procedure that discusses
the inspection requirements of the alternate feed materials that are stored in containers other
than drums from when the mill takes acceptance of the materials until they process the material
and Statement 12 Provide the procedure that discusses how alternate feed material that is
leaking from containers other than drums and is exposed to the wind will be containerized The
issue is ALAR4 Demonstrate how mill workers and the General Public are protected from
unnecessary inhalation exposure from alternate Feed Stocks that have 0.009 to 65%uranium
content that are allowed to be exposed to the wind
Denison Response
Alternate feed materials are managed at the Mill in such manner as to keep potential exposures
to the public and occupational exposures within the exposure levels for conventional ore
operations at the Mill
Conventional ores processed at the Mill range in grade from less than .05%to over 1.0%U308
on average from Arizona Strip ores The Mills State of Utah Radioactive Materials License No
UT 1900479 the Mill License contemplates that conventional ores will be stockpiled in bulk
on the Mills ore pad pending processing
The MILDOS AREA modeling performed in 2007 and submitted with the 2007 License
Renewal Application assumed full Mill operations of 2000 tons per day 365 days per year with
Arizona Strip ores having an average grade of 0.64%U308 That modeling assumed that
730000 tons of ore would be handled at the Mill each year and that an average of approximately
300000 tons of 0.64%ore would be stored on the Mills ore pat at any given time These
assumptions also result in an assumed production rate of 8.8 million pounds of U308 per year
The 2007 MJILDOS AREA modeling was also performed assuming full operations with
Colorado Plateau ores averaging 0.25%U308 resulting in the production of 3.5 million pounds
of U308 per year
The 2007 MILDOS AREA modeling demonstrated that such conventional ore operations and
practices do not result in exposures to the public in excess of the regulatory standard of 100
mrem/yr in R3 13-15-30 or the ALARA goal of 10 mrem/yr excluding radon 222 and its decay
products in R3 13-15-1014 In fact the 2007 modeling shows the Total Effective Dose
Equivalent including radon and its decay products to the nearest resident under the foregoing
assumptions for Arizona Strip ore production to be less than mrem/yr which is less than 2.0%
of the regulatory standard of 100 mrems per year and Total Effective Dose Equivalent
excluding radon and its decay products of less than mrem/yr which is less than 10%of the
ALARA goal of 10 mrem per year In addition the 2007 modeling demonstrated that the Total
Effective Dose Equivalent values both including and excluding radon and its decay products
for full operations with Colorado Plateau ores are
less than half of the values for the Arizona
Strip ores described above
The modeling also demonstrated that the doses to the nearest resident excluding radon and its
decay products do not exceed 25 mremlyr to any organ as required by 40 CFR 190 In fact the
results do not exceed mrem/yr which is less than 5%of the 40 CFR 190 standard
See Section 3.13.2.6 of the 2007 License Renewal Application for discussion of this MILDOS
AREA modeling for the Mill
Occupational exposures at the Mill are kept within the regulatory standard of 5000 mrem per
year and the Mills ALARA goal of 1250 mrem per year 25%of the regulatory standard
through implementation of the Mills radiation safety program as set out in the Mills Radiation
Protection Manual Air particulate in various areas of the Mill including various locations on
the Mills ore pad is monitored and time weighted doses are calculated for workers who may be
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exposed to air particulate from ore stored on the ore pad and other ore pad activities Similarly
time weighted exposures from radon and gamma are calculated The Total Effective Dose
Equivalents for workers at the Mill even during Arizona Strip ore runs have historically been
well below the Mills ALARA goal of 1250 mrem per year
The assumptions in the MILDOS AREA modeling are verified by air particulate sampling at the
five air particulate monitoring stations located in the areas surrounding the Mill Air particulate
samples from the Mills inception have demonstrated that the Mill operates in manner that
maintains exposures to the public at levels that are well within regulatory standards and ALARA
goals
It is evident from the foregoing that based on the modeled results and historic air particulate and
occupational exposure monitoring data the Mill operates well within applicable regulatory
standards and ALARA goals and without any significant impacts to public health safety or the
environment
The foregoing analysis for conventional ores sets the environmental envelope for Mill operations
that can be performed without considering the need for further modeling Alternate feed
materials are handled so as not to allow potential exposures to the public to exceed the potential
exposures from processing Arizona Strip ores at full capacity without further modeling and if
further modeling is required without exceeding the applicable regulatory standards and ALARA
goal specified in R313-15-101 R313-15-301 and 40 CFR 190 Similarly alternate feed
materials are only handled in manner that ensures that occupational exposures are kept within
the Mills ALARA goal of 1250 mrem per year To date all alternate feed materials have fallen
well within this envelope and no feed-specific modeling has been required
In order to meet these requirements the following practices have been followed for alternate
feed materials
High grade alternate feed materials typically with 1.0%U308 or greater are usually
received at the Mill and stored in drums or other containers This is the way that CaF2
KOH Rhone Poulenc Cotter Concentrates and the Cameco KF Calcined Regen and
UF4 alternate feed materials have been received and stored at the Mill
Alternate feed materials that are received in bulk and that have higher risk of public or
occupational exposure than Arizona Strip ores such as may result from high radioactivity
and/or fine dry particles relative to Arizona Strip ores have been covered by less
radioactive materials while stored on the Mills ore pad This is the way the Heritage
alternate feed materials were handled on site and
Alternate feed materials that are received in bulk and that have lower risk of public or
occupational exposure than Arizona Strip ores have been stored in bulk on the site in the
same manner as conventional ores This is the way the Ashland Ashland and Linde
FUSRAP materials and the Cabot and FMRI materials have been handled on site
Currently there are approximately 11000 tons of FMRI alternate feed materials and 5000 tons
of Cabot alternate feed materials stored in bulk on the ore pad The average uranium content of
each of those materials is estimated to be less than 0.25%U308 The quantity and radioactivity
of those materials is much less than the quantity and radioactivity of Arizona Strip ores assumed
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in the MILDOS AREA modeling to be stored in bulk on the ore pad 300000 tons at grade of
0.64%U308 In addition the Cabot and FMRI alternate feed materials arrive at the site in
moist state and harden into state that is if anything less dispersible by wind than conventional
ores As result the same precautions to prevent windblown at the site for conventional ores
periodic water sprays are considered adequate for those materials
Based on the foregoing practices Denison is satisfied that all alternate feed materials are handled
at the Mill in manner that ensures that exposures to the public and occupational exposures are
kept within the environmental assumptions for the site and well within applicable regulatory
standards and ALARA goals
INTERROGATORY STA TEMENT ALTERNATE FEED
Round One Interrogatory Statement 13 Provide the procedure used to determine how
and when alternate feed is to be processed through the mill The Mill is currently installing an
Alternate Feed Circuit to the mill with operational status to begin in June 2009 Provide
Radiation Safety information for example additional PPE requirements and monitoring
requirements and general overview of operation of this new circuit
Denison Response
2.1 Overview of New Alternate Feed CircuitHistorically the Mill has processed alternate feed
materials utilizing existing Mill equipment and facilities However
In most cases the portions of the existing Mill circuit used for alternate feed processing could
not simultaneously be used for conventional ore processing thereby resulting in alternate feed
processing displacing conventional ore processing and
Cleaning up the process circuits between different alternate feed processing runs and prior to
subsequent conventional ore processing runs can be costly and time-consuming
In order to eliminate these two issues the Mill constructed new alternate feed circuit the
Circuit that can be run simultaneously and independently from number of the conventional
ore processing circuits The solvent extraction precipitation drying and packaging stages
however will normally continue to be performed as needed by the use of existing facilities
The Circuit has its own drum dumping station This station was designed specifically for UF4
alternate feed material which is the first alternate feed material to be processed through the
Circuit Modifications to the Circuit including the manner of introducing feed into the Circuit
may be made for different alternate feed materials For example low grade bulk materials may
be introduced through the existing SAG mill and pulp storage tanks and piped to the new Circuit
Tailings solids are separated from solutions in the Circuit and are piped to the tailings system
Any raffinates from the Circuit are piped to the tailings system
Pregnant solutions are piped either to the Mills existing solvent extraction circuit or directly to
precipitation in the Mills existing precipitation circuit
2.2 Overview of UF4 Processing in the Circuit
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The Circuit has been designed to accommodate number of different types of alternate feed
materials However it has initially been set up to process the UF4 alternate feed materials
which are currently being processed brief description of the UF4 processing steps is set out
below
Drums of UF4 material are dumped in the drum dumping station while submerged in hot sodium
carbonate solution and then the mixture of UF4 material and hot sodium carbonate solution is
transferred to another vessel for digestion and dissolution of the uranium and fluoride Next
caustic soda is added and the uranium is precipitated from solution Diatomaceous earth is then
added to aid in filtration and the uranium precipitate is filtered from the fluoride-bearing liquid
The fluoride-bearing liquid is sent to tailings and the uranium-bearing solids are mixed with
water and transferred to another vessel for re-dissolution in hot sulfuric acid solution Following
acid re-dissolution any remaining solids are removed by second stage of filtration and the
uranium-bearing solution is sent to one of the impurity removal tanks In the impurity removal
tank ammonia is added to raise the pH sufficient to precipitate iron but leave the uranium in
solution The iron precipitate is allowed to settle and the purified uranium-bearing solution is
transferred to the normal uranium precipitation drying and packaging circuits of the Mill for
final processing
block flow diagram showing the UF4 processing is attached as Appendix to this letter
2.3 Radiation Safety Features
2.3.1 DACs
There will likely be three derived air concentrations DACs used for the Circuit ore leach
and SX These DACs will be calculated in accordance with Section 4.0 of the Mills Radiation
Protection Manual However since the current Radiation Protection Manual calculates the leach
DAC for the existing Mill facilities as one half of the ore DAC and one half of the precipitation
DAC based on proximity of the existing leach circuit to the SAG mill and the precipitation
circuit the leach DAC for the Circuit will have to be determined based on the physical
configuration of the Circuit Until such time as the manner of calculating DACs for the Circuit is
determined the Mills Radiation Safety Officer RSO will apply the strictest DAC for the
Circuit to all activities in the Circuit
2.3.2 Area Air Particulate Monitoring Stations
There currently are no permanently assigned air particulate monitoring locations in the Circuit
Initially the RSO will place portable air particulate samplers in various areas of the Circuit to
measure air particulate Once enough data is obtained the RSO will identify one or more
locations for permanent inclusion in the routine air particulate monitoring program It is
expected at this time that there will be at least one permanent air particulate monitoring location
in the Circuit However there may be one permanent sampling location for each separate DAC
area of the Circuit In addition the RSO currently plans to reactivate into the routine monitoring
program air particulate monitoring location BA-31 which is located in the nearby vanadium
oxidation circuit The number of air particulate monitoring areas their specific locations and
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whether or not BA-3 is reactivated into the routine monitoring program will depend on the
analysis of data collected from the portable air particulate monitoring samplers and the final
determination of DAC areas for the Circuit
2.3.3 Area Radon Monitoring Stations
Radon monitoring will be conducted via Modified Kusnetz sampling and counting methods
whereby samples for Working Level determination will initially be collected in the same
locations specified for the portable air particulate monitoring sampling The samples will
ultimately be collected at the same locations as the permanently assigned air particulate sampling
locations
2.3.4 Breathing Zone Samples
The RSO will also place breathing zone monitors on selected personnel at the outset to provide
supplemental information on air particulate in the work areas
2.3.5 Gamma Detectors
gamma ball is located in the nearby boiler room as part of the monitoring program for existing
Mill operations Additional gamma balls have been placed at the following locations in the
Circuit
At the drum dumping station on the south side of the Circuit
At the digest/precipitation tank on the south side of the Circuit and
At central location on the north side of the Circuit near the product holding
tank which
is likely to have the most radioactive material on the north side of the Circuit
In addition each worker will wear his or her personal dosimeter
2.3.6 Shielding
No additional shielding has been designed into the Circuit Whether or not shielding will be
required for any particular alternate feed material will be determined on case-by-case basis
2.3.7 Areas Posted as Radiation Areas
No areas of the Circuit will be posted as Radiation Areas per se The RSO will monitor each
area of the Circuit for each alternate feed material being processed through the Circuit and will
make determination if any areas need to be posted as Radiation Areas on case-by-case basis
2.3.8 Bioassays
Bioassays will be performed as required and at the frequency specified in the Radiation
Protection Manual For the initial alternate feed material the UF4 material bioassays will be
performed on all workers in the Circuit at the frequency required for yellowcake workers This
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will provide good initial data base to compare the effectiveness of the other methods of
monitoring employed at the Circuit
2.4 Personal Protective Equipment
Personal Protective Equipment PPE will vary from alternate feed material to alternate feed
material and within each node step in the process for any particular alternate feed material
The appropriate PPE is evaluated for each alternate feed material and either specified in new
SOP for the alternate feed material or in Radiation Work Permit and/or Safe Work Permit for
the feed material In addition the required PPE for any feed material or step in the process may
change over time as determined by the Mills RSO and/or Safety Coordinator Such changes
would typically be evidenced by changes to SOPs or changes to Radiation Work Permits and/or
Safe Work Permits
For the UF4 alternate feed material the following PPE is currently required
Drum Dumping Node
Rubber gloves Tyvex coveralls and hood rubber boots lead apron and full face respirator
14 UF4 Carbonate Digestion Node
Rubber gloves rubber boots wet suits and respiratory protection
NaOH Precipitation Node
Rubber gloves rubber boots and splash gear
NaOH Precipitate Filtration Node
Rubber gloves rubber boots splash gear and respiratory protection
Filter Cake Acid Re-Dissolution Node
Rubber gloves rubber boots and splash gear
Filtration After Acid Digestion of Filter Cake Node
Rubber gloves rubber boots respiratory protection and splash gear
Impurity Removal Node
Rubber gloves rubber boots respiratory protection and splash gear
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INTERROGATORY STA TEMENT ALTERNATE FEED
Provide list of approved alternate feed material that Denison Mines will no longer be
accepting Include an updated list of approved alternate feeds with their corresponding License
Condition
Denison Response
Denison has concluded that it is unlikely that further shipments of the following alternate feed
materials will be accepted at the Mill
Cotter concentrates License condition 10.8
Ashland Formerly Utilized Sites Remedial Action Program FUSRAP materials
License condition 10.10 and
Ashland FUSRAP materials License condition 10.12
The following is an updated list of approved alternate feed materials with their corresponding
License conditions after excluding the foregoing feed materials
Alternate Feed Material Current License Condition
Allied Signal CaF2 10.6
Allied Signal KOH 10.7
Cabot 10.9
Cameco UF4 Regen Materials Calcined
Byproduct and KF Materials 10.11
St Louis FUSRAP materials 10.13
Linde FUSRAP materials 10.14
W.R Grace 10.15
Heritage 10.16
Molycorp 10.17
Maywood FUSRAP materials 10.18
FMRI 10.19
INTERROGATORY STATEMENT RELEASE SURVEYS
Procedure End Dump Trailer Acceptance Handling and Release PBL-9 Rev No R-O
that was provided in Round response The procedure does not instruct the mills radiation
safety technicians on the radiation survey techniques or documentation requirements used by the
mill to release ore trucks from the restricted area Provide procedure that instructs radiation
safety technicians on how to peiform and document radiological surveys
Denison Response
Sections 5.0 and 6.0 of the End Dump Trailer Acceptance Handling Release Procedure
address decontamination and release of equipment for restricted release and unrestricted release
However those sections do not provide details on how the surveys are to be performed
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Denison will add new Section 6.0 to the Mills Radiation Protection Manual which will
provide details on the actual survey procedures See the response to Interrogatory Statement
below
In order to better tie in this new Section 6.0 of the Radiation Protection Manual to the End Dump
Trailer Acceptance Handling Release Procedure we will amend paragraph of each of
Sections 5.0 and 6.0 of that procedure to read as follows changes marked
Section 5.0 paragraph
The Radiation Technician or RSO will scan the trailer truck and tires in various
locations as shown on the Equipment Survey for Restricted Release copy
attached and document the scan readings on the Equipment Survey for Restricted
Release The contamination survey will be performed using appropriate
radiological instrumentation for total activity in accordance with DOT
transportation regulations and the procedures set out in Section 6.0 of the Mills
Radiation Protection Manual The release standards to be met for restricted
release are contained in U.S Department of Transportation DOT Part 49 CFR
173.441b and 173.443 copies attached
Section 6.0 paragraph
The Radiation Technician will perform radiological contamination survey of
the truck and trailer in accordance with the procedures set out in Section 6.0 of
the Mills Radiation Protection Manual If the Radiation Technician indicates
areas that require further decontamination decontaminate those areas as
necessary
INTERROGATORY STATEMENT RELEASE SURVEYS
Procedure Intennodal Container Acceptance Handling and Release PBL-2 Rev No R-O
that was provided in Round response The procedure does not instruct the mills radiation
safety technicians on the radiation survey techniques and documentation requirements used by
the mill to release ore trucks from the restricted area Provide procedure that instructs
radiation safety technicians on how to peiform and document radiological surveys
Denison Response
Sections 5.0 and 6.0 of the Intermodal Container Acceptance Handling Release Procedure
address decontamination and release of equipment for restricted release and unrestricted release
However those sections do not provide details on how the surveys are to be performed
Denison will add new Section 6.0 to the Mills Radiation Protection Manual which provides
details on the actual survey procedures See the response to Interrogatory Statement below
In order to better tie in this new Section 6.0 of the Radiation Protection Manual to the Intermodal
Container Acceptance Handling Release Procedure we will amend paragraph of Section 5.0
and paragraph of Section 6.0 of that procedure to read as follows changes marked
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Section 6.0 paragraph
The Radiation Technician or RSO will scan the IMC chasses tires and White
Mesa Mill truck in various locations as shown on the IMC Container Survey for
Restricted Release attached and document the scan readings on the Container
Survey for Restricted Release The contamination survey will be performed using
appropriate radiological instrumentation for total activity in accordance with DOT
transportation regulations and the procedures set out in Section 6.0 of the Mills
Radiation Protection Manual The release standards to be met for restricted
release are contained in U.S Department of Transportation DOT Part 49 CER
173 .441b and 173.443 copy of which is attached
Section 5.0 paragraph
The Radiation Technician will perform radiological contamination survey of the IMQ
chassis and tires in accordance with the procedures set out in Section 6.0 of the Mills
Radiation Protection Manual If the Radiation Technician indicates areas that require
further decontamination decontaminate those areas as necessary
INTERROGATORY STATEMENT RELEASE SURVEYS
Round One Interrogatory Statement 16 Release Surveys for Product Drums Explain
how the survey techniques the release standards used and documentation of surveys of Product
Drums that contain radioactive material are sufficient to demonstrate regulatory compliance
and maintain public health and safety Explain why surveying techniques such as the use of
Large Area Wipes or swipes to look for removable contamination are not being used on all
Product Drums being surveyed for release 49CFR 173.4431 Contamination Control
requires removable contamination survey on EACH package Change product drum survey
procedures to reflect the regulatory requirement
Denison Response
Removable contamination is currently surveyed on each product drum as required by 49 CER
173.4431 The level of non-fixed removable radioactive contamination on the external
surfaces of each product drum offered for transport is determined by the same methods as for ore
trucks and IMCs i.e by comparing survey for total fixed and removable alpha contamination
to the standard for removable contamination alone which is an other method of equal or
greater efficiency contemplated by 49 CFR 173.443 See the response to Interrogatory
Statement below
However the wording in Section 2.7 of the Mills Radiation Protection Manual for uranium
product shipments and in the Mills procedure Release and Shipping of Vanadium Blackflake
No PBL.-15 Book 10 the Vanadium Release SOP for vanadium product shipments does not
make this clear
Denison proposes to amend those procedures to more accurately describe the actual procedures
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Section 2.7 of the Radiation Protection Manual will be amended to read as follows changes over
the current version are marked
2.7.5 Uranium Concentrate Shipments
The procedures for exclusive use uranium concentrate shipments are
Inspect each product barrel that makes up the consigned shipment for leaks holes
in the barrels cleanliness etc
Barrels requiring repair shall be repaired prior to the radiation survey
Perform fixedtotal i.e fixed and removable alpha survey of each barrel using
the procedures and equipment specified in Section 6.0 The release limits for
fixedtotal fixed and removable alpha radiation contamination is an average of
5000 dpm/100 cm2 and maximum of 15000 dpmJlOO cm2 Any barrel that
exceeds 1000 dpm/100 cm2 fixed alpha radiation contamination requires
removable alpha smear/wipe test to be performed
Perform removable alpha survey of each barrel exceeding 1000 dpm/100 cm2
fixedtotal alpha contamination The release limit for removable alpha radiation
contamination is 1000 dpm/100 cm2 Perform smear/wipe test and analyze
filters for removable alpha on 25%of the barrels at minimum and perform
smear/wipe test and analyze the filters for removable alpha on any barrels that
exceed 1000 dpmllOO cm2 total alpha contamination
Similarly Section 5.5.1 of the Vanadium Release SOP will be amended to read as follows
changes over the current version are marked
5.5.1 Alpha Surveys
Perform total i.e fixed and removable fixed alpha survey of each
drum using the procedures and equipment specified in Section 6.0 of
the Mills Radiation Protection Manual The release limits for total
fixed and removable alpha radiation contamination is an average of
5000 dpm/100 cm2 and maximum of 15000 dpm/100 cm2 Any
drum that exceeds 1000 dpm/lOOcm2 fixedg alpha radiation
contamination requires removable alpha smear/wipe test to be
performed
Perform removable alpha survey on any barrel exceeding 1000
dpm/100 cm2 fixed4 alpha contamination The release limit for
removable alpha contamination is 1000 dpm/100 cm2 Perform
smear/wipe test and analyze filters for removable alpha on 25%of the
barrels at minimum and perform smear/wipe test and analyze the
filters for removable alpha on any barrels that exceed 1000 dpm/100
cm2 fixedtotal contamination
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Record the results of the foregoing alpha surveys on the attached
Source Material Assay and Radiological Survey of Vanadium Form
and
Any drums with visible contamination are to be cleaned prior to
release
INTERROGATORY STATEMENT --RELEASE SURVEYS
Provide procedure that instructs radiation safety technicians on how to perform and
document radiological surveys for releasing equipment from the Mills restricted area
Denison Response
The Mill is currently preparing written procedure for performing and documenting radiological
surveys for releasing trucks intermodal containers other equipment and product drums from the
Mills restricted area which will be new Section 6.0 of the Mills Radiation Protection Manual
Denison will submit the new Section 6.0 for Executive Secretary review within 30 days after the
date of this letter
INTERROGATORY STATEMENT RELEASE SURVEYS
Round One Interrogatory statements 14-17 Explain how the survey techniques the
release standards used and documentation of surveys of Equipment are sufficient to demonstrate
regulatory compliance and maintain public health and safety Explain why surveying techniques
such as the use of Large Area Wipes and swipes to look for removable contamination are not
being used on all items being surveyed for release
In response to the method outlined in 49 CFR 173.4431a Denison Mines states Using
portable alpha detection equipment that measures the combined fixed and removable
contamination is therefore another method contemplated by paragraph which is 49CFR
73.4431b above of equal or greater efficiency because the Mill applies the removable
contamination standard to combined reading offixed and removable contamination Provide
efficiency calculations to determine the efficiency of this method Include the survey procedure
used the efficiency of the meters and probes used in relation to U-238 Show that the meters and
probes that are/will be used has
the appropriate sensitivity to provide small enough reading to
measure the required release limits
Denison Response
8.1 Method of Scanning
Denison scans ore trucks intermodal containers product drums and other equipment using the
following techniques and equipment
Restricted Release
Ore trucks intermodal containers chassis and other equipment that are exclusive use and are
dedicated to particular project i.e will be returning to the Mill or another licensee for final
decontamination prior to free release are released from the Mills restricted area in accordance
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with the release standards set out in 49 CFR 173.443 That standard is 22 dpm/cm2 or 2200
dpm/lOOcm2 for non-fixed radioactive contamination
Mill radiation safety staff determines compliance with this standard by performing scan for
total contamination both fixed and removable using Ludlum Model counter with attached
alpha/beta pancake probe or the equivalent The probe has 15 cm2 detection face The survey
results for total fixed and removable contamination are then compared to the standard for
removable alpha contamination if the scan shows 2200 dpm/lOOcm2 or more the piece of
equipment is sent back for secondary decontamination and then resurveyed In fact Mill
practice is to send piece of equipment back for secondary decontamination if the instrument
reads anything above non-detect
The Ludlum Model counter also measures beta/gamma activity on separate scale
simultaneously with the total measurements thereby allowing Mill radiation safety staff to
determine compliance with applicable beta/gamma release standards at the same time
Unrestricted Release
Ore trucks chassis intermodal containers reagent delivery trucks and all other equipment as
well as product drums that are released from the Mills restricted area on an unrestricted basis
are released in accordance with the standards set out in NRCs Guidelines for Decontamination of
Facilities and Equipment Prior to Release for Unrestricted Use or Tennination of Licenses for
Byproduct Source or Special Nuclear Material Division of Fuel Cycle and Material Safety
USNRC Washington DC 20555 That standard is 1000 dpm/lOOcm2 for non-fixed alpha
contamination
Mill radiation safety staff determines compliance with this standard by performing scan for
total alpha contamination both fixed and removable using Ludlum Model 177 counter with
43-1 alpha detection probe or the equivalent The probe has 75 cm2 detection face The
survey results for total fixed and removable alpha contamination are then compared to the
standard for removable alpha contamination if the scan shows 1000 dpm/lOOcm2 or more the
piece of equipment or drum is sent back for secondary decontamination and then resurveyed
In addition to scanning for total alpha contamination with the Ludlum Model 177 counter Mill
radiation safety staff also performs second scan of the equipment or drums with handheld
gamma meter in order to determine compliance with applicable beta/gamma release standards
8.2 MDA Assessment
The minimum detectable activity MDA is defined as the smallest concentration of radioactivity
in sample that can be detected with 5%probability of erroneously detecting radioactivity
when in fact none was present Type error and also 5%probability of not detecting
radioactivity when in fact it is present Type II error IIDA is often used interchangeably with
Minimum Detectable Concentration since the difference between the two terms is only one of
units conversion MDA equations for survey instruments and counters are specified in NRCs
NUREG 1507 Minimum Detectable Concentrations With Typical Radiation Survey Instruments
for Various Contaminants and Field Conditions In order to assess Denisons equipment
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Equation 3-10 described below was applied to data provided by Mill radiation safety staff on
August 2009
Equation 3-10
MDC 4.65VTh
KT
Where
CB is the background count for paired observations of the sample and blank is the
proportionality constant which includes adjustments for detection efficiency and probe geometry
As mentioned above for surveys relating to restricted exclusive use containers Denison uses the
Ludlum Model counter with attached alpha/beta pancake probe The August 2009 data for
this instrument include the following
Probe Size 15 cm2 15%of the Detection Area of Concern
Probe Sensitivity when compared to calibration source 26%
Detection Area to be considered 100 cm2
Background Count 180 cpm
Background Count Time minute
Given these data the Model with pancake probe MDA calculation is
4.65VTh 4.65 13.42 1677 dpmIlOO cm2
10.260.15 0.039
Given that the Model with pancake probe is only used for exclusive use restricted containers
where Denison has adopted release standard of 2200 dpm/100 cm2 the instrument is
sufficiently sensitive to find contaminants at that level of radioactivity
As mentioned above for surveys relating to unrestricted free release for general transport and
other equipment which is being release for unrestricted use Denison uses Ludlum Model 177
counter with 43-1 alpha detection probe The August 2009 data for this instrument include the
following
Probe Size 75 cm2 75%of the Detection Area of Concern
Probe Sensitivity when compared to calibration source 24%
Detection Area to be considered 100 cm2
Background Count 20 cpm
Background Count Time minute
Given these data the Model with pancake probe MDA calculation is
4.65V 34.65 x4.47 132 dpm/100 cm2
10.240.75 0.18
DENISONOAA
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Given that the Model 177 with 43-1 probe is used for unrestricted free release where Denison
has adopted release standard of 1000 dpmIlOO cm2 the instrument is sufficiently sensitive to
find contaminants at that level of radioactivity
In conclusion the instruments used by Denison for releasing equipment and product drums from
the Mill site have the appropriate sensitivity to provide small enough reading to measure the
required release limits It should also be kept in mind that there is an added level of
conservatism in Denison approach in that the instruments are reading total alpha and beta
fixed and removable in the case of restricted release surveys and total fixed and removable
alpha contamination in the case of unrestricted release surveys yet in both cases the survey
results are compared to the standard for removable alpha contamination only
INTERROGATORY STATEMENT ALARA
Round One Interrogatory Statement 18 Designated Eating Areas within the Restricted
Area Explain the just jfication of having designated eating areas and the number of eating areas
within the restricted area and Statement 19 Designated Eating Area within the Restricted
Area Define the criteria used for determining designated eating areas within the Restricted
Area Define what controls each Designated Eating Area must have i.e frisking requirements
wash facilities Entry Procedures etc to be suitable Designated Eating Area
Denison Reponse
The Mill has amended its ALARA Program relating to designated eating areas within the Mills
restricted area after taking into account previous comments and recommendations made by the
State of Utah Division of Radiation Control DRC and suggestions made by the Mills
ALARA Committee The ALARA Program now spells out in more detail the criteria that must
be applied by the Mills RSO in designating an eating area Specifically each designated eating
area must now meet all of the following criteria
located in an area where work with uranium is not performed and there is little likelihood
of contamination
wash facilities are located close by to allow workers to wash their hands etc prior to
entering the designated eating area
scanning machines are placed at each entry into the designated eating area and
each worker entering designated eating area must perform and record personal alpha
scan in the same manner as if the worker were leaving the Mills restricted area and must
be free of contamination prior to entering the designated eating area
copy of page of the Mills ALARA Program marked to show these changes and clean
copy of that page are included as Appendix to this letter
Based on these new criteria the RSO has now reduced the number of designated eating areas in
the Mill to two areas within the restricted area based on the foot traffic in the areas the
relationship to operations both mechanical and process access to wash stations and the ability
to control access to the areas with personnel alpha monitors
DENISONDI
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The first designated eating area is the existing Lunch Room/Training Room This area is limited
to foot traffic of workers going to break or training sessions The room has access to wash
facilities in the Change Rooms located directly below on the ground floor With the Change
Rooms below this designated eating area the employees can change out of PPE wash and then
proceed to the lunch room An additional scanner has been added at the north door scanner
already exists at the south door Individuals coming from the Warehouse through the north door
will now be required to scan at that location prior to entry into the room
The second designated eating area is the area above the Warehouse offices There is only one
entrance into this designated eating area Foot traffic in the area is low The Maintenance
Superintendant and both Operation Foremen have their offices in this area In between the
offices is small break room The break room is for supervisory personnel only There is
wash station directly below the area personal alpha meter is located just inside the door
DUSA has provided training to all of Mill workers on the changes to this program Every
worker has been instructed on the proper activities regarding these designated eating areas Each
worker has been instructed to enter the areas as if they are exiting the Mills restricted area That
is every time someone enters designated eating area he or she must frisk no matter what the
circumstance
The other areas that were previously listed as designated eating areas the Warehouse Offices
Maintenance Offices Instrument Shop Scalehouse Central Control Room and the offices in the
Chemical and Metallurgical laboratories have now been removed as designated eating areas by
memorandum issued by the RSO However these former designated eating areas will continue
to be monitored on weekly basis for alpha contamination
INTERROGATORY STATEMENT EMPLOYEE TRAINING
10 In the revised White Mesa Mill Radiation Safety Training Program Appendix Radiation
Protection at the White Mesa Mill Section Types of Radiation There are five types of ionizing
radiation Alpha Beta Gamma X-Ray and Neutron All forms of ionizing radiation should be
mentioned and then be spec ffic on what types of ionizing radiation are found at the Mill
Denison Response
Section of Appendix to the White Mesa Mill Radiation Safety Training Program has been
amended to mention all forms of ionizing radiation and to better identify the types of ionizing
radiation found at the Mill copy of the revised Appendix marked to show the changes is
attached as Appendix to this letter
INTERROGATORY STATEMENT EMPLOYEE TRAINING
11 In the revised White Mesa Mill Radiation Safety Training Program Appendix Radiation
Protection at the White Mesa Mill section 43 Gamma Radiation This section does not discuss
the three 3fixed nuclear gauges that the mill uses Include discussion on the fixed gauges in
this section
OENISONI4A
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Denison Response
Section of Appendix to the White Mesa Mill Radiation Safety Training Program has been
amended to discuss the three fixed nuclear gauges that the Mill uses copy of the revised
Appendix marked to show the changes is attached as Appendix to this letter
INTERROGATORY STATEMENT STANDARD OPERATING PROCEDURES
12 Round One Interrogatory Statement 28 Provide complete list and copies of all
operating procedures used at the MilL Explain how employees are trained on the procedures
that they use Explain where procedures are kept and how employees have access to the
procedures that they use Provide missing procedures
There are Standard Operating Procedures that are missing from the application The following
are examples but not limited to of procedures that are missing from the application The
Respirator Protection Program and the ALARA Program references NRC Reg Guide 8.15 and
UAC R313-.15-703 lists all of the procedures required in Respirator Protection Program The
Mills Respirator Protection Program is missing some of these procedures
Denison Response
Denison is currently reviewing the Mills Respiratory Protection Program for compliance with
the requirements of NRC Reg Guide 8.15 and UAC R313-15-703 to identify any required
procedures that are not contained in that program Denison will submit revised Respiratory
Protection Program to the Executive Secretary for review within 45 days after the date of this
letter
INTERROGATORY STATEMENT REVISIONS AND UPDATES
13 Round One Interrogatory Statement 36 Provide all revisions to procedures and
programs that have been added or revised since February 2007 License renewal application was
submitted Also provide all procedures and programs that were not included with the February
2007 License renewal application Provide the list below
Denison Response
Attached to this letter as Appendices to are the following Mill procedures and related
documents
PBL-3 Tailings Capacity Evaluation R-9/25/00 Appendix
Section 3.1 White Mesa Mill Tailings Management System and Discharge Minimization
Technology DMT Monitoring Plan DUSA 9/01/08 Appendix
RPP-1 Respiratory Protection Program DUSA-.2 12/1/08 Appendix
Groundwater Monitoring Plan and Standard Operating Procedures for UDEQ Split
Sampling Program Rev 27/1/99 Appendix
PBL-RP-1 Radiation Monitoring-Personnel DUSA-3 8/1/08 Appendix
PBL-RP-3 Equipment Calibration DUSA-2 12/1/08 Appendix
UDEQ Split Sampling Groundwater QA Project Plan Rev 7/99 Appendix
DENISONOAA
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GWDP Groundwater Monitoring Quality Assurance Plan QAP DUSA 6/18/08
Appendix
Cell 4A BAT Monitoring Operations and Maintenance Plan DUSA 1.3 9/1/08
Appendix
PBL-4 Clearance of Linde Material Intermodal Containers R-0 3/15/01 Appendix
and
PBL-6 Heritage Alternate Feed Management R-1 2.14.03 Appendix
The Mill had generic Quality Assurance Program years ago However that program is no
longer in existence It has been replaced by specific Quality Assurance provisions inserted in
individual SOPs where appropriate and for groundwater sampling by the Mills Groundwater
Monitoring Quality Assurance Plan
SECTION ENGINEERING COMMENT INTERROGATORIES ROUND
INTERROGATORY STATEMENT The Reclamation Plan
I-A
The currently approved latest Reclamation Plan needs to receive unique identifying number as
to the version of the plan it is The DRC request that DUSA assign version number e.g 4.0 to
the currently approved reclamation plan If there are iterative changes necessary to the plan as
result of these License Renewal Application comments each DUSA proposed revision to the
plan must be identWed by unique reference number e.g suffix to the number such as
proposed Revision 4.1 4.2 etc
The updates to the Reclamation Plan conveyed by DUSA letter dated July 25 2008 were not
included in the License renewal Application They need to be included
Denison Response
Denison is in the process of preparing an updated version of the Reclamation Plan which will be
assigned the number Revision 4.0 Revision 4.0 of the Reclamation Plan will consolidate all
amendments to the Plan that have been made since Revision 3.0 was approved by NRC on July
24 2000 Revision 4.0 will also include the current approved versions of all drawings and
figures and will make number of other corrections and updates referred to in the following
interrogatory statements
Denison will submit Revision 4.0 of the Reclamation Plan to the Executive Secretary as new
Appendix to the 2007 License Renewal Application within 90 days after the date of this letter
Future amendments to the Reclamation Plan will be numbered and dated so that they can be
easily identified and tied to the then current version of the Reclamation Plan For example if
section of the Reclamation Plan is revised that section will be given revision number and date
such as Section 6.0 Revision 4.1 January 15 2010 Each revised page will have the revision
number and date of the revision in the footer or header of the page However given the size of
the Reclamation Plan and appendices figures and drawings Denison does not anticipate
renumbering and re-issuing the entire Reclamation Plan every time section of the Plan is
OENISONDAA
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amended sheet will be inserted at the beginning of the Reclamation Plan that will identify all
amendments made to the Plan since the date of issue of Revision 4.0 of the Plan The sheet will
list the Sections that have been revised the date of each revision and the revision number for that
Section This will allow reader to keep track of all amendments to the Plan and will allow
Denison and the Executive Secretary to determine if any particular copy of the Reclamation Plan
is current
INTERROGATORY STATEMENT The Reclamation Plan
I-B
Please update and complete Section of the License Renewal Application regarding the
Reclamation Plan Please include the current approved version of the Reclamation Plan as an
Appendix to the License Renewal Application
Denison Response
Revision 3.0 of the Reclamation Plan was incorporated by reference into the 2007 License
Renewal Application as permitted by R313-22-325 and was not included as an Appendix to
the application due to its size That is why it is not referred to in the Index to the Appendices in
the License Renewal Application
However as mentioned in the response to Interrogatory Statement I-A Denison is preparing an
updated Revision 4.0 of the Reclamation Plan which Denison will submit as new Appendix to
the 2007 License Renewal Application revised Index to the Appendices will be included in
Revision 4.0 of the Reclamation Plan
We have amended page 74 of the 2007 License Renewal Application to address the blank field
We have not made any other changes to that page because the dollar amount of the financial
surety was accurate at the date of filing the application Attached as Appendix is revised
page 74 to the 2007 License Renewal Application marked to show changes and clean version
INTERROGATORY STATEMENT The Reclamation Plan
I-C
Regarding the Cell Discharge Channel on Figure -2.2.4-1 Sedimentation basin Detail
The potential need for or absence of rip-rap protection for the cell discharge channel
entry and exit platform aprons must be explained and justified An adequate demonstration
will include but is not limited to analysis according to NUREG-623
The need to join or not join the existing configuration the discharge channel to the toe of
the new south dike of Cell must be explained and justjfied
Drawing details are needed to show the outcome of the above analysis to describe the
sections of the discharge channel its lining appurtenant entry exit apron zones dike
alignment and lining
Denison Response
The Cell Discharge Channel is intended to divert the water accumulated from the PMP storm
event from 143 acre area which includes the sedimentation basin created from the Cell area
the reclaimed Mill area and the area to the north of the Cell area but south of the existing
DENISONOAA
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diversion ditches The channel is created by excavation of the undisturbed ground to the west of
Cell to maximum depth of approximately 17 feet The lower 10 feet of the channel is
excavated in Dakota Sandstone to an elevation matching the lowest point on the west end of the
Cell sedimentation basin The channel will be excavated at slope of 1%and will daylight in
the Dakota Sandstone cliffs in Westwater Canyon cross section of the area to be excavated is
included in Appendix to this letter
The maximum discharge volume through the channel will be 1344 cubic feet per second
resulting in flow velocity of 7.45 feet per second assuming bottom channel width of 120 feet
The channel design proposed in the reclamation plan is actually 150 feet wide at the bottom
which will further reduce the flow velocity The allowable flow velocity for bedrock channel
is -10 feet per second therefore no riprap is required in the channel bottom The entrance to
the channel will match the bottom elevation of the sedimentation basin so no riprap will be
necessary at that point The channel discharge will be on to the cliffs of Westwater Canyon
therefore no riprap will be necessary at that point The discharge calculations are included in
Attachment to the Reclamation Plan and also included in Appendix to this letter
We do not believe that the discharge channel should be joined with the toe of the new fill area on
the north slope of the Cell dike The flows off the dike slope will be very small and the rip rap
toe will easily protect the slope and the reclamation cover The flow velocities at the entrance to
the discharge channel could possibly impact the rip rap toe or require additional rip rap and
should therefore be avoided Water potentially backing up from the entrance to the discharge
channel would be very low velocity in the area near the toe of the Cell north slope and would
not impact the stability of the slope
INTERROGATORY STATEMENT The Reclamation Plan
I-D
This interrogatory is being provided for USA information only This item will be pursued
concurrent with DRC review of the Infiltration and Contaminant Transport Modeling Report
White Mesa Mill Site Blanding Utah ICTM prepared by DUSA Last correspondence on the
report was furnished by DUSA on April 30 2009
Is installation of rock apron at the base of all the final covered tailings cell outslope intended
for the entire perimeter of the final covered tailings cell system If so please clarify by
specifying on the drawings that such is required If not please demonstrate that the absence of
such will be adequate for the 1000-year design period or at minimum 200-year period
Denison Response
The questions raised in Interrogatory Statement I-D will be addressed in the re-design of the
tailings cover system in accordance with the approved ICTM
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INTERROGATORY STATEMENT The Reclamation Plan
I-E
Please demonstrate that for final reclamation of the tailings cells filter blanket is necessary or
unnecessary to be installed below the riprap cover for the top side slopes and rock aprons of
the tailings cells
Denison Response
It is not clear why filter blanket was not included in the original cover design As noted by
DRC Denison is proposing revised cover design as part of the Infiltration Analysis which
will eliminate the rip rap on the top surface of the reclaimed tailings The need for filter
blanket on the side slope and toe areas will be evaluated at that time
INTERROGATORY STATEMENT The Reclamation Plan
I-F
Reclamation Plan Fig 3.2.3-1 Site Map Showing Locations of Buildings and Tankage needs to
be updated to current conditions
Denison Response
An updated version of Reclamation Plan Fig 3.2.3-1 Site Map Showing Locations of Buildings
and Tankage updated to current conditions will be included in Revision 4.0 of the Reclamation
Plan See the response to Interrogatory Statement I-A for more detailed discussion of Revision
4.0 of the Reclamation Plan
INTERROGATORY STA TEMENT The Reclamation Plan
I-G
In the DRC copy of the Reclamation Plan Appendix Attachment Rainfall-Duration Curve
for One-hour PMP at White Mesa Mill is illegible Please provide readable copy of the graph
Denison Response
readable copy of Reclamation Plan Appendix Attachment Rainfall-Duration Curve for
One-hour PMP at White Mesa Mill is attached as Appendix to this letter
INTERROGATORY STATEMENT The Reclamation Plan
I-H
Numerous references to the NRC in the Reclamation Plan must be changed to the Utah Division
ofRadiation Control DRC general overriding amendment to the Reclamation Plan may best
satisfy this need
E.g according to the last sentence on B-2 The report will be submitted to the NRC
Regulatory Commission Paragraph 1.4 1.2 on B-3 and paragraph 1.5 on B-6 also refer
to the NRC
OENISOJAA
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Denison Response
All references to NRC in the Reclamation Plan will be changed to be references to DRC the
State of Utah Department of Environmental Quality or the Executive Secretary as appropriate in
Revision 4.0 to the Reclamation Plan See the response to Interrogatory Statement 1-A for
more detailed discussion of Revision 4.0 of the Reclamation Plan
INTERROGATORY STATEMENT The Reclamation Plan
I-I
In the Reclamation Plan on pp B-2 and B-16 the Final Construction Report is referred to This
report is important to independently document the completion of the reclamation and
decommissioning work In that regard please revise the Reclamation Plan to include the
following
Please remove any reference to NRC/DRC field presence in the Reclamation Plan
The report must be submitted to the DRC within 180 calendar days after the apparent
completion of Construction for Executive Secretary review and approval
Denison Response
The requested changes will be included in Revision 4.0 of the Reclamation Plan See the
response to Interrogatory Statement I-A for more detailed discussion of Revision 4.0 of the
Reclamation Plan
INTERROGATORY STA TEMENT The Reclamation Plan
LI
It appears the current Table of Contents TOC in the Reclamation Plan Revision 3.0 is taken
directly from Revision 2.0 which is now outdated The actual content and page numbers of the
plan were revised in Revision 3.0 Additional content changes to the plan as result of review of
the current license renewal application are expected
Adjustments to the current TOC in the Reclamation Plan are needed to bring the table up to
date final adjustment will need to be done at the end of the review iterations for the license
renewal application
Denison Response
The Table of Contents of the Reclamation Plan will be updated in Revision 4.0 of the
Reclamation Plan See the response to Interrogatory Statement I-A for more detailed
discussion of Revision 4.0 of the Reclamation Plan
INTERROGATORY STA TEMENT The Reclamation Plan
I-K
The Reclamation Plan refers to work in Tailings Cells 123 and sometimes Cell 4A However
the plans and specifications for the reclamation of Cell 4A are not always included in the
Reclamation Plan written text and drawings
OENISON9A
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Additions to the Reclamation Plan are needed to include provisions for the reclamation of Cell
4A into the plans and specifications Provisions for Cell 4A need to be incorporated into the
Reclamation Plan Table of Contents TOC as well as the plans and specifications
Denison Response
Revision 4.0 of the Reclamation Plan will include additions relating to the reclamation of Cell
4A into the written text plans and specifications The Table of Contents of the Reclamation Plan
will be updated accordingly See the response to Interrogatory Statement I-A for more detailed
discussion of Revision 4.0 of the Reclamation Plan
INTERROGATORY STATEMENT The Reclamation Plan
I-L
The tailings cell cover design found in the Reclamation Plan provided with the February 28
2007 License Renewal Application is not the same as that provided in the November 21 2007
Infiltration and Contaminant Transport Modeling Report White Mesa Site Blanding Utah
prepared by MWHAmericas Inc It will be DUSAs responsibility to amend the License Renewal
Application and the Reclamation Plan to ensure that the tailings cells cover design plans
specifications and construction ultimately authorized conforms to the approved ICTM
Denison Response
The Reclamation Plan and to the extent applicable the 2007 License Renewal Application will
be amended to ensure that the tailings cell cover design plans specifications and construction
ultimately authorized conform to the approved ICTM Denison expects that the resulting
changes to the Reclamation Plan may be significant and may justify the creation of Revision
5.0 of the Reclamation Plan in order to properly incorporate the changes into the Plan
INTERROGATORY STATEMENT The Reclamation Plan
H-A
The application states that license violations identified during NRC or State of Utah site
inspections are listed However not all violations are listed Please include listing of all
violations of your Ground Water Quality Protection Permit
Denison Response
Denison disagrees with the foregoing statement All violations including violations under the
Mills State of Utah Groundwater Discharge Permit Air Approval Order and Radioactive
Materials License as of February 28 2007 the date of submittal of the 2007 License Renewal
Application are listed in Table 9.2-1 of Volume of the Application These violations are also
discussed in Sections 9.2.1 9.2.2 and 9.2.3 of Volume of the Application Specifically
Section 9.2.3 entitled Water Quality Notices of Violation addresses the 11 violations issued on
or before February 28 2007 under the Mills Groundwater Discharge Permit
There have been number of violations under the Mills Radioactive Materials License
Groundwater Discharge Permit and Air Approval Order since February 28 2007 However
OENISONOA
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since the disclosure in the 2007 License Renewal Application is as of February 28 2007 these
have not been addressed here
INTERROGATORY STATEMENT Correction of Modelinjj Inferences
H-B
There is no paragraph 3.13.1.6 in the Environmental Report ER This reference must be
corrected
License Renewal Application Paragraph 6.5.8 should clearly state that the statement is
based on modeling predictions
License Renewal Application Paragraph 6.5.9 should clearly state that the statement in the
paragraph is based on modeling predictions
Denison Response
The requested changes have been made to page 65 of the 2007 License Renewal Application
revised page 65 marked to indicate the changes and clean copy are attached as Appendix to
this letter
INTERROGATORY STATEMENT Correct Version of Documents
H-C
The SWBMPP provided as tab in Appendix of the License Renewal Application is not the
approved version Please replace with the June 2008 edition that was approved by the DRC on
July 2008
Denison Response
Attached as Appendix is the June 2008 edition of the Storm Water Best Management Practices
Plan that was approved by the DRC on July 2008
INTERROGATORY STATEMENT Correct Version of Documents
II-D
The edition of the White Mesa Mill Tailings Management System and Discharge Minimization
Technology DMT Monitoring Plan DMT Plan provided as tab 3.1 of Appendix of the
February 28 2007 License Renewal Application is not the approved version Please replace it
with the approved 09/08 Revision Denison-6 version of the plan and attachments
Denison Response
Attached as Appendix is the approved 09/08 Revision Denison-6 version of the White
Mesa Mill Tailings Management System and Discharge Minimization Technology DMT
Monitoring Plan
INTERROGATORY STATEMENT Omission of Document
H-E
The License Renewal Application appears to not contain the Cell 4A BAT Monitoring
Operations and Maintenance Plan OM Plan Please include the latest approved edition in
the application
OENISONOAA
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Denison Response
Attached as Appendix is version 09/08 Revision Denison 1.3 of the Cell 4A BAT Monitoring
Operations and Maintenance Plan which is the latest approved edition of that plan
An electronic version of this letter and Appendices will be transmitted under separate cover
If you should have any questions or require additional information please contact the
undersigned
Yours very truly
DENISON MINES USA CORP
By
David denlund
Vice President Regulatory Affairs and Counsel
cc Ron Hochstein
Harold Roberts
Steven Landau
David Turk
OENISONOs4A
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Circuit for Processing UF4
To Be Operated at theWhite Mesa Mill
White Mesa Mill 2/07 Revision DUSA-
Book 12 ALARA Program Page of 20
The RSO may have other safety related duties such as responsibility for programs of industrial
hygiene and fire and safety but will have no direct production-related responsibility
1.1 Operating Procedures
1.1.1 Standard Operating Procedures Established
The Mill is required to maintain written standard operating procedures or Radiation Work
Permits RWPs for all activities that involve handling processing or storing radioactive
materials as well as health physics monitoring sampling analysis and instrument calibration
All such procedures include consideration of pertinent radiation safety practices to the extent not
covered in the Radiation Protection Manual Respiratory Protection Manual or Environmental
Protection Manual
1.1.2 Policy-for Eating Restricted Area
Smoking is pprrnitted anywhere within the Mills Restricted Area Eating lunches or snacks
or chewing tobacco is not allowed within the Restricted Area of the Mill except for those areas
so designated by the RSO Such noted activity as observed results in supervisory review of
employee actions documentation of the incident and retraining by the Radiation Safety Staff
Repeated occurrences shall be cause for dismissal This policy is in effect to ensure that
radiation and uranium ingestion exposures to Mill workers are maintained ALARA
.hZ hiflhl
The areas of the administrative office building except for the metallurgical laboratory and
sample processing sections is located outside of the Mills Restricted Area are designated as an
eating MeaT
areas The Restricted Area designated eating areas are as designated by the RSO from time to
time and may include Each designated eating area must satisfy the following criteria
Scalehouse
Warehouse Office
Maintenance Office
Change Room
.-.
Mill Office Lunchroom
Chief Chemist Office
Met Lab Office
Training Room
located in an area where work with uranium is not performed and there is little likelihood
of contamination
This page was revised on August 14 2009
White Mesa Mill 2/07 Revision DUSA
Book 12 ALARA Program Page of 20
wash facilities are located close by to allow workers to wash their hands etc prior to
entering the designated eating area
scanning achines are placed
at each entry into the designated eating area and
each worker entering designated eating area must perform and record personal alpha
scan iii the same manner as if the worker were leaving the Mills Restricted Area and
musf be free of contamination prior to entering the designated eating area
The designated eating areas are routinely monitored for alpha and beta-gamma contamination as
provided in the Radiation Protection Manual
This page was revised on August 14 2009
White Mesa Mill 2/07 Revision DUSA-
Book 12 ALARA Program Page of 20
The RSO may have other safety related duties such as responsibility for programs of industrial
hygiene and fire and safety but will have no direct production-related responsibility
1.1 Operating Procedures
1.1.1 Standard Operating Procedures Established
The Mill is required to maintain written standard operating procedures or Radiation Work
Permits RWPs for all activities that involve handling processing or storing radioactive
materials as well as health physics monitoring sampling analysis and instrument calibration
All such procedures include consideration of pertinent radiation safety practices to the extent not
covered in the Radiation Protection Manual Respiratory Protection Manual or Environmental
Protection Manual
1.1.2 Policy-for Eating Restricted Area
Smoking is not permitted anywhere within the Mills Restricted Area Eating lunches or snacks
or chewing tobacco is not allowed within the Restricted Area of the Mill except for those areas
so designated by the RSO Such noted activity as observed results in supervisory review of
employee actions documentation of the incident and retraining by the Radiation Safety Staff
Repeated occurrences shall be cause for dismissal This policy is in effect to ensure that
radiation and uranium ingestion exposures to Mill workers are maintained ALARA
The areas of the administrative office building located outside of the Mills Restricted Area are
designated as eating areas The Restricted Area designated eating areas are as designated by the
RSO from time to time Each designated eating area must satisfy the following criteria
located in an area where work with uranium is not performed and there is little likelihood
of contamination
wash facilities are located close by to allow workers to wash theft hands etc prior to
entering the designated eating area
scanning machines are placed at each entry into the designated eating area and
each worker entering designated eating area must perform and record personal alpha
scan in the same manner as if the worker were leaving the Mills Restricted Area and
must be free of contamination prior to entering the designated eating area
The designated eating areas are routinely monitored for alpha and beta-gamma contamination as
provided in the Radiation Protection Manual
This page was revised on August 14 2009
RADIATION PROTECTION AT THE WHITE MESA MILL
Radiation
High levels of radiation are harmful to us The amount of radiation person is exposed to is
referred to as his or her dose and is typically measured in millirems mrems per year
We are exposed to radiation from natural sources such as the sun the soils and rocks around us
as well as the air we breathe We are also exposed to radiation from other sources such as x-rays
performed in connection with medical and dental examinations In the landing area each
member of the general population
is exposed to about 400 mrem per year from these natural
sources not counting things such as x-rays
Exposure Limits
In order to protect workers from excessive exposure to radiation the Nuclear Regulatory
Commission NRC has set maximum doses that workers can receive each year from working
at facilities such as the White Mesa Mill Under these standards the maximum total dose from
all sources at the Mill over and above background radiation from natural sources is 5000 mrem
per year
In addition the NRC requires that each facility make efforts to keep exposures to workers As
Low as is Reasonably Achievable ALARA below the 5000 mremlyr limit In accordance
with this requirement the Mill has set an ALARA goal at 1250 mremlyr for each worker over
and above natural background This goal is 25%of the regulatory standard of 5000 mremlyr
Exposures to Mill workers are typically well below this ALARA goal being usually in the 80
mremlyr to 400 mremlyr range above background
How do we Keep Exposures to Radiation to Minimum
One of our prime objectives is to keep radiation exposures to Mill workers to minimum This
not only requires the efforts of Denison It also requires the efforts of each Mill worker to keep
his or her exposures to minimum In order for workers to be able to do this proper
understanding of radiation how you can be exposed to it and what precautions you can take are
extremely important These topics are summarized below
Types of radiation
There are three types of ionizing radiation alpha beta and gamma radiation being the
prevalent sources of exposure at the Mill as well as x-ray and neutron radiation which are of
lesser concern at uranium milling facilities
4.1 Alpha Radiation
Here at the White Mesa Mill we work with uranium one of those elements that is naturally
radioactive Uranium is an alpha emitter Alpha radiation doesnt travel very far even in air
The range in air for alpha radiation is about 1.25 inches single sheet of paper can block
alpha radiation Even the skin layer on our bodies stops alpha
radiation So outside of our
body alpha radiation is really no problem What about inside the body Breathing uranium
dust or swallowing uranium dust is the problem Uranium in the human body tends to seek
the bones and kidneys i.e to collect there where it can cause damage
In addition radon gas which comes primarily from uranium ores and tailings emits alpha
radiation and is in the air we breathe at the Mill There is no smell or taste to radon gas and
you cant see it Breathing high levels of radon in the air is also harmful to us
4.2 Beta Radiation
Beta radiation does not travel very far in air but it can penetrate the body so merely being
close to source of beta radiation will result in exposure to radiation It is not necessary to
breathe in or swallow beta emitting particles although that would also be another way that
beta radiation could enter your body
However because most of the radiation associated with the uranium process is alpha
radiation beta radiation is not much of problem at the Mill While exposures to the body
merely from being close to beta radiation are minimal at the Mill internal exposure to beta
radiation that enters the body through inhalation or ingestion of radioactive dust is concern
For example as uranium decays some beta radiation is emitted especially where aged
yellowcake is concerned so personal hygiene in the yellowcake processing portion of the
Mill is important
4.3 Gamma Radiation
Gamma rays are constantly being emitted from the raw ore Like beta radiation gamma
radiation can penetrate the body so being close to source of gamma radiation will result in
exposure to radiation However gamma radiation is stronger can travel further in air and
can penetrate the body more readily than beta radiation As with beta radiation it is not
necessary to breathe in or swallow gamma emitting particles although that would also be
another way that gamma radiation could enter your body
Gamma radiation at the Mill is mainly associated with raw ores tailings solids and some
alternate feed materials So the people working in the ore piles bucking room tailings or
close to certain alternate feed materials should have the highest exposure to gamma radiation
here at the Mill site
In addition to these sources of gamma radiation there are nuclear density gauges in the
Mill complex i.e one west of the CCD area on the exterior of the tails box and two in the
SAG Mill area one of which is located east of the Derrick Screens on the level of the
SAG facility and another on the first level of the SAG facility on the feed line to the east pre
leach tank These gauges contain the gamma emitter Cs-137 The Cs-137 is retained in
container which is in-turn housed within shielded containment referred to as the pig in
order to provide protection to workers from the unshielded source These devices are labeled
with the tn-foil radiation symbol and in-plant gamma surveys are conducted in the
immediate area of these sources to assure that gamma radiation levels are maintained
ALARA These sources of Cs-137 must remain in their shielded containment They must
also be tested periodically However they may only be removed from their shielding tested
serviced or removed from installation by specifically licensed outside contractor
4.4 X-Rays
There are no direct sources of x-radiation at the Mill thus exposure to x-rays is minimal and
only related to minor emissions of x-radiation associated with the uranium decay chain
radiation is similar to gamma radiation in that it is penetrating and considered to be an
external source of exposure to the body Because the Mills radiation safety staff measures
gamma radiation and any x-rays will be an element of those readings the protections
provided for gamma radiation also protect from the minor influence of x-rays at the facility
For these reasons x-rays require no additional consideration at the Mill
4.5 Neutrons
There are no sources of neutron radiation associated with the uranium milling process
However when earthen construction projects are underway at the Mill such as tailings cell
construction construction contract personnel may use neutron gauges to measure soil
moisture and density conditions for construction purposes These devices are not owned or
operated by Denison and any licensing of the gauges is the responsibility of such
contractors As result Denison employee exposure to these sources is negligible and could
only occur near the gauge when in operation
4.6 Radioactive Dust is the Main Concern at the Mill Site
4r4
As can he seen from the discussion above radiation that enters the body through the
inhalation or ingestion of dust is the main concern at the Mill site Keeping dust to
minimum and providing protections to workers to minimize their exposure to radioactive
dust is therefore primary objective Radon is usually not problem unless in confined
spaces Exposures from being close to beta/gamma radiation is also not usually as big
concern at the Mill site due to the relatively low levels of those types of radiation found at
the Mill X-rays and neutron radiation are of minor concern at the Mill
Exposure Pathways and Precautions to be Taken
Radiation can enter the body in three different ways
5.1 Being Close to Source of Gamma Radiation
Being close to ore tailings or certain alternate feed materials will expose the worker to
gamma and beta radiation The stronger the source the closer you are and the longer you
spend close to the source will increase your exposure Shielding such as lead can be used in
some circumstances to reduce exposures to gamma and beta radiation although shielding is
not commonly used at the Mill due to the generally low beta/gamma radiation experienced at
the Mill
Each worker is required to wear an OSL badge that records his or her exposure to beta and
gamma radiation The OSL badge must be worn on the torso and must not be shielded by
clothing
Areas where beta/gamma radiation is high i.e over mradfhr must be posted as Radiation
Areas
The precautions we take at the Mill to keep exposure to beta/gamma radiation to minimum
are
Keeping workers away from areas with high beta/gamma radiation When you see an
area posted as Radiation Area do not go near that area unless required to do so for
specific task
Minimizing the time each worker is required to work in areas with elevated beta/gamma
radiation This also involves rotating workers so that the time each worker spends in the
Radiation Area is kept to minimum
Using shielding in some cases and
Engineered controls in our process to reduce exposures faced by workers
5.2 Breathing in Radioactive Dust or Radon
Any dust at the Mill can be radioactive Ore dust is radioactive Dust from the ore pad is
radioactive Dust from around the facility buildings can be radioactive Yellowcake dust is
radioactive and tailings dusts are radioactive In addition radon gas is radioactive and can be
found in all areas of the Mill facility and property Radon gas is particularly dangerous in
closed areas where it can accumulate
The Mill monitors various areas of the Mill facilities and Mill properties for radioactive dust
and radon gas Each worker is required to keep track of the time he or she spends in each area
of the Mill each day and record these times on his or her Exposure Time Sheet This allows
Mill Radiation Safety Staff to calculate how much exposure to radiation the worker has had
each day by determining how much time each worker spends in each area and by calculating
the exposure for the time spent in each area based on the monitoring results for that area
This is why it is important for each worker to carefully and accurately fill out his or her
Exposure Time Sheet each day
The precautions we take to keep exposures to radioactive dust and radon to minimum are
the following
Good housekeeping is important in order to keep dust to minimum within facility
buildings
Water is sprayed on the ore pad and other areas of the Mill property in order to keep dust
to minimum
Posting and restricting access to areas where there is potential for higher exposures to
radioactive dust
Respiratory protection is required in areas where there is potential for higher exposures
to radioactive dust and/or radon such as in the yellowcake packaging area where uranium
concentrate is being handled
Showers are available to all workers and yellowcake workers are required to shower at
the end of their work shift
Non-routine projects that may result in radiation exposure are controlled by Radiation
Work Permit where personal protective equipment PPE and additional monitoring such
as breathing zone sampling requirements can apply and
Work clothing remains at the Mill and all workers entering the restricted area are
required to survey for alpha contamination prior to leaving the facility
5.3 Ingesting Radioactive Particles
Ingestion of radioactive materials at the Mill is minimal but can occur directly by swallowing
dust that has entered your mouth or indirectly from contamination of food or other items
person might put into his or her mouth For these reasons S-smoking eating chewing gum or
tobacco etc are not allowcdpermitted in working areas of the Mill Eating is restricted to
only designated eating areas You may smoke only in designated area outside of the Mills
restricted area This exposure pathway is best controlled by personal hygiene principles such
as cleaning your hands before eating
Monitoring and Calculation of Total Dose Received by the Worker
In order to ensure that worker exposure is maintained within the regulatory limits and the Mills
ALARA goal various monitoring methods are used to assess the workers exposure Air
samples are collected throughout the plant to assess concentrations of radioactive dust and radon
in the air and the amount of time spent by workers in the various plant areas is recorded to
determine the inhalation exposure of each worker given his/her particular job assignment In
addition gamma and beta exposure is monitored by means of personal exposure badges OSL to
assess individual exposure to external sources The amount of exposure worker receives from
radioactive dust radon and beta/gamma radiation to the body are added up to determine the total
dose referred to as the workers Total Effective Dose Equivalent or TEDE received by the
worker for the year The workers TEDE is then compared to the regulatory limits and the Mills
ALARA goal
Urine samples are also collected from workers to ensure that internal uptake of uranium is not
damaging kidneys and in some instances to determine uptake due to unusual circumstances In
addition and as mentioned above workers are required to scan for alpha contamination as they
exit the restricted area to protect against offsite contamination and exposure
Leaving the Mill Each Day
As can be seen from the information provided above contamination control is important as
means of minimizing exposure to radiation at the Mill One of the more important places where
this control is necessary is when worker leaves the Mill Taking shower leaving work
clothes at the work place and scanning out to ensure that you are not taking contaminants home
on your person are good practices to protect you and your family from offsite exposure All
workers must scan before leaving the Mills restricted area All yellowcake workers must also
shower before leaving the restricted area
Reporting
In order to determine that employee exposures are being maintained within the regulatory limits
and company goals annual exposure calculations for each worker are completed by the
Radiation Safety Department These reports are utilized to demonstrate compliance with the
standards assess any trends in exposure and to provide record to the individual worker Each
worker receives an exposure report annually from the Radiation Safety Department
Conclusion
Uranium is naturally occurring radioactive element which can have harmful effects if not
properly monitored and controlled At the Mill we can be exposed primarily to alpha beta and
gamma radiation and our exposures to those forms of radiation are limited by regulation and
company policy Because uranium is primarily an alpha emitter alpha radiation is the principle
type of radiation exposure at the Mill This means that minimizing the inhalation or swallowing
of radioactive dust at the Mill is primary objective
The radiation you may be exposed to at the Mill is monitored by sampling the air you breathe
and measuring the external radiation received by your personnel exposure badge The results of
this monitoring are evaluated and reported to you annually so that you are made aware of your
exposure
While the company provides engineering controls to protect you from sources of radiation each
employee must remain aware of conditions at the Mill Avoiding high radiation areas wearing
respirators where/when required cleaning your hands before eating avoiding dusty situations
and using contamination control procedures when you leave the property are individual
protections you can use to minimize your exposure to radiation at the Mill
No PBL-3 INTERNATIONAL URANIUM USA CORPORATION
Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date September 25 Title Tailings Capacity Evaluation
2000
1.0 Purpose
The Nuclear Regulatory Commission NRC license for the White Mesa uranium mill
Mill is Performance-Based License PBL The PBL allows International Uranium
USA Corporation IUSA to evaluate and implement certain changes in the licensed
operation without applying for and receiving formal amendment to the NRC license The
following procedure outlines the steps to follow when accepting additional conventional ore
or alternate feed materials to ensure that the currently permitted capacity of the Tailings
Management System is not exceeded This Standard Operating Procedure SOP is as per the
Mills NRC License
2.0 Tailings Capacity Determination Procedure
Whenever the Mill is considering receiving conventional ore le2 material or an alternate
feed the capacity of the Mill Tailings System will have to be determined to ensure that
sufficient volume is available to store the projected incremental volumes of tailings material
as well as the projected volumes of waste material from final reclamation of the Mill facility
based on the approved Reclamation Plan This evaluation will be performed by the Mill
Manager or his designee and approved by the President of IUSA or his designee
The procedure for determining whether there is sufficient capacity is described as follows
and documented on the attached Tailings Capacity Form
2.1 For the first evaluation the base volume BY available will be based on the
capacity stated in the Tailings Capacity Evaluation report submitted to the NRC
May 15 2000 copy of which is attached For each subsequent evaluation the
previous evaluation will produce remaining tailings capacity value which will
become the BY
2.2 Mill Management will maintain Tailings Capacity Evaluation Record TCER
book in which all evaluation forms and supporting calculations will be maintained
Refer to the TECR to obtain the BY value to be used in each subsequent evaluation
2.3 The volume of tailings discharged to the active tailings cells between the date of the
BY and the evaluation date will be estimated based on the Mills production reports
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Files\Content.Outlook\I5CXRH6Z\PBL-3 Tailings Capacity SOP Rev 25
00.docPtdmin4aster SOPsBook 10_PBL SopsPBL 3_Tailings Capacity SOP Seied
9.25.00 Rev 0.doc
No PBL-3 INTERNATIONAL URANIUM USA CORPORATION
Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date September 25 Title Tailings Capacity Evaluation
2000
2.4 The amount of Mill site trash disposed of in the tailings system will be determined
The number of loads of trash hauled between the date of the BY and the evaluation
date will be taken from the Garbage Log
2.5 The amount of 11 e.2 in-situ waste material deposited into the tailings system
between the date of the BY and the evaluation date will be summarized The
quantities of material will be listed by supplier and will be based on the Scale House
Weigh Tickets from each shipment
2.6 The BY minus the quantities in items 2.3 2.4 and 2.5 above will become the current
tailings capacity This number will be used as the BY item 2.1 above for the
subsequent evaluation
2.7 The amount of alternate feed material or conventional ore committed to be processed
and deposited into the tailings system will be summarized The maximum projected
quantities of material will be listed by supplier and stated in dry tons i.e less the
estimated moisture content
2.8 The sum of the quantities estimated in item 2.7 above will be subtracted from the
current tailings capacity calculated in item 2.6 above to determine the remaining
capacity available
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Files\Content.Outlook\15CXRH6PBL-3_Tailings Capacity SOP Rev 25
00.docPtdmin4aster SOPsWook 10_PBL SopsWBL 3_Tailings Capacity SOP Seied
onc fl Day 0.doc
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
WHITE MESA MILL TAILINGS MANAGEMENT SYSTEM
AND
DISCHARGE MINIMIZATION TECHNOLOGY DMT
MONITORING PLAN
INTRODUCTION
This Tailings Management System and Discharge Minimization Technology Monitoring Plan the
Plan for the White Mesa Mill the Mill provides procedures for monitoring of the tailings cell
system as required under State of Utah Radioactive Materials License No UT1900479 the
Radioactive Materials License as well as procedures for operating and maintenance of monitoring
equipment and reporting procedures that are adequate to demonstrate DMT compliance under State
of Utah Ground Water Discharge Permit No 370004 for the Mill the GWDP
This Plan is designed as systematic program for constant surveillance and documentation of the
integrity of the tailings impoundment system including dike stability liner integrity and transport
systems as well as monitoring of water levels in Roberts Pond and feedstock storage areas at the
Mill The Plan requires daily weekly quarterly monthly and annual inspections and evaluations and
monthly reporting to Mill management
DAILY TAILINGS INSPECTIONS
The following daily tailings inspections shall be performed
2.1 Daily Comprehensive Tailings Inspection
On daily basis including weekends all areas connected with the four tailings cells will be
inspected Observations will be made of the current condition of each cell noting any corrective
action that needs to be taken
The Environmental or Radiation Technician is responsible for performing the daily tailings
inspections except on weekends when the Shift Foreman will perform the weekend tailings
inspections The Radiation Safety Officer may designate other individuals with training as
described in Section 2.4 below to perform the daily tailings inspection
Observations made by the inspector will be recorded on the Daily Inspection Data form copy of
which is attached in Appendix The Daily Inspection Data form contains an inspection checklist
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
which includes tailings cells map and spaces to record observations especially those of immediate
concern and those requiring corrective action The inspector will place check by all inspection
items that appear to be operating properly Those items where conditions of potential concern are
observed should be marked with an note should accompany the specifying what the
concern is and what corrective measures will resolve the problem This observation of concern
should be noted on the form until the problem has been remedied The date that corrective action
was taken should be noted as well
Areas to be inspected include the following Cell and 4A Dikes 4A-S and 4A-W
wind movement of tailings effectiveness of dust minimization methods spray evaporation Cell
spillway Cell spillway Cell and 4A liquid pools and associated liquid return equipment cell
leak detection systems and the wildlife ponds
Operational features of the tailings area are checked for conditions of potential concern The
following items require visual inspection during the daily tailings inspection
Tailings slurry and SX raffinate transport systems from the Mill to the active
disposal cells and pool return pipeline and pumps
Daily inspections of the tailings lines are required to be performed when the Mill
is operating The lines to be inspected include the tailings slurry lines from CCD
to the active tailings cell SX raffinate lines that can discharge into Cell Cell
or Cell 4A the pond return line from the tailings area to the Mill and lines
transporting pond solutions from one cell to another
Cell
Cell
Cell
Cell 4A
Dike structures including dikes 4A-S and 4A-W
The Cell spillway Cell spillway Cell and Cell 4A liquid pools and
associated liquid return equipment
Presence of wildlife and/or domesticated animals in the tailings area including
waterfowl and burrowing animal habitations
Spray evaporation pumps and lines
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
Wind movement of tailings and dust minimization
Wind movement of tailings will be evaluated for conditions which may require
initiation of preventative dust minimization measures for cells containing tailings
sand During tailings inspection general surface conditions will be evaluated for
the following areas of tailings subject to blowing and/or wind movement
liquid pool size areas not subject to blowing and/or wind movement
expressed as percentage of the total cell area The evaluations will he reviewed
on weekly basis or more frequently if warranted and will be used to direct dust
minimization activities
Observation of flow and operational status of the dust control/spray evaporation
systems
Observations of any abnormal variations in tailings pond elevations in Cells 13
and4A
Locations of slurry and SX discharge within the active cells Slurry and SX
discharge points need to be indicated on the tailings cells map included in the
Daily Inspection Data form
An estimate of flow for active tailings slurry and SX lines
An estimate of flow in the solution return lines
Daily measurements in the leak detection system LDS sumps of the tailings
cells will be made when warranted by changes in the solution level of the
respective leak detection system
The trigger for further action when evaluating the measurements in the Cell and
Cell leak detection systems is gain of more than 12 inches in 24 hours The
solution level in Cell 4A leak detection is not allowed to be more than 1.0 foot
above the lowest point on the bottom flexible membrane liner elevation 5556.14
feet amsl If any of these observation are made the Mill Manager should be
notified immediately and the leak detection system pump started
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
Whenever the leak detection system pump is operating and the flow meter
total izer is recording notation of the date and the time will be recorded on the
Daily Inspection Data form This data will be used in accordance with License
Condition 1.3.B through 1.3.E of the Mills Radioactive Materials License to
determine whether or not the flow rate into the leak detection system is in excess
of the License Conditions
An estimate of the percentage of the tailings beach surface area and solution pool
area is made including estimates of solutions cover areas and tailings sands for
Cells and 4A
Items and are to be done only when the Mill is operating When the Mill is down
these items cannot be performed
2.2 Daily Operations Inspection
During Mill operation the Shift Foreman or other person with the training specified in Section 2.4
below designated by the Radiation Safety Officer will perform an inspection of the tailings line and
tailings area at least once per shift paying close attention for potential leaks and to the discharges
from the pipelines Observations by the Inspector will be recorded on the appropriate line on the
Operating Foremans Daily Inspection form
2.3 Daily Operations Patrol
In addition to the inspections described in Sections 2.1 and 2.2 above Mill employee will patrol
the tailings area at least twice per shift during Mill operations to ensure that there are no obvious
safety or operational issues such as leaking pipes or unusual wildlife activity or incidences
No record of these patrols need be made but the inspectors will notify the Radiation Safety Officer
and/or Mill management in the event that during their inspection they discover that an abnormal
condition or tailings emergency has occurred
2.4 Training
All individuals performing inspections described in Sections 2.1 and 2.2 above must have Tailings
Management System training as set out in the Tailings Inspection Training procedure which is
attached as Appendix This training will include training pack explaining the procedure for
performing the inspection and addressing inspection items to be observed In addition each
individual after reviewing the training pack will sign certification form indicating that training
has been received relative to his/her duties as an inspector
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
2.5 Tailings Emergencies
Inspectors will notify the Radiation Safety Officer and/or Mill management immediately if during
their inspection they discover that an abnormal condition exists or an event has occurred that could
cause tailings emergency Until relieved by the Environmental or Radiation Technician or
Radiation Safety Officer inspectors will have the authority to direct resources during tailings
emergencies
Any major catastrophic events or conditions pertaining to the tailings area should be reported
immediately to the Mill Manager or the Radiation Safety Officer one of whom will notify Corporate
Management If dam failure occurs notify your supervisor and the Mill Manager immediately The
Mill Manager will then notify Corporate Management MSFIA 303-231-5465 and the State of
Utah Division of Dam Safety 801-538-7200
WEEKLY TAILINGS AND DMT INSPECTION
3.1 Weekly Tailings Inspections
Weekly tailings inspections are to be conducted by the Radiation Safety Department and include the
following
Leak Detection Systems
Each tailings cells leak detection system shall be checked weekly to determine
whether it is wet or dry If marked wet the liquid levels need to be measured and
reported In Cell and Cell the leak detection system is measured by use of
pipe that is removed from the system which will indicate the presence of
solutions in the LDS system The Cell 4A leak detection system is monitored on
continuous basis by use of pressure transducer that feeds water level
information to an electronic data collector The pressure transducer is calibrated
for fluid with specific gravity of 1.0 The water levels are measured every hour
and the information is stored for later retrieval The water levels are measured to
the nearest 0.10 inch The data collector is currently programmedto store days
of water level information The number of days of stored data can be increased
beyond days if needed The water level data is downloaded to laptop
computer on weekly basis and incorporated into the Mills environmental
monitoring data base and into the files for weekly inspection reports of the
tailings cell leak detection systems
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
If sufficient fluid is present in the leak detection system of any cell the fluid shall
be pumped from the LDS to the extent reasonably possible and record the
volume of fluid recovered Any fluid pumped from an LDA shall be returned to
disposal cell
If fluid is pumped from an LDS the flow rate shall be calculated by dividing the
recorded volume of fluid recovered by the elapsed time since fluid was last
pumped or increases in the LDS fluid levels were recorded whichever is the
more recent This calculation shall be documented as part of the weekly
inspection
Upon the initial pumping of fluid from an LDS fluid sample shall be collected
and analyzed in accordance with paragraph 11.3 of the Radioactive Materials
License
For Cell 4A under no circumstance shall fluid head in the leak detection
system sump exceed 1-foot level above the lowest point in the lower flexible
membrane liner To determine the Maximum Allowable Daily LDS Flow
Rates in the Cell 4A leak detection system the total volume of all fluids
pumped from the LDS on weekly basis shall be recovered from the data
collector and that information will be used to calculate an average volume
pumped per day Under no circumstances shall the daily LDS flow volume
exceed 24160 gallons/day The maximum daily LDS flow volume will be
compared against the measured cell solution levels detailed on Table in
Appendix to determine the maximum daily allowable LDS flow volume for
varying head conditions in Cell 4A
Slimes Drain Water Level Monitoring
Cell is an active tailings cell while Cell is partially reclaimed with approximately
90%of the surface covered by platform fill Each cell has slimes drain system
which aids in dewatering the slimes and sands placed in the cell
ii Cell has pump placed inside of the slimes drain access pipe at the bottom of the
slimes drain As taken from actual measurements the bottom of the slimes drain is
38 feet below water level measuring point at the centerline of the slimes drain
access pipe at the ground surface level This means that the bottom of the slimes
drain pool and the location of the pump are one foot above the lowest point of the
FML in Cell which based on construction reports is at depth of 39 feet below
the water level measuring point on the slimes drain access pipe for Cell
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
iiiThe slimes drain pump in Cell is on timed system under which it pumps for 15
minutes each hour thereby allowing the slimes wastewater to recharge for 45
minutes before being pumped again Based on measurements
taken in August 2006
the water level in the Cell slimes drain recharges to depth of about 28.50 feet
before each pumping and is pumped to depth of 38 feet after each pumping in each
case measured below the water level measuring point on the slimes drain access pipe
The average wastewater head in the Cell slimes drain is therefore about feet The
depth to water of about 28.50 feet after recharge is below the phreatic surface of
tailings Cell which is at depth of about 20 feet below the water level measuring
point on the slimes drain access pipe As result there is continuous flow of
wastewater from Cell into the slimes drain collection system Mill management
considers that the average allowable wastewater head in the Cell slimes drain
resulting from pumping at these intervals is satisfactory and is as low as reasonably
achievable Based on past experience cycling the pump morethan 15 minutes every
hour can result in more replacement costs for pumps and more resulting system
downtime
ivThe Cell slimes drain pump is checked weekly to observe that it is operating and
that the timer is set properly which is noted on the Weekly Tailings Inspection Form
If at any time the pump is observed to be not working properly it will be fixed or
replaced within 15 days
Depth to wastewater in the Cell slimes drain access pipe shall be monitored and
recorded weekly to determine maximum and minimum fluid head before and after
pumping cycle respectively All head measurements must be made from the same
measuring point the notch at the north side of the access pipe and made to the
nearest 0.01 foot The results will be recorded as depth-in-pipe measurements on the
Weekly Tailings Inspection Form
viOn monthly basis the slimes drain pump will be turned off and the wastewater in
the slimes drain access pipe will be allowed to stabilize for at least 90 hours Once
the water level has stabilized based on no change in water level for three
successive readings taken no less than one hour apart the water level of the
wastewater will be measured and recorded as depth-in-pipe measurement on the
Monthly Inspection Data form by measuring the depth to water below the water level
measuring point on the slimes drain access pipe
vii No process liquids shall be allowed to be discharged into Cell
viii If at any time the most recent average annual head in the Cell slimes drain is
found to have increased above the average head for the previous calendar year the
Licensee will comply with the requirements of Part I.G.3 of the GWDP including the
requirement to provide notification to the Executive Secretary orally within 24 hours
followed by written notification
ixBecause Cell and Cell 4A are currently active no pumping from the Cell or Cell
4A slimes drain is authorized Prior to initiation of tailings dewatering operations for
Cell or Cell 4A similar procedure will be developed for ensuring that average
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
head elevations in the Cell and Cell 4A slimes drains are kept as low as reasonably
achievable and that the Cell and Cell 4A slimes drains are inspected and the results
reported in accordance with the requirements of the permit
Wind Movement of Tailings
An evaluation of wind movement of tailings or dusting and control measures
shall be taken if needed
Tailings Wastewater Pool Elevation Monitoring
Solution elevation measurements in Cells and 4A and Roberts Pond are to be taken by
survey on weekly basis as follows
The survey will be performed by the Mills Radiation Safety Officer or designee
the Surveyor with the assistance of another Mill worker the Assistant
ii The survey will be performed using survey instrument the Survey Instrument
accurate to 0.01 feet such as Sokkai No B21 or equivalent together with
survey rod the Survey Rod having visible scale in 0.01 foot increments
iiiThe reference Points the Reference Points for Cells and 4A and Roberts
Pond are known points established by professional survey For Cell and Roberts
Pond the Reference Point is wooden stake with metal disk on it located on the
southeast corner of Cell The elevation of the metal disk the Reference Point
Elevation for Cell and Roberts Pond is at 5623.14 feet above mean sea level
FMSL For Cell and cell 4A the Reference Point is piece of metal rebar
located on the south dike of Cell The elevation at the top of this piece of rebar
the Reference Point Elevation for Cell and cell 4A is at 5607.83 FMSL
iv The Surveyor will set up the Survey Instrument in location where both the
applicable Reference Point and pond surface are visible For Cell and Roberts
Pond this is typically on the road on the Cell south dike between Cell and
Roberts Pond approximately 100 feet east of the Cell 1/Roberts Pond Reference
Point For Cell and Cell 4A this is typically on the road on the Cell dike
approximately 100 feet east of the Cell Reference Point
Once in location the Surveyor will ensure that the Survey Instrument is level by
centering the bubble in the level gauge on the Survey Instrument
viThe Assistant will place the Survey Rod vertically on the Reference Point on the
metal disk on the Cell 1/Roberts Pond Reference Point and on the top of the rebar
on the Cell and cell 4A Reference Point The Assistant will ensure that the
Survey Rod is vertical by gently rocking the rod back and forth until the Surveyor
has established level reading
vii The Surveyor will focus the cross hairs of the Survey Instrument on the scale on
the Survey Rod and record the number the Reference Point Reading which
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page of 36
represents the number of feet the Survey Instrument is reading above the
Reference Point
viii The Assistant will then move to designated location where the Survey Rod can
be placed on the surface of the main solution pond in the Cell or Roberts Pond as
the case may be These designated locations and the methods to be used by the
Assistant to consistently use the same locations are as follows
Cell
stake has been place in the central area of the south dike of Cell The
Assistant will walk perpendicular to the dike from the stake to the nearest point
on the liquid surface of Cell and place the Survey Rod at that location
Ce114A
The Assistant will walk down the slope in the northeast corner of Cell 4A and
place the Survey Rod at the liquid level
Cell
mark has been painted on the north side of the ramp going to the pump
platform in Cell The Assistant will place the Survey Rod against that mark
and hold the rod vertically with one end just touching the liquid surface and
Roberts Pond
mark has been painted on the railing of the pump stand in Roberts Pond The
Assistant will place the Survey Rod against that mark and hold the rod
vertically with one end just touching the liquid surface
Based on the foregoing methods the approximate coordinate locations for the
measuring points for Roberts Pond and the Cells are
Northing Easting
Roberts Pond 323041 2579697
Cell 322196 2579277
Cell 320508 2577760
Cell 4A 320300 2579360
These coordinate locations may vary somewhat depending on solution elevations
in the Pond and Cells
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 10 of 36
ixThe Assistant will hold the Survey Rod vertically with one end of the Survey Rod
just touching the pond surface The Assistant will ensure that the Survey Rod is
vertical by gently rocking the rod back and forth until the Surveyor has established
level reading
The Surveyor will focus the cross hairs of the Survey Instrument on the scale on
the Survey Rod and record the number the Pond Surface Reading which
represents the number of feet the Survey Instrument is reading above the pond
surface level
The Surveyor will calculate the elevation of the pond surface as FSML by adding the
Reference Point Reading for the Cell or Roberts Pond as the case may be to the Reference
Point Elevation for the Cell or Roberts Pond and subtracting the Pond Surface Reading for
the Cell or Roberts Pond and will record the number accurate to 0.01 feet
Summary
In addition the weekly inspection should summarize all activities concerning the
tailings area for that particular week
Results of the weekly tailings inspection are recorded on the Weekly Tailings and DMT Inspection
form An example of the Weekly Tailings and DMT Inspection form is provided in Appendix
3.2 Weekly Inspection of Solution Levels in Roberts Pond
On weekly basis solution elevations are taken on Roberts Pond in accordance with the procedures
set out in Section 3.1 above The Weekly solution level in Roberts Pond is recorded on the
Weekly Tailings and DMTlnspection form Based on historical observations the FML at the Pond
Surface Reading area for Roberts Pond is approximately six inches above the lowest point on the
pond sFML If the pond solution elevation at the Pond Surface Reading area is at or below the Fls/IL
for that area the pond will be recorded as being dry
3.3 Weekly Feedstock Storage Area Inspections
Weekly feedstock storage area inspections will be performed by the Radiation Safety Department to
confirm that
the bulk feedstock materials are stored and maintained within the defined area described in
the GWDP as indicated on the map attached hereto as Appendix and
all alternate feedstock located outside the defined Feedstock Area are maintained within
water tight containers
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison6
Book 11 Environmental Protection Manual Section 3.1 Page 11 of 36
The results of this inspection will be recorded on the Ore Storage/Sample Plant Weekly Inspection
Report copy of which is contained in Appendix Any variance in stored materials from this
requirement or observed leaking alternate feedstock drums or other containers will be brought to the
attention of Mill Management and rectified within 15 days
MONTHLY TAILINGS INSPECTION
Monthly tailings inspections will be performed by the Radiation Safety Officer or his designee from
the Radiation Safety Department and recorded on the Monthly Inspection Data form an example of
which is contained in Appendix Monthly inspections are to be performed no sooner than 14 days
since the last monthly tailings inspection and can be conducted concurrently with the quarterly
tailings inspection when applicable The following items are to be inspected
Tailings Slurry Pipeline
When the Mill is operating the slurry pipeline will be inspected at key locations to
determine pipe wear Pipe thickness will be measured using an ultrasonic device by
either the radiation safety staff or other trained designees The critical points of the
pipe include bends slope changes valves and junctions which are critical to dike
stability These locations to be monitored will be determined by the Radiation Safety
Officer or his designee from the Radiation Safety Department during the Mill run
Diversion Ditches
Diversion ditches and shall be monitored monthly for sloughing erosion
undesirable vegetation and obstruction of flow Diversion berm should be checked
for stability and signs of distress
Sedimentation Pond
Activities around the Mill and facilities area sedimentation pond shall be summarized
for the month
Overspray Dust Minimization
The inspection shall include an evaluation of overspray minimization if applicable
This entails ensuring that the overspray system is functioning properly In the event
that overspray is carried more than 50 feet from the cell the overspray system should
be immediately shut-off
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison
Book 11 Environmental Protection Manual Section 3.1 Page 12 of 36
Remarks
section is included on the Monthly Inspection Data form for remarks in which
recommendations can be made or observations of concern can be documented
Summary ofDaily Weekly and Quarterly Inspections
The monthly inspection will also summarize the daily weekly and if applicable
quarterly tailings inspections for the specific month
In addition settlement monitors are typically surveyed monthly and the results reported on the
Monthly Inspection Data form
QUARTERLY TAILINGS INSPECTION
The quarterly tailings inspection is performed by the Radiation Safety Officer or his designee from
the Radiation Safety Department having the training specified in Section 2.4 above once per
calendar quarter quarterly inspection should be performed no sooner than 45 days since the
previous quarterly inspection was performed
Each quarterly inspection shall include an Embankment Inspection an Operations/Maintenance
Review Construction Review and Summary as follows
Embankment Inspection
The Embankment inspection involves visual inspection of the crest slope and toe
of each dike for movement seepage severe erosion subsidence shrinkage cracks
and exposed liner
Operations/Maintenance Review
The Operations/Maintenance Review consists of reviewing Operations and
Maintenance activities pertaining to the tailings area on quarterly basis
Construction Review
The Construction Review consists of reviewing any construction changes or
modifications made to the tailings area on quarterly basis
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 13 of 36
Summary
The summary will include all major activities or observations noted around the
tailings area on quarterly basis
If any of these conditions are noted the conditions and corrective measures taken should be
documented in the Quarterly Inspection Data form An example of the Quarterly Inspection Data
form is provided in Appendix
ANNUAL EVALUATIONS
The following annual evaluations shall be performed
6.1 Annual Technical Evaluation
An annual technical evaluation of the tailings management system is performed by registered
professional engineer PE who has experience and training in the area of geotechnical aspects of
retention structures The technical evaluation includes an on-site inspection of the tailings
management system and thorough review of all tailings records for the past year The Technical
Evaluation also includes review and summary of the annual movement monitor survey see Section
5.2 below
All tailings cells and corresponding dikes will be inspected for signs of erosion subsidence
shrinkage and seepage The drainage ditches will be inspected to evaluate surface water control
structures
In the event tailings capacity evaluations as per SOP PBL-3 were performed for the receipt of
alternate feed material during the year the capacity evaluation forms and associated calculation
sheets will be reviewed to ensure that the maximum tailings capacity estimate is accurate The
amount of tailings added to the system since the last evaluation will also be calculated to determine
the estimated capacity at the time of the evaluation
Tailings inspection records will consist of daily weekly monthly and quarterly tailings inspections
These inspection records will be evaluated to determine if any freeboard limits are being
approached Records will also be reviewed to summarize observations of potential concern The
evaluation also involves discussion with the Environmental and/or Radiation Technician and the
Radiation Safety Officer regarding activities around the tailings area for the past year During the
annual inspection photographs of the tailings area will be taken The training of individuals will be
reviewed as part of the Annual Technical Evaluation
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 14 of 36
The registered engineer will obtain copies of selected tailings inspections along with the monthly
and quarterly summaries of observations of concern and the corrective actions taken These copies
will then be included in the Annual Technical Evaluation Report
The Annual Technical Evaluation Report must be submitted by September 1st of every year to
Directing Dam Safety Engineer
State of Utah Natural Resources
1636 West North Temple Suite 220
Salt Lake City Utah 84116-3156
6.2 Movement Monitors
movement monitor survey is to be conducted by licensed surveyor annually during
the second
quarter of each year The movement monitor survey consists of surveying monitors along dikes 3-S
4A-W and 4A-S to detect any possible settlement or movement of the dikes The data generated
from this survey is reviewed and incorporated into the Annual Technical Evaluation Report of the
tailings management system
6.3 Freeboard Limits
Tailings Cells and 4A
The freeboard limits are as per January 10 1990 Drainage Report for Cells
and 4A and are stated below
liquid maximum elevation of 5615.4 feet mean sea level in Cell
ii liquid maximum elevation of 5596.4 feet mean sea level in Cell 4A
Tailings Cell
The freeboard limit for Cell is determined annually using the following
procedure
From survey of Cell the pool surface will be determined
ii An estimate of the maximum tons of dry tailings to be generated during
the next 12 months will be made This estimate is multiplied by 1.5
factor of safety to yield the Maximum Mill Production
iii The Maximum Mill Production is divided by the number of tons required
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 15 of 36
to reduce the pooi size by one acre and then subtracted from the pool
surface determined in Step yielding the Reduced Pool Area
iv The PMP Flood Volume Requirement as per the January 10 1990
Drainage Report is 123.4 acre feet The PMP Flood Volume
Requirement is divided by the Reduced Pool Area to determine the PMP
Freeboard Level
The Wave Run Up of 0.78 feet as specified in the January 10 1990
Drainage Report is added to the PMP Freeboard Level to determine the
Total Required Freeboard
The calculation of the Total Required Freeboard for Cell will be calculated
annually and the calculation sheet filed in the Mill Central File
Tailings Cell 4A
The freeboard limit for Cell 4A is determined annually using the following
procedure
The Cell 4A design includes concrete spillway between Cell and Cell 4A
with the invert elevation feet below the top of the Cell dike at an elevation
of 5604.5 feet amsl Should Cell receive the full PMP volume of 123.4 acre
feet of water approximately 62 acre feet of that volume would flow through
the spillway into Cell 4A
The flood volume from the PMP event over the Cell 4A area is 36 acre-feet of
water 40 acres plus the adjacent drainage area of 3.25 acres times the PMP of
10 inches This would result in total flood volume of 98 acre-feet including
the 62 acre-feet of solution from Cell The freeboard depth required for Cell
4A from the PMP event would be 2.44 feet plus wave run-up depth of 0.77 feet
from the 1990 Drainage Report for total freeboard requirement of 3.2 feet
This calculation is illustrated on Attachment The Groundwater Quality
Discharge Permit No UGW370004 for the White Mesa Mill requires that the
minimum freeboard be no less than 3.0 feet for any of the existing Cell
construction but based on the above calculation the freeboard would be set 3.2
feet below the top of liner The freeboard for Cell 4A would therefore be 5595.3
amsl top of liner 5598.5 3.2 feet
The calculation of the Total Required Freeboard for Cell 4A will be calculated
annually and the calculation sheet filed in the Mill Central File
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 16 of 36
Roberts Pond
The freeboard limit for Roberts Pond is liquid maximum elevation of 5624.0
feet above mean sea level as specified in the GWDP
6.4 Annual Leak Detection Fluid Samples
In the event solution has been detected in leak detection system sample will be collected on an
annual basis This sample will be analyzed according to the conditions set forth in License
Condition 11.3 .C The results of the analysis will be reviewed to determine the origin of the
solution
OTHER INSPECTIONS
All daily weekly monthly quarterly and annual inspections and evaluations should be performed as
specified in Sections and above However additional inspections should be conducted
after any significant storm or significant natural or man-made event occurs
REPORTING REQUIREMENTS
In addition to the Daily Inspection Data Weekly Tailings Inspection Monthly Inspection Data and
Quarterly Inspection Data forms included as Appendix and described in Sections and
respectively and the Operating Foremans Daily Inspection and Weekly Mill Inspection forms
described in Sections and respectively the following additional reports shall also be prepared
8.1 Monthly Tailings Reports
Monthly tailings reports are prepared every
month and summarize the previous months activities
around the tailings area If not prepared by the Radiation Safety Officer the report shall be
submitted to the Radiation Safety Officer for review The Mill Manager will review the report as
well before the report is filed in the Mill Central File The report will contain summary of
observations of concern noted on the daily and weekly tailings inspections Corrective measures
taken during the month will be documented along with the observations where appropriate All daily
and weekly tailings inspection forms will be attached to the report monthly inspection form will
also be attached Quarterly inspection forms will accompany the report when applicable The report
will be signed and dated by the preparer in addition to the Radiation Safety Officer and the Mill
Manager
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 17 of 36
8.2 DMT Reports
Quarterly reports of DMT monitoring activities of all required information required by Part .F.2 of
the GWDP relating to the inspections described in Section 3.1b limes Drain Water Level
Monitoring 3.1d Tailings Wastewater Pool Elevation Monitoring 3.2 Weekly Inspection of
Solution Levels in Roberts Pond and 3.3 Weekly Feedstock Storage Area Inspections will be
provided to the Executive Secretary on the schedule provided in Table of the GWDP An annual
summary and graph for each calendar year of the depth to wastewater in the Cell slimes drain must
be included in the fourth quarter report After the first year and beginning in 2008 quarterly reports
shall include both the current year monthly values and graphic comparison to the previous year
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 18 of 36
APPENDIX
FORMS
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White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 23 of 36
APPENDIX CONT
DENISON MINES USA CORP
WEEKLY TAILINGS INSPECTION
Date____________________Inspectors
Pond elevations mslft Cell Pond Solution Elevation _________________
FML Bottom Elevation 5597
Depth of Water above FML a-b ________________
Cell aPond Solution Elevation _________________
bFML Bottom Elevation 5570
cDepth of Water above FML a-b ________________
Cell 4A aPond Solution Elevation _______________
bFML Bottom Elevation ______5564
cDepth of Water above FML a-b_______________
Roberts
Pond aPond Solution Elevation _______________
bFML Bottom Elevation 5612.34
cDepth of Water above FML a-b ________________
Slimes Drain Liquid Levels Cell Pump functioning properly
Pump Timer set at 15mm on 45 mm off
Depth to Liquid pre-pump
Depth to Liquid Post-pump
all measurements are depth-in-pipe
Pre-pump head is 38-Depth to Liquid Pre-pump
Post-pump head is 38 Depth to Liquid Post-
pump _____
White Mesa Mill Standard Operating Procedures
Book 11 Enviromnental Protection Manual Section 3.1
Leak Detection Systems
9/08 Revision Denison-6
Page 24 of 36
Cell Cell Cell Ce1I4A
Observation
Is LDS wet or dry wet__dry wet__dry wet__dry wet__dry
If wet Record
liquid level
to
Liquid
to
Liquid
to
Liquid
to
Liquid
If sufficient fluid is
present record
volume of fluid
pumped and flow
rate
Volume
Flow Rate_______
Volume
Flow Rate_______
Volume
Flow Rate_______
Volume
Flow Rate______
Was fluid sample
collected
Tailings Area Inspection Note dispersal of blowing tailings
Control Methods Implemented
Remarks
Contaminated Waste Dump
Does Level exceed 12 inches above the lowest point on the bottom flexible membrane liner elevation
5556.14 amsl _____no _____yes
If Cell 4A leak detection system level exceeds 12 inches above the lowest point on the bottom flexible
membrane liner elevation 5556.14 amsl notify supervisor or Mill manager immediately
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 25 of 36
APPENDIX CONT
MONTHLY INSPECTION DATA
Inspector
Date ___________________________________
Slurry Pipeline
Pipe Thickness To be measured only during periods when the Mill is operating
Diversion Ditches and Diversion Berm
Observation
Diversion Ditch Diversion Ditch Diversion Ditch Diversion Berm
Diversion Ditches
Sloughing yes no _____yes no _____yes no
Erosion _____yes no _____yes no _____yes no
Undesirable _____yes no _____yes no _____yes no
Vegetation
Obstruction of Flow _____yes no _____yes no _____yes no
Diversion Berm
Stability Issues _____yes no
Signs of Distress _____yes no
Comments
Summary of Activities Around Sedimentation Pond _________________________________
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 26 of 36
Overspray Dust Minimization
Overspray system functioning properly yes no
Overspray carried more than 50 feet from the cell _____yes no
If yes was system immediately shut off ______yes no
Comments
Remarks
Settlement Monitors
Cell Wi _____________Cell 2W3-S _____________Cell 3-iN ______________
Cell W2 _____________Cell 2Ei-N _____________Cell 3-iC ______________
Cell W3 _____________Cell 2Ei-iS _____________Cell 3-iS ______________
Cell W4 ____________Cell 2Ei-2S _____________Cell 3-2N ______________
Cell 2W7-C _____________Cell East _____________Cell 2W5-N ____________
Cell W7N ____________Cell W7S ____________Cell W6N ___________
Cell W6C ____________Cell W65 ____________Cell W4N ___________
Cell 4A-Toe ___________Cell W4S ____________Cell W5C ___________
Cell 3-2C Cell 3-2S
Summary of Daily Weekly and Quarterly Inspections
Monthly Silmes Drain Static Head Measurement for Cell Depth-in-Pipe Water Level
Reading ___________________
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 27 of 36
APPENDIX CONT
WHITE MESA MILL
TAILINGS MANAGEMENT SYSTEM
QUARTERLY INSPECTION DATA
Inspector
Date __________________________
Embankment Inspection
Operations/Maintenance Review
Construction Activites
Summary
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 28 of 36
APPENDIX CONT
ORE STORAGE/SAMPLE PLANT WEEKLY INSPECTION REPORT
Week of _________through _________Date of Inspection
Inspector
Weather conditions for the week
Blowing dust conditions for the week
Corrective actions needed or taken for the week
Are all bulk feedstock materials stored in the area indicated on the attached diagram
yes no________
comments
Are all alternate feedstock materials located outside the area indicated on the attached diagram maintained
within water-tight containers
yes_______no_______
comments e.g conditions of containers_________________________________________
Conditions of storage areas for materials
Other comments
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 29 of 36
APPENDIX
TAILINGS INSPECTOR TRAINING
This document provides the training necessary for qualifying management-designated individuals for
conducting daily tailings inspections Training information is presented by the Radiation Safety
Officer or designee from the Environmental Department Daily tailings inspections are conducted in
accordance with the White Mesa Mill Tailings Management System and Discharge Minimization
Technology DMT Monitoring Plan The Radiation Safety Officer or designee from the Radiation
Safety Department is responsible for performing monthly and quarterly tailings inspections Tailings
inspection forms will be included in the monthly tailings inspection reports which summarize the
conditions activities and areas of concern regarding the tailings areas
Notifications
The inspector is required to record whether all inspection items are normal satisfactory requiring no
action or that conditions of potential concern exist requiring action check mark indicates no
action required if conditions of potential concern exist the inspector should mark an in the area
the condition pertains to note the condition and specify the corrective action to be taken if an
observable concern is made it should be noted on the tailings report until the corrective action is
taken and the concern is remedied The dates of all corrective actions should be noted on the reports
as well
Any major catastrophic events or conditions pertaining to the tailings area should be reported
immediately to the Mill Manager or the Radiation Safety Officer one of whom will notify Corporate
Management if dam failure occurs notify your supervisor and the Mill Manager immediately The
Mill Manager will then notify Corporate Management MSHA 303-231-5465 and the State of
Utah Division of Dam Safety 801-538-7200
Inspections
All areas of the tailings disposal system are routinely patrolled and visible observations are to be
noted on daily tailings inspection form Refer to Appendix for an example of the daily tailings
inspection form The inspection form consists of three pages and is summarized as follows
Tailings Slurry Transport System
The slurry pipeline is to be inspected for leaks damage and sharp bends The pipelinejoints
are to be monitored for leaks and loose connections The pipeline supports are to be
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 30 of 36
inspected for damage and loss of support Valves are also to be inspected particularly for
leaks blocked valves and closed valves Points of discharge need to be inspected for
improper location and orientation
Operational Systems
Operating systems including water levels beach liners and covered areas are items to be
inspected and noted on the daily inspection forms Sudden changes in water levels
previously observed or water levels exceeding the operating level of pond are potential
areas of concern and should be noted Beach areas that are observed as having cracks severe
erosion or cavities are also items that require investigation and notation on daily forms
Exposed liner or absence of cover from erosion are potential items of concern for ponds and
covered areas These should also be noted on the daily inspection form
Cells and 4A solution levels are to be monitored closely for conditions nearing
maximum operating level and for large changes in the water level since the last inspection
All pumping activities affecting the water level will be documented In Cells and the
PVC liner needs to be monitored closely for exposed liner especially after storm events It is
important to cover exposed liner immediately as exposure to sunlight will cause degradation
of the PVC liner Small areas of exposed liner should be covered by hand Large sections of
exposed liner will require the use of heavy equipment
These conditions are considered serious and require immediate action After these conditions
have been noted to the Radiation Safety Officer work order will be written by the
Radiation Safety Officer and turned into the Maintenance Department All such repairs
should be noted in the report and should contain the start and finish date of the repairs
Dikes and Embankments
Inspection items include the slopes and the crests of each dike For slopes areas of concern
are sloughs or sliding cracks bulges subsidence severe erosion moist areas and areas of
seepage outbreak For crests areas of concern are cracks subsidence and severe erosion
When any of these conditions are noted an mark should be placed in the section marked
for that dike
In addition the dikes in particular dikes 4A-S and 4A-W should be inspected closely for
mice holes and more importantly for prairie dog holes as the prairie dogs are likely to
burrow in deep possibly to the liner If any of these conditions exist the inspection report
should be marked accordingly
Flow Rates
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 31 of 36
Presence of all flows in and out of the cells should be noted Flow rates are to be estimated
in gallons per minute GPM Rates need to be determined for slurry lines pond return SX
tails and the spray system During non-operational modes the flow rate column should be
marked as The same holds true when the spray system is not utilized
Physical Inspection of Slurry Lines
physical inspection of all slurry lines has to be made every hours during operation of the
mill If possible the inspection should include observation of the entire discharge line and
discharge spill point into the cell If fill to elevation flags are in place the tailings and
build-up is to be monitored and controlled so as to not cover the flags
Dust Control
Dusting and wind movement of tailings should be noted for Cells and 4A Other
observations to be noted include brief description of present weather conditions and
record of any precipitation received Any dusting or wind movement of tailings should be
documented In addition an estimate should be made for wind speed at the time of the
observed dusting or wind movement of tailings
The Radiation Safety Department measures precipitation on daily basis Daily
measurements should be made as near to 800 a.m as possible every day Weekend
measurements will be taken by the Shifter as close to 800 a.m as possible All snow or ice
should be melted before reading is taken
Observations of Potential Concern
All observations of concern during the inspection should be noted in this section Corrective
action should follow each area of concern noted All work orders issued contacts or
notifications made should be noted in this section as well It is important to document all
these items in order to assure that the tailings management system records are complete and
accurate
Map of Tailings Cells
The last section of the inspection involves drawing as accurately as possible the following
items where applicable
Cover area
Beach/tailing sands area
Solution as it exists
Pump lines
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 32 of 36
Activities around tailings cell i.e hauling trash to the dump liner repairs etc
Slurry discharge when operating
Over spray system when operating
Safety Rules
All safety rules applicable to the mill are applicable when in the tailings area These rules
meet the required MSI-IA regulations for the tailings area Please pay particular notice to the
following rules
The posted speed limit for the tailings area is 15 mph and should not be exceeded
No food or drink is permitted in the area
All personnel entering the tailings area must have access to two-way radio
Horseplay is not permitted at any time
Only those specifically authorized may operate motor vehicles in the restricted area
When road conditions are muddy or slick four-wheel drive vehicle is required in the
area
Any work performed in which there is danger of falling or slipping in the cell will
require the use of safety belt or harness with attended life line and an approved life
jacket portable eyewash must be present on site as well
Anytime the boat is used to perform any work an approved lifejacket and goggles must
be worn at all times There must also be an approved safety watch with two-way hand-
held radio on shore portable eyewash must be present on site as well
10 Preservation of Wildlife
Every effort should be made to prevent wildlife and domesticated animals from entering the
tailings area All wildlife observed should be reported on the Wildlife Report Worksheet
during each shift Waterfowl seen near the tailings cells should be discouraged from landing
by the use of noisemakers
11 Certification
Following the review of this document and on-site instruction on the tailings system
inspection program designated individuals will be certified to perform daily tailings
inspections The Radiation Safety Officer authorizes certification Refer to the Certification
Form Appendix This form should be signed and dated only after thorough review of the
tailings information previously presented The form will then be signed by the Radiation
Safety Officer and filed
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Enviromnental Protection Manual Section 3.1 Page 33 of 36
APPENDIX
CERTIFICATION FORM
Date _____________________________
Name ______________________________
have read the document titled Tailings Management System White Mesa Mill Tailings
Inspector Training and have received on-site instruction at the tailings system This instruction
included documentation of daily tailings inspections analysis of potential problems dike
failures unusual flows notification procedures and safety
Signature
certify that the above-named person is qualified to perform the daily inspection of the tailings
system at the White Mesa Mill
Radiation Safety Personnel Tailings System
Supervisor
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 34 of 36
APPENDIX
FEEDSTOCK STORAGE AREA
5\BM\US Projocts\Chloroform\dwg\Whito F4cx 2004 Ore Pad.dwg fed ag ir GOal Ip 00103/2U0o PM
Xerox 03545 P5.pc3 Loiter
International Uranium USA Corporation
Project WHITE MESA MILL
REVISIONS
2S2L
County Sate Utah
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Feedstock Storage Area Map
Scale N/A Oate 08/03/2006 Iwh_m_200Core_po
Author unknown WreSted By brn
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 35 of 36
APPENDIX
TABLES
White Mesa Mill Standard Operating Procedures 9/08 Revision Denison-6
Book 11 Environmental Protection Manual Section 3.1 Page 36 of 36
Table
Calculated Action leakage Rates
for Various head Conditions
Cell 4A White mesa Mill
landing Utah
Head above Liner System feet Calculated Action leakage Rate
gallons acre day
222.04
10 314.01
15 384.58
20 444.08
25 496.50
30 543.88
35 587.46
37 604.01
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page of 21
RESPIRATORY PROTECTION PROGRAM
Table of Contents
1.0 APPLICABILITY
1.1 Respiratory Protection Policy
1.2 Responsibilities
1.2.1 Mill Manager
1.2.2 Radiation Safety Officer
1.3 Policy Regarding Facial Hair
1.4 Physiological or Psychological Limitations to Respirator Use
2.0 PROCEDURES FOR RESPIRATOR USE
2.1 Supervision of the Program Including Program Audits
2.2 Training and Minimum Qualifications of Respiratory Program Supervisors
and Implementing Personnel
2.3 Training of Respirator Users
2.4 Fit Testing
2.5 Selecting Respirators
2.6 Maintaining Breathing
Air Quality
2.7 Inventory and Control of Respiratory Protection Equipment
2.8 Storage and Issuance of Respiratory Protection Equipment
2.9 Maintenance Repair Testing and Quality Assurance of Respiratory
Protection Equipment
2.10 Record keeping
2.11 Limitations on Periods of Respirator Use and Relief from Respirator Use
2.12 Monitoring Including Air Sampling and Bioassays
3.0 PROCEDURES FOR MEDICAL EVALUATIONS AND AUDITS
3.1 Performing and documenting the Required Medical Evaluation
3.2 Maintaining TEDE ALARA and Performing ALARA Evaluations of
Respiratory Protection
4.0 PROCEDURES FOR RESPIRATOR APPLICATONS
4.1 Routine Respirator Use
4.2 Nonroutine Respirator Use
4.3 Emergency Respirator Use
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page2of2l
RESPIRATORY PROTECTION PROGRAM
1.0 APPLICABILITY
The Respiratory Protection Program coordinates the
Air sampling sufficient to identify the potential hazard select the proper
equipment and estimate exposures
Surveys and bioassays as appropriate to evaluate actual intakes
Testing of respirators for operability prior to each use
Written procedures regarding selection fitting issuance maintenance and
testing of respirators including testing for operability immediately prior to
each use supervision and training of personnel monitoring including air
sampling and bioassays and record keeping and
Detennination by physician prior to the initial fitting of respirators and
either every 12 months thereafter or at greater frequency determined by
physician that the individual user is medically fit to use the respiratory
protection equipment over the age of 45 or every five years for
individuals under 45 years of age
1.1 Respiratory Protection Policy
The Respiratory Protection Program is established for this facility as policy of Denison
Mines USA Corp DUSA to protect its employees from occupational exposure to
harmful concentrations of radioactive and/or toxic materials in the air
The following is DUSA policy with respect to respiratory protection
Process or other engineering controls will be used whenever feasible to
reduce the need for use of respirators
For work in areas in which respirators must be routinely used to reduce
exposures SOPs will detail use of respiratory protection Non-routine
use of respirators will be performed under Safe Work Permits Self
Contained Breathing Apparatus SCBA respirators will only be used
for evacuation and emergency response situations
Due to the added physical stress of working while using respirator work
periods will be alternated with rest periods
Respirators will not be issued to employees unless they are to be used
1.2 Responsibilities
As noted in NRC Regulatory Guide 8.15 it is widely recognized among safety
professionals that the use of respiratory protection devices in the workplace can impose
physiological and psychological stresses on workers obstruct their vision hinder their
movements and make effective communications difficult These factors increase the risk
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page of 21
of physical injury to respirator wearers that in many cases far exceeds any potential risk
associated with the inhalation of small quantity of airborne radioactive material
Therefore the NRC recommends that process or engineering controls be used to the
extent practical to control the concentration of radioactive material in air and that the use
of respiratory protection devices be contemplated only after other measures to limit
intake have been considered
In general the Mill Manager is responsible for providing the equipment and resources
necessary for the successful implementation of the Respiratory Protection Program and
for facilitating the application of engineering controls to reduce the need for the use of
respiratory protection devices The Radiation Safety Officer RSO has primary
responsibility for implementation and oversight of all aspects of the respiratory protection
program The Mill Manager and the RSO will coordinate efforts to use to the extent
practical procedures and engineering controls based on sound protection principles to
achieve ALARA
1.2.1 Mill Manager
The Mill Manager is responsible for ensuring that respiratory protection program
meeting or exceeding that specified by regulation is established and maintained for the
employees under his or her jurisdiction
1.2.2 Radiation Safety Officer
The RSO is responsible for the implementation and direct control of the respiratory
protection program The RSO is charged with the following responsibilities
Supervision of respirator selection procedures
Establishment of training sessions about respiratory equipment for
employees
Establishment of continuing program of cleaning and inspecting the
equipment
Designation of proper storage areas for respiratory equipment
Establishment of issuance and accounting procedures for uses of
respiratory equipment
Establishment of medical screening programs and procedures for
employees assigned to wear respiratory equipment
Establishment of periodic inspection schedule of those work
places/conditions requiring respiratory equipment to determine exposure
and/or changing situations
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-l Book 14 Page4of2l
continuing evaluation of the above aspects to assure their continued
functions and effectiveness
1.2.3 Employees
Respirators are provided to employees for their personal protection and the proper use of
respirators in areas in which such protection is required is condition of their
employment Violating the established rules for respirator use may result in disciplinary
action up to and including dismissal
1.3 Policy Regarding Facial Hair
The proper fitting of respiratory device is necessary to ensure that it will function
adequately Facial hair beards mustaches and long sideburns will not allow an airtight
seal to be formed between the face and mask as contaminated air will enter into the
wearers breathing zone if the proper seal is not achieved Leakage of air into the mask
will nullify the purpose of the respiratory device
The policy of DUSA concerning facial hair is
As condition of employment those employees who may at any time be
required to wear respirator as part of their employment will not have
any facial hair that will restrict the proper fitting of respiratory device
1.4 Physiological or Psychological Limitations to Respirator Use
This section describes physiological and psychological including emotional factors
which may limit an individuals ability to wear or work in respirator Any questions or
problems concerning respirators or their use such as the types described in this section
should be addressed to the RSO
1.4 Physiological Limitations
As described below in Section 3.1 medical qualification will be required of each
employee that might be using respirator in their normal work duties This is necessary
to evaluate the individuals limitations to wearing respirator devices licensed
physician to determine that the individual user is medically fit to use the respiratory
protection equipment will perform the medical evaluation The physician will report on
any physiological factors that may limit an individuals ability to wear respirator
1.4.2 Psychological Limitations
Mental factors must also be taken into consideration when employees are required to
wear respirators Some individuals become claustrophobic when wearing respirator
These individuals should not be required to wear respirators if the condition is severe
enough to cause panic
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page of 21
1.4.3 Other Factors
Other factors which may cause problems in respirator sealing must be considered when
performing fit testing These may include such factors as facial structure scars skin
creases or dentures
2.0 PROCEDURES FOR RESPIRATOR USE
2.1 Supervision of the Program Including Program Audits
The Respiratory Protection Program is administered by the RSO Quarterly ALARA
Reports from the RSO are sent to members of the ALARA Committee The effectiveness
of the Respiratory Protection Program is reviewed and exposure data evaluated during
annual ALARA audits
2.2 Training and Minimum Qualifications of Supervisors
supervisor that is person who has the responsibility of overseeing the work activities
of one or more persons who must wear respirators shall be given adequate training to
ensure the proper use of respirators Supervisor training shall include but shall not
necessarily be limited to the following subjects
Basic respiratory protection practices
Nature and extent of respiratory hazards to which persons under his/her
supervision may be exposed
Principles and criteria of selecting respirators
Training of respirator wearers
Issuance of respirators
Inspection of respirators
Use of respirators including monitoring their use
Maintenance and storage of respirators
Regulations concerning respirator use
2.3 Training of Respirator Users
Each employee who may wear respirator will be required to receive training for the
proper use of the device The following outline will be followed during the training
process
Need for Respiratory Protection Equipment
Mechanics of Breathing
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-l Book 14 Page6of2l
Types of Respiratory Particles
Dust
Fumes
Mists
DUSAs Respiratory Company Respiratory Protection Policy Statement
Respiratory Hazards
Airborne uranium and effect
Radon daughters and effect
Chlorine and effect
Ammonia and effect
Airborne vanadium and effect
Acid gases and effect
Other effects
Engineering Controls
De-mister
Ventilation
Ventilating systems for the yellowcake dryer and packaging rooms
Respirator Selection
Type of respirators their function limitations
Full-face with combination cartridges
Powered Air Purifying Respirators PAPR with
radiological dust cartridges
Self-contained breathing apparatus
NIOSH and MSHA approved respirators only
Identification of Hazards
02 content
Routine hazards
Non-routine hazards
Instructions on Field Inspection of the Respirator
Valves
Body of mask
Straps
Lens
Air hoses
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page7of2l
Fitting Donning and Wearing Instructions and Training
Wearing instructions and training including practice demonstrations
shall be given to each respirator wearer and shall cover the following
items
Donning including seal check wearing and removing the
respirator
Adjusting the respirator so that its respiratory-inlet
covering is properly fitted on the wearer and so that the
respirator causes minimum of discomfort to the wearer
Allow the respirator wearer to wear the respirator in safe
atmosphere for an adequate period of time to ensure that
the wearer is familiar with the operational characteristics of
the respirator
Respirator Sealing Problems
Respirators shall not be worn when conditions prevent seal of the
respirator to the wearers face For example
person who has hair beard stubble mustache sideburns
beard low hairlines or bangs that passes between the face
and the sealing surface of the face piece of the respirator
shall not be permitted to wear such respirator
person who has facial hair mustache or beard which
interferes with the function of respirator valves shall not
be permitted to wear such respirator
Glasses which have temple bars or straps which passes
between the sealing surface of respirators full-face piece
and the wearers face shall not be used
head covering which passes between the sealing surface
or respirator face piece and the wearers face shall not be
used
The wearing of glasses or goggles face shield welding
helmet or other eye and face protective device which
interferes with the seal of respirator to the wearer shall
not be allowed
If scars hollow temples excessively protruding
cheekbones deep creases in facial skin the absence of
teeth or dentures or unusual facial configurations prevent
the seal of respirator face piece to wearers face the
person shall not be permitted to wear the respirator
If missing teeth or dentures prevent the seal of respirator
mouthpiece in persons mouth the person shall not be
allowed to wear respirator equipped with mouthpiece
If person has nose of shape or size that prevents the
closing of the nose by the nose clamp of mouthpiece/nose
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page of 21
clamp type of respirator the person shall not be permitted
to wear this type of respirator
Maintenance Storage and Respirator Exchange Procedures
Cleaning sanitizing and maintenance techniques for all types of
respirators
The frequency of respirator exchange clean exchanged for used
Heavy use
Occasional use
The steps that are to be taken to exchange respirators
When how and why SCBA are used
Leaving Hazardous Area
respirator wearer shall be permitted to leave the hazardous area
for any respirator-related cause Reasons which may cause
respirator wearer to leave hazardous area included but are not
limited to the following
Failure of the respirator to provide adequate protection
Malfunction of the respirator
Detection of leakage of air contaminant into the respirator
Increase resistance to breathing
Severe discomfort in wearing the respirator
Illness of the wearer including sensation of dizziness
nausea weakness fatigue breathing difficulty coughing
sneezing vomiting fever or chills
Claustrophobia anxiety or other psychological factors that
may affect the wearer
Emergency respirator use
SCBA self-contained breathing apparatus
Emergency respirator issuance
Regulations for respirator use
lOCFRPart2OSubpartH
2.4 Fit Testing
Frequency annually for every employee who is required to wear respiratory protective
device
White Mesa Mill Standard Operating Procedures Date 2/08 Revision DUSA-2
RPP-1 Book 14 Page9of2l
Quantitative fit testing will be performed using the FitTester 3000 or equivalent
Quantitative fit testing measurements will be performed as follows on the
FitTester 3000 or equivalent
Input the employees name style of respirator and size
Select perform fit test the computer will walk you through series
of five tests
During the testing program the computer will evaluate the employee
If there is failure during any test the employee will adjust the
respirator and try again
If after several attempts to pass test and the employee still fails try
different size respirator
Once the employee passes each of the five tests document will be
printed certifying the successful completion of the examination
The document will then be signed by both the employee and the
facilitator of the examination
The document will then be filed with the employees other Safety
documents in the Radiation Safety Department
Qualitative fit testing measurements will be performed using an MSA
ventilation smoke tube Part No 5645 or equivalent aspirator bulb Steps for
respirator issuance fit testing are as follows
Respirators equipped with high-efficiency filters will be used for this
test red/green filters
Both ends are broken on an MSA ventilation smoke tube One end is
inserted into the tube connected to the positive pressure of two-way
aspirator bulb and the other end covered by inch length of tygon
surgical or rubber tubing The test aerosol is generated by squeezing
the aspirator bulb
The test subject will don the respirator and visual inspection of the
facepiece to face seal made by the tester An obvious leak in the
facepiece to face seal shall be reason to abort the test and record the
mask as unsatisfactory Expression of discomfort created by the mask
shall also be reason to abort the test
The smoke will be generated in all areas surrounding the mask The
smoke is not harmful however it is sufficiently irritating that if there is
leak in the seal of the mask it will be discovered immediately
Any indication of detection of the smoke by the test subject during
fitting indicates failure of that respirator If leakage is detected the
facepiece to face seal shall be visually inspected for obvious leakage
If any doubt about the condition of the respirator or the filter exists
another like respirator shall be tested to assure the leakage was due to
the facepiece to face seal
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page lOof2l
2.5 Selecting Respirators
Respirator selection will be determined by the type of environment in which the
employee will be working The concentration of oxygen and the type and concentration
of hazardous contaminants in the work area atmosphere must be considered during the
selection process
Prior to selecting specific type of respirator the work environment must be thoroughly
evaluated for respiratory hazards The following questions must then be answered
What are the hazards the employee will be exposed to
What are the contaminants and their concentration
Are there any contaminants in the workplace environment that may
damage or irritate the eyes nose or skin
Yes full-face style is recommended
Is the oxygen concentration in the workplace atmosphere between 19.5%
to 23%
Yes combination cartridges will be used if the concentration of
the contaminant is within the acceptable limits for the cartridge
No The workplace or area may only be entered if the 02
concentration is between 19.5 and 23%The workplace
environment will be remediated i.e ventilated by safety
engineering controls such that the oxygen concentration falls
between these limits before it may be entered
Do the contaminant concentrations in the work environment exceed the
limits listed for the combination cartridge being used
Yes Modify the air contaminant concentration by safety
engineering measures
No combination cartridges may be used if oxygen concentration
is between 19.5% and 23%
2.5.1 Air Purifying Respirators
Only MSHA and NIOSH approved and accepted respirators will be used The inventory
will consist of full face and PAPR units and SCBAs
There is only one type of air purifying respirator cartridge used for air contaminants for
the full-face respirators This is red/green GME-H universal cartridge which is
normally effective for removing all air contaminants and atmospheric hazards and is
approved by NIOSH for use under the following conditions
Organic Vapors less than 1000 ppm
Pesticides
Mists of Paints Lacquers and Enamels
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 11 of 21
Dustless than 0.5 mg/m3
Fumes less than 0.5 mg/m3
Mists less than 0.5 mg/m3
The PAPR units are not designed for areas that may come in contact with chemical mists
or high humidity The PAPR units use an Optifilter XL Filter Assembly HE that is only
good for dusty environments These units are ideal for the packaging enclosure
Yellowcake Dryers Ore Storage and Tails
The PAPRs must have the battery fully charged prior to usage The battery charge on
each unit will last approximately eight continuous working hours All maintenance and
cleaning techniques utilized with the full-face respirators will be used for the PAPR units
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 12 of 21
2.5.2 Supplied Air Apparatus
SCBA versus supplied air respirators
Self-contained breathing apparatus
will only be used for evacuation or emergency
purposes
Supplied air respirators will be the apparatus of choice when
The length of the work exceeds 20 minutes
There is adequate time to hook up hoses and filter boards
If at any time the atmosphere contains materials that might be corrosive to the employee
or respiratory device the area will be evacuated The area must be ventilated until the
corrosive materials fall to safe level before work may resume
2.6 Maintaining Breathing Air Quality
The quality of air delivered to all supplied-air respirators shall meet the requirements for
Grade air for breathing air systems as defined in CGA G-7 1-1997 as cited in
Regulatory Guide 8.15 under 6.5.2 Air Quality Requirements The ANSIJCGA G.7-1
1989 specifies the contents of Grade breathing air as oxygen volume/volume of 19.5
to 23.5%hydrocarbon condensed of mg/m3 of air or less carbon monoxide of 10
ppm or less carbon dioxide of 1000 ppm or less and the lack of noticeable odor
2.7 Inventory and Control of Respiratory Protection Equipment
Storage cabinets that will be used for routine respirator issuance will be located in the
respirator cleaning facility Only persons authorized to use respirators are to access the
storage cabinets
When an employee needs clean respirator he or she will obtain one from the storage
location where clean respirators are packaged and kept After obtaining clean
respirator the employee will enter the pertinent information on the log sheet that is kept
in the cabinet with the clean respirators
When used respirator is exchanged for clean unit the dirty respirator will be placed in
the receptacle provided for such use
Employees who routinely wear respirator for more than four hours each day or work in
areas of higher exposure potential i.e yellowcake packaging or precipitation will be
required to exchange respirators daily
Employees that need to be issued PAPR unit will need to see the RSO or his designee to
be checked out on the proper usage of the unit All PAPRs are inventoried and only key
operators or RWP individuals will be issued one of these units
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 13 of 21
Those employees who do not use respirators routinely will exchange them as they
become ineffective in eliminating the hazardous contaminant This determination is
made by the employee by physical inspection of the respirator by impaired breathing
i.e by plugging of cartridge or by the detection of irritant smoke or other conditions
which may indicate defective device
2.8 Storage of Respiratory Protection Equipment
Respirators shall be stored in manner sufficient to protect the device against dust
sunlight extreme cold excessive moisture or damaging chemicals
The cleaned respirators will be stored in cabinets in the respirator cleaning facility
outside the safety department The respirators will be stored in single layers with the
facepieces and exhalation valves in more or less normal position to prevent the rubber
or plastic from cracking
When respirators are not being used they must be stored in the plastic bags in which they
were issued Dirty respirators will be placed in receptacles located in the mill central
control room and at the maintenance shop They will be gathered from these locations
for cleaning and repairs
The frequency that dirty respirator must be exchanged for clean one will be
determined by the amount of time it is used If the employees use is greater than four
hours per day the exchange will be made daily Occasional use will require weekly
exchange Infrequent use will require monthly exchanges
The cabinets containing emergency respirators will be located in areas that are readily
accessible and in areas in which hazard may arise Emergency cabinets are located on
the north side of the mill building outside of the SAG Mill doors outside the SX on the
north wall on the south end of SX on the fire cabinet and at the fire hose station at the
front gate All employees should be made aware of these locations
The cabinets will not be locked but they will have seals attached to the hasps The seals
will prevent employees from using the respirators for routine use but will allow
emergency access During emergencies the seal will be broken and respirator may be
selected in matter of seconds
2.9 Maintenance Repair Testing and Quality Assurance of Respiratory
Protection Equipment
Respirators and component parts shall be maintained and repaired only by persons
specifically trained to perform this work Repairs and maintenance shall be performed in
accordance with the procedures detailed below
2.9.1 Maintenance Cleaning Repair and Testing
Each used respirator must be disassembled before cleaning the cartridges must be
removed and discarded and any hoses or regulators must be removed and washed
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 14of21
separately Some of the units have elastic head straps these should also be removed and
washed separately
The respirators will be cleaned and rinsed in commercially available dishwasher The
radiation and safety staff will perform cleaning and washing of respirators The
respirators will be washed and then aired dried
Each reassembled respirator must be inspected for radiation contamination before it is
used An instrument survey or swipe test may be conducted to determine if any item is
contaminated The equipment check must indicate levels of less than 100 dpmIlOO cm2
of alpha radiation or 1000 dpmllOO cm2 of beta-gamma radiation to be serviceable If
repeated washings do not decrease contamination to acceptable levels that item must be
disposed of
Respirators shall be inspected in accordance with NRC Regulatory Guide 8.15 Revision
October 1999 The following conditions should be checked during any type of
inspection
Air Purifying Respirators
Routinely used air purifying respirators should be checked as follows before and after
each use
Examine the facepiece for
Excessive dirt
Cracks tears holes or distortion from improper storage
Inflexibility stretch and massage to restore flexibility
Cracked or badly scratched lenses in full facepieces
Incorrectly mounted full facepiece lens or broken or missing
mounting clips
Cracked or broken air purifying element holders badly worked
threads or missing gaskets if required
Examine the head straps or head harness for
Breaks
Loss of elasticity
Broken or malfunctioning buckles and attachments
Full facepieces only excessively worn serrations on the head
harness which might permit slippage
Examine the exhalation valve for the following after removing its cover
Foreign material such as detergent residue dust particles or
human hair under the valve seat
Cracks tears or distortion in the valve material
Improper insertion of the valve body in the facepiece
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 15 of 21
Cracks breaks or chips in the valve body particularly in the
sealing surface
Missing or defective valve cover
Improper installation of the valve in the valve body
Examine the air purifying elements for
Incorrect installation loose connections missing or warn gaskets
or cross-threading in holder
Cracks or dents in outside case of filter cartridge or canister
If the device has corrugated breathing tube examine it for
Broken or missing end connectors
Missing or loose hose clamps
Deterioration determined by stretching the tube and looking for
cracks
Examine the harness of front or back mounted gas mask for
Damage or wear to the canister holder which may prevent its being
held securely in place
Broken harness straps or fastenings
Blower mechanism on the PAPR units only
Damage to the outer casing of the blower unit will result in the
replacement of the blower
Missing or broken pins that connect the blower to the battery pack
will result in replacing of damaged pieces
Supplied Air Respirators
The following shall be checked
If the device has tight fitting facepiece use the procedures outlined
above for air purifying respirators
Examine the air supply for
Integrity and good condition of air supply lines and hoses
including attachments and end fittings
Correct operation and condition of all regulators valves or other
air flow regulators
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 16 of2l
2.9.2 Quality Assurance
To prevent the use of faulty or defective respiratory equipment the following
steps will be taken
New Equipment
All new equipment will be thoroughly inspected before it is put into
service Only MSHAINIOSH approved equipment will be used Parts
used for repairs will be purchased only from the manufacturer of the unit
being repaired or theft agents
Cleaning and Repairs
All respiratory devices will be inspected before and after cleaning and
before and after repairs are made The inspection procedures that are to be
used are listed above under Section 2.9.1
Any replacement items that will be used for repairs will be inspected prior
to assembly
Periodic Checks of Items in Storage
At lease once during each quarter all of the respirators that are in storage
will be checked for serviceability and to make sure that they will be ready
for immediate use
2.10 Recordkeeping
Inspections of all respiratory devices will be conducted in accordance with the provisions
contained in NRC Reg Guide 8.15 and section 2.9.1 above and under no circumstances
shall device that is known to be defective be used
Freshly cleaned and inspected respirators will be placed in plastic bags and sealed
The individual who serviced the respirator shall write the date on each bag and initial it to
indicate the work has been done properly
Respirators used for emergency use are inspected and the inspection recorded once per
month
2.11 Limitations on Periods of Respirator Use and Relief from Respirator Use
As noted above under Section 1.2 the NRC has noted that the use of respiratory
protection devices in the workplace can impose physiological and psychological stresses
on workers obstruct their vision hinder their movements and make effective
communications difficult In consideration of this respirator wearer shall be permitted
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 17 of2l
to leave the work area for any respirator-related cause Reasons which may cause
respirator wearer to leave work area include but are not limited to the following
Failure of the respirator to provide adequate protection
Malfunction of the respirator
Detection of leakage of air contaminant into the respirator
Increased resistance to breathing
Severe discomfort in wearing the respirator
Illness of the wearer including sensation of dizziness nausea weakness
fatigue breathing difficulty coughing sneezing vomiting fever or chills
Claustrophia anxiety or other psychological factors that may affect the
wearer
2.12 Monitoring Including Air Sampling and Bioassays
2.12.1 Evaluation of Respiratory Hazards
Before respiratory protective device is used the work area must be evaluated as to the
type of hazards that may be encountered The type of respiratory protection may be
selected only after the hazard has been classified
Most areas of the mill have been evaluated for hazards during routine work assignments
Signs will be posted in the different areas that will indicate the type of respiratory device
to be used under normal conditions
Equipment needed
Oxygen and Combustible Gas Detector
MSA Orion or equivalent
MSA Samplair Pump Kit or similar with the following detector tubes
Carbon Dioxide
Carbon Monoxide
Sulfur Dioxide
Ammonia
Hydrogen Sulfide
Nitrous Oxide
Halogen Gases Chlorine
Acid fumes and mists
Organic vapors
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 18 of2l
Many environmental designs were incorporated into the mills construction to keep
exposures to most hazards at minimum This environmental equipment is checked
frequently to ensure that it is functioning properly
To ensure the reliability of these controls monthly gross alpha and radon daughters
samples will be collected at numerous locations throughout the mill Routine samples
will also be collected in the vanadium precipitation and packaging areas and analyzed for
airborne vanadium
The routine samples have already identified some areas that require respirator use at all
times during normal working conditions These areas are inside the yellowcake dryer and
packaging enclosures and the vanadium dryer area and the packaging area Other areas
that may require respirator use may include but would not be limited to the sample
bucking room and the SAG mill
Respirators need not be worn routinely during normal working conditions in other areas
of the mill At these locations usage will be determined by the hazard level or at the
employees request Occasionally condition may exist that the environmental controls
cannot handle At that time the appropriate respirator must be used until the workplace
atmosphere is returned to normal
Infrequently maintenance work will have to be performed in areas that are not normally
sampled or areas that may have questionable air quality Prior to anyone entering one of
these areas the environment must be evaluated to determine what hazards exist
Safe Work Permit is issued for all work tasks that are anticipated to present
unidentified or unusual hazardous environmental conditions Radiation Work Permit is
issued for work in unassessed areas or for nonrecurring tasks for which engineering
controls are not in place or practical The safety department will be responsible for the
evaluation of the areas before work begins
When the oxygen concentration is listed as potentially hazardous portable detector will
be used to determine the exact oxygen-air mixture NIOSH defines that air which
contains less than 19.5% 02 is an oxygen-deficient atmosphere and attempting to breathe
such air is considered to present hazard that would be immediately dangerous to life
and health Any area having less than 19.5%02 will not be entered until or unless the 02
concentration returns to and is maintained at level above 19.5%If an area is identified
as having an oxygen-deficient atmosphere the oxygen levels must be remedied by
engineering controls prior to entry by personnel The use of SCBA will only be for
emergency escape or emergency response purposes
Other atmospheric hazards will be identified and quantified by using air sampling
equipment such as the MSA Samplair Pump or similar device with detector tubes for
the specific contaminant in question The instructions must be carefully read for every
test as each type of detector tube is handled differently
After exposure to the atmosphere the tubes will indicate the presence and concentration
of the chemical for which that tube is designed Chemical cartridges are good only in
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 19 of 21
atmospheres in which the chemical concentration is less than the limit set by the
manufacturer and the oxygen concentration is equal to or greater than 19.5%As noted
above the company policy is not to enter an area in which the 02 level is below 19.5%
but to enter such areas only in emergency situations such as to retrieve an injured
worker and then with the use of SCBA
There are many other hazards that are very obvious but are often overlooked The
following are examples
dust concentrations have an adverse affect on breathing and/or the comfort of the
individual
some substances may cause irritation to the eyes nose throat etc but may not be
chemically toxic
These and other such conditions should always be considered in evaluating respiratory
hazards If there is any doubt about the conditions within the work area respiratory
device should be used Always be conservative
2.11.2 Breathing Zone Air Samples
Breathing zone samples are collected to determine the air contamination concentration an
individual may be exposed to during the execution of his job The respiratory protection
factor is used to calculate the individuals exposure during the work task duration The
application of respiratory protection factor assigned to the particular respiratory device
is used to reduce an individuals exposure to an air contaminant concentration as
determined by breathing zone sampling Routine breathing zone samples are collected by
the use of small belt-mounted pump attached to hose that is in turn attached to the
persons clothing close to the head or breathing zone The sample is collected for
period of time that would be representative of one eight hour workday They are
collected in such manner that the material collected will be representative of that being
inhaled by the individual wearing the sampler
2.11.3 Bioassay Program
Evaluation of the effectiveness of the respiratory protection program will be
accomplished by air sampling described above in 2.12.1 and by the Mill Bioassay
Program
Those employees who are working in areas that require the use of respirators will submit
urine specimen for analysis on biweekly basis Employees who use respirators during
maintenance may also be required to submit specimens after maintenance ceases The
samples will be collected from individuals who have performed maintenance tasks in
atmospheres that are significantly elevated in contaminant concentration or they are
working in such an area for an extended period of time
The specimens will be analyzed for uranium content
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 20 of 21
3.0 PROCEDURES FOR MEDICAL EVALUATIONS AND AUDITS
3.1 Performing and Documenting the Required Medical Evaluation
Medical qualification will be required of each employee that might be using respirator
in their normal work duties This is necessary to evaluate the individuals limitations to
wearing respirator devices The medical evaluation will be performed by licensed
physician to determine that the individual user is medically fit to use the respiratory
protection equipment Medical evaluation will be performed prior to the initial fitting of
respirator use and either every 12 months thereafter or periodically at frequency to be
determined by the physician
The medical screening process will include medical history and will be sufficient in the
opinion of the physician to identify any person who should not use respiratory devices
for medical reasons or who should be limited to the use of specific types of respirators
The physician will report any medical restrictions the employee has that would limit an
individuals ability to use respirator Based on the physicians recommendations any
employee may be subject to additional or more frequent medical evaluation as deemed
necessary by the physician
3.2 Maintaining TEDE ALARA and Performing ALARA Evaluations of
Respiratory Protection
As stated in the Policy Statement in 1.0 DUSA shall use to the extent practical
procedures and engineering controls based on sound protection principles to achieve
ALARA and shall limit intakes by means of engineering controls or procedures along
with the use of respirators consistent with maintaining the TEDE ALARA When
specific ALARA evaluation is performed to justify the use or nonuse of respirators the
evaluation shall consider the elements detailed in Section 2.1 of Regulatory Guide 8.15
4.0 PROCEDURES FOR RESPIRATOR APPLICATIONS
4.1 Routine Respirator Use
As noted above under 2.8 the cabinets for routine use respirators will be located in the
respirator cleaning facility outside the safety department
Respirators will not be issued to employees unless they are to be used Only employees
having current authorization to use respirators are to access the storage cabinets and
obtain respirators
When respirators are not being used they must be stored in the plastic bags in which they
were issued Dirty respirators will be placed in receptacles located in the mill central
control room and at the maintenance shop They will be gathered from these locations
for cleaning and repairs
White Mesa Mill Standard Operating Procedures Date 12/08 Revision DUSA-2
RPP-1 Book 14 Page 21 of 21
Donning the respirator must be performed in accordance with the training provided At
least one type of user seal check must be performed immediately prior to exposure to
ensure that the respirator is properly seated on the face
The frequency that dirty respirator must be exchanged for clean one will be
determined by the amount of time it is used If the employees use is greater than four
hours per day the exchange will be made daily Occasional use will require weekly
exchange Infrequent use will require monthly exchanges
4.2 Nonroutine Respirator Use
Nonroutine Respirator Use shall be defined as use of respirators in unassessed areas or
for nonrecurring tasks for which engineering controls are not in place of practical
4.3 Emergency Respirator Use
Emergency Respirator Use shall be used for recovery of an injured person from an area
where air concentrations of radioactive material may be high the breathing quality of the
ambient air has not been assessed or the area may become immediately dangerous to life
or health IDLH because of the presence of nonradiological hazards
Respirators designed for emergency use will be stored in areas that are readily accessible
to all employees Emergency cabinets are located on the north side of the mill building
outside of the SAG Mill doors outside the SX on the north wall on the south end of SX
on the fire cabinet and at the fire hose station at the front gate
White Mesa Mill Standard Operating Procedures Date 7/99 Revision
Book 18 UDEQ Split Sampling Groundwater Monitoring Plan Page of 21
GROUNDWAThR MONITORING PLAN
AND STANDARD OPERATING PROCEDURES
FOR
UDEQ SPLIT SAMPLING PROGRAM
International Uranium USA Corporation
P.O Box 809
BlandingUT 84511
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Procedure3doc
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TABLE OF CONTENTS
SECTION PAGE
GROUNDWATER MONITORING PLAN AND STANDARD OPERATING PROCEDURES
PART GROUNDWATER MONITORING PLAN
1.0 GROUNDWATER MONITORING
2.0 QUALITY ASSURANCE
PART II-GROUNDWATER STANDARD OPERATING PROCEDURES
STANDARD OPERATING PROCEDURE NO 1.0-GROUNDWATER SAMPLING AND
MEASUREMENT OF FIELD PARAMETERS
1.0 EQUIPMENT
1.1 SAMPLING EQUIPMENT
1.2 MEASUREMENT OF PHREATIC ELEVATIONS
2.0 MONITORING METHODOLOGY
2.1 PHREATIC ELEVATIONS QUARTERLY
2.2 GROUNDWATER QUALITY
2.3 FIELD SAMPLE PROCEDURE FOR MONITORING WELLS
2.4 FIELD SAMPLING PROCEDURE FOR CULINARY WELLS
2.5 FIELDDATA
2.6 SAMPLE TRANSPORTATION 10
3.0 CALIBRATION 10
3.1 PIIREATIC MEASUREMENTS 10
3.2 WATER QUALITY 10
4.0 RECORD KEEPING 10
5.0 MONITORING LOCATIONS AND FREQUENCY 10
6.0 ANALYSIS PROCEDURE 10
7.0 QUALITY ASSURANCE METHODOLOGY 11
7.1 WELL CONTAMINATION 11
7.2 PHREATIC ELEVATIONS 11
7.3 WATER QUALITY 11
STANDARD OPERATING PROCEDURE NO 2.0 SAMPLE HANDLING DOCUMENTATION AND
ANALYSIS 12
1.0 SAMPLELABELING 12
2.0 SAMPLE HANDLING AND SHIPPING 12
3.0 SAMPLE DOCUMENTATION AND TRACKING 12
4.0 SAMPLE CHAIN-OF-CUSTODY 13
5.0 RECORD KEEPING 13
6.0 PVC WELL CASING LIMITATIONS 13
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Split Sampling Procedures.docPAciminMaster SOP\Bonk 8_UDEQ Procedures Plans\UDEQ Groundwater Split Sampling
Proceduresdoc
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TABLE OF CONTENTS
SECTION PAGE
STANDARD OPERATING PROCEDURE NO 3.0 DATA VALIDATION 15
1.0 DATAVALIDATIONANDREVIEW 15
1.1 DATAQUALIFIERS 15
1.2 REQUIRED CONTENTS OF LABORATORY ANALYTICAL DATA PACKAGES 15
2.0 DATA VALIDATION PROCEDURE 15
3.0 CORRECTIVE ACTION 15
TABLE 1-GROUNDWATER MONITORING PROGRAM 16
TABLE 2-SAMPLE PRESERVATION 17
TABLE 3-DETECTION LIMITS 18
ATTACHMENT 1-FIELD WATER ANALYSIS OF GROUNDWATE 19
ATTACHMENT 2-CALCULATION OF CASING VOLUME FROM DEPTH OF WATER IN WELL2O
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GROUNDWATER MONITORING PLAN AND STANDARD OPERATING
PROCEDURES
PART GROUNDWATER MONITORING PLAN
1.0 GROUNDWATER MONITORING
Groundwater is sampled on quarterly basis for water surface elevations and
analysis of radionuclides and chemical parameters The active monitoring wells
are MW-5 MW-il MW-i2 MW-i4 MW-iS and MW-i7 Quarterly
groundwater samples are tested for the following parameters U-Nat nickel
potassium and chloride
UDEQ has requested an additional sampling program the split sampling
program involving additional wells and parameters This Groundwater
Monitoring Plan and SOP applies only to the groundwater split sampling
events requested by UDEQ Quarterly POC sampling of monitoring wells for
compliance with the NRC license requirements will continue to be conducted in
accordance with the most current revision of the Groundwater Monitoring Plan
and Standard Operation Procedures for quarterly POC Monitoring
To implement the DEQ split-sampling program monitoring wells MW-i MW-2
MW-3 MW-4 MW-i8 MW-i9 and culinary wells and will be sampled in
addition to the six POC wells named above The sampling parameters for the
DEQ split-sampling program will include VOCs SVOCs radiologics major
ions dissolved metals pesticides herbicides and nutrients for all wells
If split sampling for UDEQ occurs on the same dates as the quarterly POC
monitoring separate samples will be collected for the split sampling and quarterly
POC sampling The separate quarterly POC samples will be analyzed and results
reported in accordance with the Groundwater Monitoring Plan and Standard
Operation Procedures for Quarterly POC Monitoring and the current NRC license
conditions
2.0 QUALITY ASSURANCE
Quality assurance for groundwater monitoring consists of QC samples submitted
with each set of samples The QC samples for split sampling consist of
duplicate spike equipment rinsate and blank During split sampling one
QAIQC trip blank for VOCs will also be sent with each cooler list of sample
containers and the preservatives to be used for split sampling is shown in Table
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PART II GROUNDWATER STANDARD OPERATING PROCEDURES
STANDARD OPERATING PROCEDURE NO 1.0 GROUNDWATER
SAMPLING PROCEDURE AND MEASUREMENT OF FIELD PARAMETERS
1.0 EQUIPMENT
Groundwater monitor wells consist of narrow diameter PVC cased wells
Equipment used for groundwater sampling program is as follows
1.1 Sampling Equipment
1.8 inch O.D air-driven sampling pump
150 psi air compressor and ancillary equipment
pH meter and probe
Temperature level and conductivity meter with probe
0.45 micron filters
Field preservation chemicals H2S04 HNO3 HC1
Five gallon sample bucket
Sample containers and labels see Table
Rubber gloves
10 Distilled water
11 Teflon bailer and rope
12 Cooler and ice
1.2 Measurement of Phreatic Elevations
Measurement of phreatic elevations is accomplished by using the
following water level equipment
YSI Model 3000 temperature level and conductivity meter with
probe or equivalent
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2.0 MONITORING METHODOLOGY
2.1 Phreatic Elevations Quarterly
Phreatic elevations are determined in each monitoring well prior to
sampling by using water level indicator meter Field log books are
maintained listing depth to water from top of casings Readings are taken
by lowering the sensor into the casing until the electrical sensor contact
shows that conductive liquid has been reached The distance from the
point of contact to known one-foot interval marker on the wire is
determined using tape measure in inches or the scale provided on the
back of the T-L-C meter in tenths of foot Data is recorded as Depth to
Water This information is maintained on computer files
There are no action levels associated with monitor well phreatic elevation
2.2 Groundwater Quality
The perched zone monitoring wells at the White Mesa Mill are located in
low-yield formation During any sampling event some or all of the
perched zone wells may be incapable of yielding two casing volumes of
purge water The sampler will attempt to evacuate two casing volumes If
the well yields two casing volumes the individual performing the sampling
should immediately test for pH temperature and specific conductance and
collect the samples at once in order of the parameters volatilization
sensitivity If the well cannot yield two casing volumes the individual
performing sampling should evacuate the well to dryness once
Approximately 24 hours later the first sample should be tested for pH
temperature and specific conductance Samples should then be collected
and containerized in the order of the parameters volatilization sensitivity
The well should be retested for pH temperature and specific conductance
after sampling as measure of purge efficiency and as check on the
stability of the water samples over time
The wells will be sampled for the following parameters in the order listed
Volatile Organic Compounds VOC 120 ml samples
Semi-volatile Organic Compounds SVOC liter samples
POC parameters filtered liter sample
Dissolved Metals 250 ml samples
Pesticides liter samples
Herbicides liter samples
Nutrients 2500 ml samples
Major ions 1/2 gallon samples
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Radiologics 1/2 gallon samples
All UDEQ split samples will be unfiltered except for the samples collected
for POC parameters dissolved metals and radiologics
2.3 Field Sampling Procedure for Monitoring Wells
After two casing volumes have been evacuated or 24 hours after low
yield well has been evacuated teflon bailer will be lowered to collect
sample for VOCs and SVOCs Sample collection equipment should be
rinsed with water from the source before containers are filled Care should
be taken to not agitate the water in the well during the repeated lowering
of the bailer The VOC and SVOC sample should be slowly decanted into
the sample container filling the container completely The sample should
then be rapidly capped excluding any headspace inverted to check for air
bubbles and put into sample cooler as soon as possible The remaining
samples POC parameters metals pesticides herbicides nutrients major
ions and radiologics will be collected using the field pump
Remove casing cap and check water level in well by lowering the
electrical water level probe until conductance reading is
measured
Record water level in Monitoring Well logbook Record the water
level casing volume and other data required in Attachment This
may be recorded in the well logbook
Determine the casing volume Volumegaj O.653h for casing
volume and Volumegai .367h for casing or see Attachment
Lower field pump into well making sure to keep pump at least five
feet from the bottom of the well
Evacuate two casing volumes if possible
If well cannot yield two casing volumes evacuate well to dryness
and wait 24 hours before performing step
Remove pump from well and replace the casing cap on well if
necessary
Rinse pump with distilled water before sampling next well
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Lower teflon bailer into well to collect VOC and SVOC sample
10 The first sample collected with the teflon bailer should be tested
for p11 temperature and specific conductance
11 Add preservative to sample container if required
12 Slowly pour the sample from the teflon bailer into the sample
containers for VOCs and SVOCs taking care not to agitate the
sample
13 When filling the sample containers for VOCs allow the
groundwater to fonn meniscus in the sample container and
quickly cap the sample excluding any headspace
14 Invert the sample bottle to check for air bubbles
15 After samples have been collected for VOCs and SVOCs lower
field pump into well
16 If filtered sample is required rinse filter with water from the
sample source and place 0.45 micron filter on sample tubing Be
careful not to contaminate filters by handling them with dirty
fingers or gloves
17 Pump sample through filtration unit if required and into sample
container after letting the first 100 ml be used to rinse the sample
container and be wasted
18 Add preservative to sample container if required
19 Rinse lid of sample container when container is filled with filtered
or uiifiltered water depending on the type of sample to be collected
and tighten lid onto container
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20 Identify and label the sample container with
Project/facility
Date and time of sample
Any preservation method utilized
Samplers initials
Filtered or unfiltered
Ii Sample location
21 Place sample in cooler
Upon returning to the office the samples are stored in
refrigerator at until transferred to the analytical laboratory
22 Before leaving the sampling location thoroughly document the
sampling event in the field logbook by recording the items
required in SOP 2.0 Step and any other significant features or
conditions during the sampling event
2.4 Field Sampling Procedure for Culinary Wells
The sampling procedure for the culinary wells will be the same as the
procedure for the monitoring wells except that all samples will be obtained
from the pump located in the culinary well and the well will not be purged
before the samples are collected The groundwater will be tested for pH
conductance and temperature until three successive samples show
stabilized readings on pH to 0.50 temperature to 2C and
conductivity to 500 umhos When the well water has reached
equilibrium the samples will be collected
2.5 Field Data
Field data is retained on file or on computer for review This information
is compared to the analytical results of sampling for Quality Assurance
and correctness
The sampler or observer will record the same types of information in the
well logbook as described in Section 2.3 above
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Proceduremdoc
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2.6 Sample Transportation
Samples are catalogued at the White Mesa Mill office and sent to the
Analytical Laboratory with the appropriate Chain of Custody sheets
attached Samples are transported via sealed containers by postal or
contract services Laboratory chain of custody procedures will be
followed
3.0 CALIBRATION
3.1 Phreatic Measurements
Equipment used in phreatic measurements is checked for calibration
quarterly
3.2 Water Quality
Probe and meter function including temperature p11 and conductivity are
calibrated prior to each use by using known pH solutions and conductivity
standards Temperature is checked comparatively by using thermometer
4.0 RECORD KEEPING
Field data are logged onto field file worksheets see Attachment and into the
field logbook Once all the data for the quarter all wells is completed the data
from the worksheets is typed into computer file Certificates of analysis and
computer worksheets are maintained as backup file for this information
Data includes well I.D sample date well phreatic elevations field analytical data and all
analytical data
5.0 MONITORING LOCATIONS AND FREQUENCY
Monitor wells are monitored quarterly for phreatic elevation radionuclide and chemical
analyte constituents For UDEQ split sampling water samples are collected from
monitor wells 11 12 14 15 17 18 and 19 and culinary wells and
6.0 ANALYSIS PROCEDURE
Analytical procedures utilized by the contract laboratory are in accordance with
their respective established quality assurance and quality control programs The
analyses to be performed on each well sample collected for the split sampling
program as follows VOCs SVOCs POC parameters dissolved metals
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Procedurec.doc
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pesticides herbicides nutrients major ions radiologics Detailed information on
sample size preservation techniques holding times analytical procedure numbers
and required limits of detection for each parameter are provided in Tables and
7.0 QUALITY ASSURANCE METHODOLOGY
7.1 Well Contamination
Well contamination from external surface factors is controlled by
installation of cap over the surface casing and cementing the surface
section of the drill hole Wells have surface covers of mild steel with
lockable cap cover Environmental staff have access to the key series
locking the wells
Subsurface well stagnation for pumped wells is reduced by purging the
monitoring wells and pumping the culinary wells until the temperature
pH and conductivity levels of water samples become consistent This
verifies that the aquifer zone water is being drawn into the well and is
representative sample
7.2 Phreatic Elevations
Monitoring of phreatic elevations is controlled by comparing historical
field log data to actual measurement depth This serves as check of the
field measurements
7.3 Water Quality
Quality assurance of water sample collection sample handling and
preservation is maintained by following procedures established in the
White Mesa Mill groundwater quality assurance plan Observation of
technician performance is monitored on periodic basis to ensure
compliance with this procedure Blind duplicates of at least one well per
quarter are submitted to the analytical laboratory to monitor field and
laboratory quality assurance performance Deviations exceeding ten
percent 10%result in analytical and field procedure review
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Proceduresdoc
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STANDARD OPERATING PROCEDURE NO 2.0 SAMPLE HANDLING
DOCUMENTATION AND ANALYSIS
2.1 1.0 SAMPLE LABELING
All sample labels must be filled out in ink and numbered The date time
samplers initials and the sample location will be identified on each sample The
following information will be contained on the label projectifacility date
and time of sample collection samplers initials filtered or unfiltered
preservatives and sample location
2.0 SAMPLE HANDLING AND SIUPPING
Sample containers will be placed and packaged in large plastic coolers Samples
will be stored at four degrees Centigrade Samples will then be transported in
these sealed containers by postal contract services to the contract analytical
laboratory
Chain-of-Custody reports will be placed inside resealable bag and taped to the
inside lid Seals will be placed on outside of packaging
3.0 SAMPLE DOCUMENTATION AND TRACKING
Documentation of observations and data from sampling provide important
information about the sampling process and provide permanent record for
sampling activities All observations and sampling data will be recorded in
waterproof ink in bound field logbook with consecutively numbered pages
The field logbook will contain the following information project name
sample location samplers names and signatures date and time of sample
collection sample depth description of sample type description of
QA/QC samples sample handling including filtration and preservation when
warranted field observations such as weather conditions 10 results of in-
field measurements and 11 names of personnel present observing the sampling
The field logbook will also contain detailed notes describing any other significant
factors during the sampling event including as applicable mechanical
equipment and vehicles operating nearby condition of the well cap and lock
water appearance color odor clarity presence of debris or solids placement of
sample containers and coolers relative to the sample pump exhaust difficulties in
sample handling container filling or preservation any variances from the
sampling plan and procedures and any other relevant feature or condition
4.0 SAMPLE CHAIN-OF-CUSTODY
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Procedures.doc
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Chain-of-Custody form accompanies the sample being shipped to the
laboratory Standard Chain-of-Custody protocol is initiated for each sample set
COC form is to be completed for each set of samples collected in container
and is to include the following samplers name company name date
and time of collection sample location and analyses requested
The person shipping the samples to the laboratory will sign the COC form
document shipment method and send the original and the second copy of the
COC form with the samples Upon receipt of the samples the person receiving
the samples will sign the COC form and return the second copy to the
Environmental Coordinator
Copies of the COC forms and other relevant documentation will be retained at this
facility
5.0 RECORD KEEPING
All groundwater data are kept in the files and when analytical results are available
the results are entered into computer file Laboratory analytical data are stored
in the groundwater files after the data has been entered on computer file
Records will be maintained at this facility for the appropriate period of time
6.0 Pvc WELL CASING LIMITATIONS
Numerous evaluations have been conducted of what impact PVC well casings
may have on groundwater sampling results for VOCs These studies have often
resulted in significantly different conclusions However the vast majority have
concluded that PVC is capable of sorbing and leaching organic constituents
These varying conclusions reflect different interpretations of what constitutes
significant parameter interference In some cases PVC interference may be
insignificant while in others it may seriously bias the analytical results
Regardless EPA continues to advise against the use of PVC well casings where
dilute organic concentrations are expected or are of interest
If high concentrations are encountered greater than mgfL it is unlikely that
leaching from the PVC-cased wells at the Mill would present any significant bias
However should analytical results indicate low level detection of organic
compounds in number of the wells the detected parameters should be compared
to the list of those known to leach from PVC or glued joints Given that the limit
of detection of EPA Method 8260 is ug/L analytical results for parameters
known to leach from PVC or glued joints near the detection level could
realistically be produced by PVC interference and should be attributed to that
source
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STANDARD OPERATING PROCEDURE NO 3.0 DATA VALIDATION
1.0 DATA VALIDATION AND REVIEW
1.1 Data Qualifiers
Laboratory analyses will be reviewed by the Environmental Coordinator
and/or staff Quality control samples provide comparative basis for
analysis fundamental to this review process Rejected data will not be
usable for any purpose
1.2 Required Contents of Laboratory Analytical Data Packages
The contract laboratory will prepare and retain all analytical and QC
documentation The laboratory will provide hard copy information in each
data package submitted in accordance with QA objectives for the Surface
Water QA Project Plan COC forms cover sheets with comments
narrative samples analyzed reporting limits and LLD values for analytes
and analytical results of QC samples The data reduction and laboratory
review will be documented signed and dated by the analyst
2.0 DATA VALIDATION PROCEDURE
Ten percent of the data will be subjected to complete data validation
using appropriate scientific methods and guidance from NRC
Regulatory Guides 4.14 and 4.15 minimum of reported results of one
or more analytes for ten percent of the samples will be recalculated from
the raw data and checked for transcription order The laboratorys data
validation specialist will be responsible in part for validating the analytical
data
3.0 CORRECTIVE ACTION
Corrective action will be taken for any noted deficiency in laboratory data
QA/QC problems will be brought to the immediate attention of the environmental
coordinator and or staff Appropriate response measures will be taken with regard
to these problems
Appropriate attachments and forms are maintained by the Environmental
Department in accordance with record keeping policies of the White Mesa Mill
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TABLE
GROUNDWATER MONITORING PROGRAM
MONITOR SITES
Monitor Wells No 11 12 14 15 17 18 19 Culinary Wells
and QA/QC samples
FIELD REQUIREMENTS
Depth of well in feet to nearest tenth inch
Temperature in degrees Celsius
pH to two decimal places
Specific conductance in umhos at temperature
Detailed description of field sampling conditions in well logbook
LAB REQUIREMENTS
POC Quarterly Samples UDEQ Split Samples
filtered unfiltered except metals
Chlorides VOCs
Nickel mg/l SYOCs
Potassium mgIl Dissolved Metals
U-nat uCiIml Pesticides
U-nat LLD uCilml Herbicides
Nutrients
Major ions
Radiologics
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Procedurez.doc
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TABLE
SAMPLE PRESERVATION AND ANALYSES
Analysis Sample Bottle Preservative Max Holding
Time
Volatile Organics
8260A
40 ml glass
vials with teflon
lids
HCI 2-3 drops days
Semi-Volatile Organics 8270 liter amber
glass
none days
POC Parameters filtered liter plastic HNO3 28 days
Dissolved Metals filtered
Type ifi aluminum antimony
arsenic barium beryllium
cadmium chromium copper iron
lead manganese mercury
molybdenum nickel selenium
silver thallium vanadium zinc
250 ml plastic HNO3 28 days
Pesticides unfiltered
8081
liter glass with
teflon cap
none days
Herbicides unfiltered
8151
liter glass with
teflon cap
none days
UDEQ Chemistry sample
unfiltered Type II
bicarbonate calcium carbonate
chloride fluoride hydroxide
magnesium potassium sodium
sulfate total suspended solids
CO2 total alkalinity total hardness
conductivity pH total dissolved
solids CO3 solids turbidity
gallon plastic none days
Nutrients unfiltered
NO2 NH3 Total P04
500 ml plastic H2S04 28 days
Radiologic filtered
Gross and f3 Radium-226
Radium-228 Unat
gallon plastic HNO3 months
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Procedures.doc
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Book 18 UDEQ Split Sampling Groundwater Monitoring Plan Page 17 of 21
TABLE
DETECTION LIMITS TO BE USED FOR UDEQ SPLIT SAMPLING
Parameter Detection Limit Parameter Detection Limit
VOC UDEQ Chemistry Bottle Parameters
Bicarbonate
SVOC Calcium mg/l
Carbonate
POC Parameters Chloride mg/I
Chlorides mg/i Fluoride 0.05 mg/I
Nickel 0.05 mg/l Hydroxide
Potassium mg/i Magnesium mg/l
U-nat 0.0003 mg/i Potassium mg/i
Sodium mg/l
Dissolved Metals Sulfate 10 mg/I
Aluminum 30 ug/l Total Alkalinity mg/I
Antimony ug/l Total Hardness
Arsenic ug/l Turbidity 0.05 NTU
Barium ug/l CO2
Beryllium ug/l Conductivity
Cadmium ug/l pH
Chromium ug/l Total Dissolved Solids mg/i
Copper 12 ug/l CO3 Solids
Iron 20 ug/l Total Suspended Solids mg/i
Lead ug/l
Manganese ug/i Nutrients
Mercury 0.2 ug/l N02 0.02 mg/i
Molybdenum ug/l NFl3 0.05 mg/i
Nickel 10 ug/l Total P04 0.02 mg/l
Selenium ug/l
Silver ugh Radiologic Parameters
Thallium ug/l Gross Alpha pCi/i
Vanadium 30 ug/l Gross Beta 10 pCi/i
Zinc 30 ug/l Radium-226 0.5 pCi/i
Radium-228 pCi/l
Pesticides Total pCi/I
Herbicides
Detection Limit is per EPA Standard Method SW-846
ATTACHMENT
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Precedures.doc
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FIELD WATER ANALYSIS OF GROUNDWATER
Location___________________________Date/Sampler
pH Buffer 7.0 pH Buffer 4.0
Specific Conductance uMHOS Well Depth
Depth to Water ______________________Casing Volume .653h1.367h
Conductivity avg pH of Water avg
Temperature avg
Conductivity________________Conductivity
pH______________________pH
Temperature Temperature
Conductivity________________Conductivity________________
pH______________________pH
Temperature Temperature
Conductivity________________Conductivity
pH________________pH________________
Temperature Temperature
Conductivity________________Conductivity
pH________________pH________________
Temperature Temperature
Comments
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Procedurcs.dpc
White Mesa Mill Standard Operating Procedures Date 8/08 Revision DUSA-3
SOP PBL-RP-
Book Radiation Protection Manual Section Page of 19
1.0 RADIATION MONITORING PERSONNEL
This section contains the following procedures for personnel radiation monitoring
including airborne particulates alpha surveys beta/gamma surveys and
urinalysis surveys
1.1 AIRBORNE PARTICULATES
Sampling for personnel exposure to airborne particulate radionuclides other than for
radon progeny will be done utilizing two distinct sampling protocols personnel
breathing zone samplers and ambient air high volume samplers Specific standard
operating procedures
for these two collection methods are described in Section 1.1.2 and
1.1.3 below
1.1.1 Frequency
For work where there is the potential to cause airborne radiation doses to site personnel
the frequency and type of air sampling to be conducted is determined from measured air
concentrations
0.01 DAC 0.1 DAC Quarterly or monthly area air sampling and/or bioassay
measurements
0.1 DAC Continuous sampling is appropriate if concentrations are
likely to exceed 0.10 DAC averaged over 40 hours or
longer
The RSO will determine the exact frequency of area air sampling breathing zone
sampling and/or bioassay measurements and determine how many workers in group of
workers performing similar jobs are to be equipped with breathing zone air samplers
Higher airborne concentrations warrant more frequent use of area air samplers bioassay
measurements and breathing zone air samplers Area air samplers may be used where
documentation exists showing the sample is equivalent to breathing zone sample
Breathing zone samples taken within one foot of the workers head are considered
representative without further documentation Breathing zone air samplers are preferred
under work conditions of higher airborne concentrations Table 1.1.1-1 below from
Regulatory Guide 8.25 provides additional guidance for the RSO in designing and
implementing air sampling programs for specific jobs
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White Mesa Mill Standard Operating Procedures
SOP PBL-RP-l
Book Radiation Protection Manual Section
Table 1.1.1-1
Air Sampling Recommendations Based on Estimated Intakes and Airborne Concentrations
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Page of 19
Workers Estimated
Annual Intake as
Fraction of ALl
Estimated Airborne
Concentrations as
Fraction of DAC
Air Sampling Recommendations
0.1 0.01
0.01
Air sampling is generally not necessary
However monthly or quarterly grab samples or
some other measurement may be appropriate to
confirm that airborne levels are indeed low
Some air sampling is appropriate Intermittent or
grab samples are appropriate near the lower end
of the range Continuous sampling is appropriate
if concentrations are likely to exceed 0.1 DAC
averaged over 40 hours or longer
0.1 0.3
0.3
Monitoring of intake by air sampling or bioassay
is required by 10 CFR 20.1502b
demonstration that the air samples are
representative of the breathing zone is appropriate
if intakes of record will be based on air
sampling and concentrations are likely to
exceed 0.3 DAC averaged over 40 hours i.e
intake more than 12 DAC-hours in week
Any annual intake Air samples should be analyzed before work
resumes the next day when potential intakes may
exceed 40 DAC-hours in week When work is
done in shifts results should be available before
the next shift ends Credit may be taken for
protection factors if respiratory protection
program is in place
Continuous air monitoring should be provided if
there is potential for intakes to exceed 40 DAC
hours in day Credit may be taken for
protection factors if respiratory protection
program is in place
White Mesa Mill Standard Operating Procedures Date 8/08 Revision DUSA-3
SOP PBL.-RP-1
Book Radiation Protection Manual Section Page of 19
1.1.2 Breathing Zone Sampling
1.1.2.1 General
Breathing zone samplers SKC pumps and accessory kits or equivalent are used to
determine airborne exposure to uranium while individuals are performing specific jobs
The units consist of portable low volume pump that attaches to the individuals belt
tygon tubing and filter holder that is attached to the individuals lapel or shirt collar The
unit monitors airborne uranium in persons breathing zone Pumps must be recharged
after to hours of use
1.1.2.2 Applicability
Breathing zone samples are required
for all calciner maintenance activities
at least quarterly during routine operating and maintenance tasks on
representative individuals performing these tasks
when radiation work permits are issued in which airborne concentrations may
exceed 25%of 1OCFR2O limits
weekly for yellowcake operations or
at the discretion of the RSO
1.1.2.3 Procedure
The procedure for collecting breathing zone sample is as follows
Secure the breathing zone sampler which has been charged and loaded with filter
paper from the radiation department
Secure the pump to the workers belt and the filter holder to the shirt collar or lapel
Try to secure pump tubing to minimize restriction of motion
Turn pump on record the time pump was turned on and continue monitoring until
the work being monitored is completed and the worker no longer is in the exposure
area Record the time at which the job is complete
Return the pump and accessories to the RSO who will remove the filter paper for
analysis Be sure to indicate accurately the total time taken by the work being
monitored
Analysis of filter samples will be performed using sensitive alpha detector The
procedure is as follows count background sample for ten minutes divide the
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SOP PBL-RP-1
Book Radiation Protection Manual Section Page of 19
background count by ten to obtain the background count rate in cpm Place the
breathing zone sample in the instrument and count the sample again for ten minutes
divide the sample count by ten to obtain the count rate in cpm subtract the
background count rate from the sample count rate and record all data on the
Breathing Zone sampling analysis form copy of which is attached
Record the total hours of exposure that are being assigned to the employee on the
Employee Exposure form which is maintained in personnel folders Be sure to
consider protection factors permitted by respirator use if the employee was also
wearing respiratory protection during the job
The number of DAC hours assigned is calculated using the following formula
DAC hours Measured air concentration Total hours of exposure
of exposure DACPF
where DAC Derived Air Concentration for uranium 10 CFR Part 20
Appendix
PF protection factor for respirator use If no respiratory
protection was used PF
The measured air concentration must be in uCilcc
1.1.2.4 Calibration
Prior to use calibration of the breathing zone samplers will be done using the Bubble
Tube Calibration method described in Section 3.2.1
1.1.2.5 Equipment Breathing Zone Sampler
The equipment used for breathing zone samples consists of
Personal sampling pumps
Gelman 37 mm Delrin filter holders or equivalent
Gelman 37 mm type A/F glass fiber filters or equivalent
Kurz Model 543 air mass flow meter or equivalent
1.1.2.6 Data Record
Data maintained on file includes
Time on and off for each sample pump
Sampling locations
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SOP PBL-RP-1
Book Radiation Protection Manual Section PageS of 19
Individuals name identification number etc
Date and sample number
Sample count rate
1.1.2.7 Calculations
The airborne concentration in uCi/cc is equal to the sample count rate minus the
background count rate in cpm divided by the instrument alpha efficiency the sample flow
rate in cc/minute the sample time in minutes and conversion factor converting dpm to
uCi
The calculation is
Equation Number
Airborne concentration Count Rate
TimeeffTjconiersion factorFlow Rate
i.e cpm-Bkg uCi 1_
cc eff2.22x lO6dpmcc/minmin
where eff cpm/dpm for counting instruments
cpm counts/mm
dpm disintegrations/min
conversion factor uci 2.22x 106 dpm
Flow Rate cc/min
Collection time mm
Once the airborne concentration has been calculated it is possible to calculate personnel
exposure in microcuries uCi Personnel exposure is determined for an individual who is
working in an area at known air concentration uCi/cc for given amount of time
hours breathing the area air at an assumed rate The breathing rate for standard person
Handbook of Radiological Health is 1.20 cubic meters per hour m3/hr
The calculation for personnel exposure is
Equation Number
Exposure uCi uCilcc1.20m3/hrhours of exposureconversion rate
where uCilcc air concentration from Equation
1.20 m3/hr breathing rate for standard man ICRP
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hours of exposure hours
conversion factor lO6cc/m3
It is also possible to determine the percent or fraction of the Derived Air Concentration
DAC for particular radionuclide using the information obtained from the exposure
calculation and dividing this value by the regulatory limit DAC listed in 10 CFR Part 20
DAC Exposure in uCiluCi limit 10 CFR Part 20
For the natural uranium U-Nat the DAC limits from 10 CFR Part 20 for insoluble Class
compounds are as follows
Weekly 1.0 i03 uCi/week
Quarterly 1.25 102 uCi/Qt
Yearly 5.0 102 uCi/yr
1.1.2.8 ALA RA/Quality Con trol
The RSO reviews each monitored result and initiates action if levels exceed 25%of 10
CFR 20 limits At minimum ten percent 10%of the air samples collected in given
quarter will be recounted using the same instrument or using different instrument and
these results will be compared to the original sample results Deviations exceeding 30%
of the original sample results will be reviewed by the RSO and the samples will be
recounted again until the sample results are determined to be consistent Additional QA
samples consisting of spiked air samples duplicate samples and blank samples will be
submitted to the radiation department for counting This will be based on ten percent
10%of the number of samples collected during quarter The sample results will be
compared to the spiked values duplicate values or blank background values of the
prepared sample Deviations exceeding 30%of the determined spiked duplicate or blank
value will be recounted If no resolution of the deviation exceeding 30%is made the QA
samples preparation will be repeated Periodic reviews by the RSO and the ALARA
audit committee will be made and documented to ensure quality maintenance and
ALARA control
1.1.3 Airborne Uranium High Volume Sampling
Grab air sampling involves passing representative sample of air through filter paper
disc via an air pump for the purpose of determining the concentration of uranium in
breathing air at that location Although the process is only measuring airborne
concentrations at specific place and at specific time the results can often be used to
represent average concentration in general area high volume sample pump will be
used for this purpose Samples will be analyzed as per standard gross alpha analysis
procedures using sensitive alpha detector
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1.1.3.1 Frequency and Locations
The following principles used for the collection of area grab samples must be considered
when collecting sample in order to obtain representative air concentration that workers
may be exposed to during their assigned work tasks
The locations selected for sampling should be representative of exposures to
employees working in the area
For special air sampling the sampling period should represent the conditions during
the entire period of exposure This may involve sampling during the entire exposure
period
For routine sampling the sampling period must be sufficient to ensure minimum
flow rate of 40 liters per minute for at least 60 minutes
Sample filters will be analyzed for gross alpha using sensitive alpha detector
Grab sampling procedures may be supplemented by use of Breathing Zone Samples
for special jobs or non-routine situations
1.1.3.2 Sampling Equipment
Monitoring equipment will be capable of obtaining an air sample flow rate of at least 40
liters per minute for one hour or longer Equipment utilized will be and Eberline RAS-1
or Scientific Industries Model H25004 or equivalent Filter media will have
maximum of 0.8 micron pore diameter Equipment is calibrated prior to each usage as
per Section 3.6 of this manual
1.1.3.3 Sampling Procedure
Steps for collection of area airborne grab samples are as follows
high volume pump will be used for sample collection
Check sample pump calibration
Locate sampler at designated site Insert clean filter using tweezers into the filter
holder on the sampler Do not contaminate the filter Log start time and Mill
operating conditions at the site
Collect sample for minimum of 60 minutes at flow rate of 40 liters per minute
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After sampling is completed carefully remove the filter using tweezers from the
filter holder and place it in clean glassine envelope or in the plastic casing furnished
with the filter
Log all sample data on the log sheet
Sample location and number also on the envelope
Time on time off and date
Mill operating conditions at the site
Samplers initials
Analyze for gross alpha
1.1.3.4 Calculations
Perform calculations as described in Section 1.1.2.7
1.1.3.5 Records
Logs of all samples taken are filed in the RSO files Data are used to calculate radiation
exposures as described in Section 4.0
Whenever grab sampling results indicate that concentrations in work locations exceed
25%of the applicable value in 10 CFR Part 20 Appendix time weighted exposures of
employees who have worked at these locations shall be computed Calculations will
reveal an individuals exposure in DAC hours This value shall be assigned to the worker
and logged onto the workers Employee Exposure to Airborne Radionuclides form
This form is in Section Whenever special air sampling programs as required for
cleanup maintenance decontamination incidents etc reveal that an employee has been
exposed to airborne radioactive material the calculated value shall also be entered on the
individuals exposure form
1.1.3.6 Quality Assurance
Calibration checks on each air sampler prior to field use ensure accurate airflow
volumes Use of tweezers and new filter storage containers minimizes contamination
potential Field logging of data during sampling and logging of identifying data on
sampled filter containers minimizes sample transposition Quality control samples will be
analyzed as described in Section 1.1.2.8
Review of data by the RSO and by the ALARA Audit committee further assures quality
maintenance
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1.2 ALPHA SURVEYS
1.2.1 Restricted Area
The Restricted Area is defined as
The property area within the chain link fence surrounding the mill property and the
area enclosed to the north and east of the facility by the posted Restricted Area fence
The active tailings and liquid waste disposal areas
All personnel who enter the Restricted Area will monitor themselves each time they leave
the Restricted Area and at the end of their shift The Radiation Safety Department will
review the monitoring information All personnel exiting the Restricted Area must initial
record of their monitoring activity
1.2.2 Instrumentation
The instrumentation utilized for personnel alpha scanning is listed in Appendix at the
end of this manual Personnel alpha survey
instruments are located at the exits from the
Restricted Area
1.2.3 Monitoring Procedures
The monitoring procedure includes the following steps
The alarm rate meter is adjusted within the range of 500 to 750 dpm/100 cm2 to
ensure margin of 250 dpm/100 cm2 due to the low efficiency of this
instrumentation
An individual monitors himself by slowly passing the detector over their hands
clothing and shoes including the shoe bottoms at distance from the surface of
approximately inch An area that is suspected of possessing any contamination i.e
hands boots visible spotting/stain on clothing etc should be carefully monitored by
placing the detector directly on the surface and note the measurement
Should an alarm be set off indicating the presence of contamination the individual
should
Resurvey themselves to verify the contamination
If contamination is present the individual must wash the affected area and
again resurvey themselves to ensure the contamination has been removed
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if the decontamination efforts by the individual are not successful then the Radiation
Safety personnel will be contacted to assess the situation Further decontamination
may be required
II an individuals clothing cannot be successfully decontaminated they must obtain
clothing from the warehouse to use and must launder the personal clothing in the
laundry room
Individual surveys are to be logged and initialed
Access to and from the Mills Restricted Area by all Mill workers contractors and
delivery personnel other than Radiation Safety and Environmental Staff Senior
Laboratory personnel Mill Management and Mill Supervisory personnel and others as
may be designated by the RSO will be limited to one or more access points as may be
designated by the RSO from time to time
Radiation Technician will be positioned at each access point designated by the RSO
under paragraph above during peak transition times such as during breaks and at
the ends of shifts to observe that each worker contractor or delivery person is
performing proper scan This paragraph will cease to apply to any such access
point if and when one or more automated full body scanners portals or the equivalent
are situated at the access point which would require workers exiting at that location
to scan themselves by exiting through the portal and the procedures in this Manual
are amended to incorporate the use and maintenance of such portal or portals
1.2.4 Training
All employees will be trained on the proper scanning procedures and techniques
1.2.5 Records
Log sheets will be collected daily and filed by the Radiation staff Records will be
retained at the Mill Contamination incidents will result in written record which is
maintained on file
1.2.6 Limits/ALARA
Contamination limits for personnel scans are set at 1000 dpm/100 square centimeters
Records will be reviewed by the RSO to maintain levels noted as low as reasonable
achievable
1.2.7 Quality Assurance
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random check of an individuals scanning technique provides quality assurance of the
monitoring procedures Daily function checks using calibrated sources assures
instrumentation performance Periodic review by the RSO and the ALARA audit
committee document and ensure quality control and ALARA maintenance
1.3 BETA-GAM1VEA SURVEYS
Site employees working within the Restricted Area will be required to wear personal
monitoring device such as TLD LUXEL badge or other NVLAP approved device
which has been approved by the RSO and the SERP during their work period The
personal monitoring devices are normally issued to each employee quarterly however
during pregnancy or if the radiological potential for exposure to an individual is
anticipated to be elevated and requires quick assessment the badges may be issued
monthly
1.3.1 Monitoring Procedures
The monitoring procedures consist of
Personnel issued personal monitoring devices will wear the device on the trunk
torso of the body or visibly on the exterior of their hard hat The personal
monitoring device records beta/gamma radiation as well as other forms of penetrating
radiation such as x-rays personal monitoring device is an exposure record of an
individuals personal exposure to radiation while on the job Therefore personal
monitoring devices are to remain at the Mill in the personal possession
of each
individual in locker or other secure area All exposure records obtained by
personal monitoring device which are not consistent with the exposure rates of work
tasks or work location measurements made throughout the Mill will be evaluated by
the RSO This evaluation will result in an investigation by the RSO and written
explanation of the findings These written records will be maintained at the Mill
Personal monitoring devices will be issued at minimum quarterly and will be
exchanged by the Radiation Safety Department Missing or lost badges will be
reported to management
Female employees that become pregnant and continue to work during the course of
their pregnancy will be placed on monthly personal monitoring device exchange
during this period NRC Regulation Guide 8.13 provides guidelines to be followed
during pregnancy and is made part of this procedure
1.3.2 Records
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The Radiation Safety Department will maintain all occupational exposure records in the
departmental files
Occupational exposure records are part of an individuals health record and as such
will be considered private information
An individual may examine his/her exposure record upon request
An employee terminating his/her employment with Denison Mines USA Corp may
request copy of his/her occupational exposure records
The Radiation Safety Department on the signature of the employee will request prior
occupational exposure records
Occupational exposure records will be made available to authorized company or
regulatory personnel
1.3.3 Quality Assurance
Periodic reviews by the RSO and the ALARA audit committee document and ensure
quality control and maintenance of conditions ALARA
1.4 URINALYSIS SURVEYS
1.4.1 Frequency
Urinalyses will be performed on those employees that are exposed to airborne
yellowcake or involved in maintenance tasks during which yellowcake dust may be
produced or routinely exposed to airbome uranium ore dust Baseline urmnalyses will
be performed prior to initial work assignments
Urine samples are collected on routine basis from mill employees as required in
Regulatory Guide 8.22 Urine samples will be collected from employees who have
worked in yellowcake packaging yellowcake precipitation grind area SAG mill ore
feed sample plant scale house and the sample preparation room every two weeks during
production periods Samples will be collected from all other employees monthly during
production periods During non-production periods bi-weekly samples will be collected
if individual exposures are expected to exceed 25%of the DAC value otherwise samples
will be collected from all employees quarterly Non-routine urinalyses will usually be
performed on employees who have been working on assignments that require Radiation
Work Permit and always on any individual that may have been exposed to airborne
uranium or ore dust concentrations that exceed the 25%of the DAC level
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1.4.2 Specimen Collection
Clean disposable sample cups with lids will be provided to each employee that will be
required to submit urine specimen The containers will be picked up at the
administration building before the individual enters the Restricted Area
The container filled with specimen will be returned to the bioassay laboratory prior to
reporting to work The name of the employee and the date of collection will be indicated
on the specimen cup
valid sample must be collected at least 40 hours but not more than 96 hours after the
most recent occupancy of the employees work area after two days but not more than
four days off
The specimen should be collected prior to reporting to the individuals work location To
prevent contamination the hands should be carefully washed prior to voiding
Under unusual circumstances where specimens cannot be collected in this manner the
worker will shower immediately prior to voiding
1.4.3 Sample Preparation
Equipment required
15 ml disposable centrifuge tubes with lids
10 ml pipette
ul pipette
lOulpipette
Disposable tips for the above pipettes
Spiking solution 0.03 or 0.02 gIl of uranium in de-ionized water
After the specimens are received they will be stored in refrigerator until they are
prepared for analysis
Sample preparation will be done in an area decontaminated to less than 25 dpm alpha
removable per 100 cm2 prior to preparation of samples All of the equipment that is
used in sample preparation will be clean and maintained in such condition
log will be prepared and the following information will be kept for each urinalysis
performed
Sample identification number
Name of employee submitting the specimen
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Date of sample collection
Date the sample was sent to the laboratory
Date the results were received
Results of the urinalysis in ugh
Indication of any spike used in ugh
The centrifuge tubes will be marked with sample identification number 10 milliliters
of urine will then be pipetted into the centrifuge tube using the pipette device To
prevent contamination new tip must be used for each specimen After each step of the
procedure the proper entry must be made in the logbook
The samples that are to be spiked for quality assurance purposes will then be prepared
The spikes will be introduced into the sample with ul or 10 ul pipettes new tip must
be used with each spike With the standard spike solution 0.03 gIl of ul spike
will result in 15 ug/l concentration for the 10 ml sample the 10 ul spike will give 30
ug/l The proper entry must be made in the logbook for each sample spiked
After preparation has been completed the QA samples are securely packaged as soon as
practicable and sent to the contract laboratory for analysis
The samples that are to be analyzed in-house will be placed in the chemistry laboratorys
refrigerator until the analysis can be completed copy of the in-house analytical
procedure is described in Section 1.4.7.6
1.4.4 Quality Assurance
To assure reliability and reproducibility of results at least 25%of the samples that are
submitted for analysis will be used for quality assurance purposes These samples will
consist of spikes duplicates and blanks samples collected from individuals known to
have no lung or systemic uranium burden
Spiked samples will be prepared as stated under sample preparation of this procedure
Duplicates will be identical samples of the same specimen and/or spikes of identical
concentrations
To assure reliability of the in-house analytical procedure 10%of the samples will be sent
to contractor laboratory for analysis These samples will contain quality assurance
items designed to provide intra-laboratory comparisons
1.4.5 Analysis
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After the samples are collected as outlined in Guide 8.22 they are identified to the lab by
collection date and number Urinalysis results must be completed and reported to the
Radiation Safety Department within seven days of the sample collection
1.4.5.1 Equipment List
Specimen collection cups with disposable lids VWR No 15708-711 or equivalent
Screw cap disposable graduated 15 ml centrifuge tubes Coming No 25310 or
equivalent
Micro-pipettes each each 10 microliters Oxford Model 7000 or equivalent
20 ml Scintillation Vials
Disposable micro-pipette tips for micro-pipettes Oxford No 910A or equivalent
Lab Oven
Hot Plate
Fume Hood
Ultrasonic Cleaner
10 ICP-MS
11 Forceps with curved tips
1.4.5.2 Reagent List
1%to 2%Nitric Acid
Concentrated Nitric Acid
Perchloric Acid Concentrated 70%
Wetting Agent
1000 ug/ml Uranium Stock Solution certified vendor prepared
Dilutions of the above stock solution replaced bi-annually Used for QA/QC
Appropriate Cleaning Solution for Ultrasonic Cleaner
Ensure that all reagents used are within their expiration dates listed on each reagent
package if applicable
1.4.5.3 Premise
portion of urine is digested in the presence of strong oxidizer and the sample is
heated at 550 degrees Celsius for hour to destroy all organics and insure proper
oxidation state of any uranium present to allow the uranium to solubilize in dilute
matrix mix
1.4.5.4 Safety Precautions
Follow laboratory guidelines when working with acids
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Utilize all appropriate PPE
All digestions must be done under working fume hood
Working with perchloric acid in the presence of organic material can be hazardous
Do not overheat to dryness Excess nitric acid is required to insure all organic material
is destroyed prior to perchloric phase of digestion
1.4.5.5 Sample Preparation Procedure
Compare sample numbering with bioassay result sheet to insure order and eliminate
discrepancies
To 20 ml scintillation vials add mls instrument grade concentrated nitric acid and
ml concentrated perchloric acid
Maintaining sample order of left to right front to back lowest sample number to
highest sample number in the set add ml to 10 ml of sample to the scintillation vial
Swirl the vial and place on hot plate again maintaining the above stated sample order
Hot plate should be set to allow sample to cook down for approximately hours prior
to perchloric phase of digestion
Cook samples down to perchloric salts If there is any brown color left in the sample
repeat digestion It is important that wet ashing of sample is complete to insure
oxidation of the uranium
Place the samples in oven at 550C for at least hour
Remove samples from the oven allow to cool and add 10 ml of 1%or 2%nitric acid
that has 0.2%wetting agent to the samples
Heat the samples to digest salts
Analyze using procedure on the ICP-MS described in section 1.4.7.6
1.4.5.6 ICP-MS Procedures
Special considerations Because of the high salt content of the samples it is necessary to
clean the skimmer and sampler cones after each use
Turn the argon on at the tank and set the delivery pressure at 80 pounds per square
inch psi
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The ICP-MS is in continuous standby mode because it is necessary to maintain
vacuum on the detector To move from the standby mode to the operating mode press
the ON button
There are two turbo vacuum pumps that need to come up to speed prior to operating
the ICP-MS While waiting for the pumps purge the interface area with argon by
pressing the and buttons The argon light will come on while the argon is
purging It is good idea to purge at least times
Turn on the exhaust fan and the water supply to the ICP-MS The water supply has to
have delivery pressure of 70 psi It may be necessary to change the filters on the
water supply in order to achieve sufficient water supply pressure The ICP-MS will
not operate below this pressure
Turn on the computer and enter the Spectro program
Press the START button to start the ignition sequence The ignition step is 60
seconds At 10 seconds the vacuum pump for the interface starts If the exhaust fan
is not on the plasma will shut off few seconds after ignition
After the plasma ignites the electronics go through check loop Avoid any input to
the computer during this time
Under the instrument window in the generator parameters turn the pump on and set
the nebulizer flow to the appropriate amount determined from previous set up
operations
Under Utilities select the Scan Manager window From this window select the time
scan that has previously been set up for your operation
10 Using the instrnment settings adjust or verify that the Rh line is about io5 counts
Close and exit Scan Manager
11 Under Measure select Quantitative and then Bioanalysis
12 After entering this window under Function select Standardize Method and follow
prompts After verifying standardization values are close to previous operation begin
sample analysis
13 Because of the nature of the sample it is necessary to aspirate blank in between
each sample After to samples the blank needs to be aspirated for sufficient
time to clean the salt build up
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14 To begin sample analysis press F2 or click the Start button at the bottom left side of
the window Record the value and move to the next sample
15 After the last sample exit window and aspirate the blank long enough to clean the
lines and chambers
16 Allow the pump to run long enough without aqueous uptake to void all lines and
chambers
17 Turn the pump off and relax lines off of pump
18 Push the STOP button to go back to the standby mode
19 After to 10 minutes turn off the water supply exhaust fan and argon
All bioassay samples need to be analyzed three working days from receipt in the
laboratory Samples are extremely susceptible to contamination Precautions should be
taken to minimize traffic and fugitive dust while samples are digesting
Volume additions are made with an auto-pipette for which the calibration has been
checked
1.4.6 Reporting and Corrective Actions
As soon as the analytical results are received they are entered in the logbook and the
entries are checked for correctness and completeness
The lab report is returned to the Radiation Safety Department with results reported as
micrograms/liter of uranium The information must be placed in the individual
employees exposure file and maintained as directed by the DRC
The Radiation Safety Department is notified immediately of any sample with
concentration greater than 35 micrograms/liter of uranium Corrective actions will be
taken when the urinary uranium concentration falls within the limits listed in Table
attached
The Radiation Safety Department should compute the error on the control spiked samples
and advise the lab if the results are more than 30%of the known values If any of the
results obtained for the quality assurance control samples are in error by 30%the
analysis must be repeated
1.5 IN-VIVO MONITORiNG
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In-vivo body counting for lung burdens of U-natural and U-235 will not be routinely
conducted Monitoring will be conducted at the discretion of the RSO in consultation
with DUSA management should potential exposure to an individual warrant
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3.0 EOUIPMENT/CALIBRATION
All radiation detection instruments used at the Mill are sent to qualified independent
laboratory for calibration every six months If necessary Radiation Safety Staff can use
the procedures outlined below to verify calibration
3.1 Counters/Detectors
3.1.1 General
All radiation detectors require determination of detector optimal voltage performance or
plateau operating point The graph of voltage applied to detector versus detector
response is referred to as plateau curve The plateau curve typically has two rapidly
sloping sections and stable flat region The optimal operating point is typically located
at the beginning of the flat or flatter section of the graph The plateau curve is specific
for particular detector and its accompanying readout or measuring meter and may vary
over time depending upon electronic component condition
The equipment used to determine detector plateau curves includes
Appropriate radiation sources
Electrostatic voltmeter
Radiation detecting instrument
Graph paper
Manufacturers technical manual
The procedure is
Ensure instrument batteries are fresh or fully charged if applicable
Turn the instrument on
Adjust the instrument voltage control starting at voltage of 600 using electrostatic
voltmeter to monitor voltage setting
Expose detector to radiation source applicable to the type of detector and in the
appropriate setting
Record voltage and instrument response for each adjustment of voltage applied
increments of 50 volts are adequate
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Repeat steps and until instrument response rapidly increases versus voltage level
At this point the detector is approaching potential differentials across the electrode
that may damage the detector
Graph instrument response versus voltage applied
Set equipment high voltage control to the optimum operating point Record on graph
voltage selected
Retain graph with calibration records
3.1.2 Function Checks
Calibration function checks are required prior to use of radiation detection instruments
used at the Mill for the purpose of verifying that the instruments are operating at the same
efficiency as when they were calibrated by the calibration laboratory i.e within 1-10%
Function checks are also used for verifying repeatability reliability and comparability of
an instruments measurements from one period to another By performing function
checks for extended time periods or on larger sample size these goals are met
Function checks involve two basic elements
calibration laboratory efficiency is compared to the instruments efficiency on the
date of the function check and
the function check is verified with check source having similar isotopic
composition as the one that was used by the calibration laboratory to calibrate the
instrument
Function checks are made for all types of radiation survey instruments The basic
principle in performing function check is measuring the radiation field using survey
instrument against known amount of radiation from calibrated source These
measurements are made for the specific type of radiation occurring For example when
performing beta/gamma survey the instrument function check is performed using
beta/gamma check source such as SrY-90 When performing an alpha survey use an
alpha check source such as Th-230 or Pu-239 for performing the function check
Function checks are documented on the Calibration Check Forms see Attachment for
copies of forms to be used for each specific instrument They will be maintained in the
instruments calibration and maintenance file
number of radiation detection instruments are used at the Mill An Instrument Users
Manual for each instrument is maintained in the calibration files together with calibration
documentation The Users Manuals are to be considered the primary reference for
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operating particular instrument This Standard Operating Procedure SOP is not
intended to replace the Users Manual but rather to supplement the Manual by providing
steps to be performed for function checks Before operating an instrument personnel
should read
the Users Manual and become familiar with the instruments operation
capabilities and special features Personnel will also receive on the job training on each
instrument
3.1.3 Alpha Monitors
Alpha particles travel very short distances in the air due to their high ionization ability
typically 1/4 to inch Due to this limitation alpha monitoring must be done at distance
of inch or less between the detector face and the source Alpha monitoring to be
consistent requires ensuring consistent distance be utilized between the detector face
and the source Alpha detectors read out in counts per minute cpm correlation
relationship known as the efficiency factor between the meter response and the actual
disintegration rate of the source is used to determine actual calibration of the meter
Radioactivity is measured in curies Ci which by definition is 3.7 1010 disintegrations
per second dps or 2.2 1012 disintegrations per minute dpm Mother measurement
unit is the Becquerel or one dps Alpha radiation is usually monitored as dpm per
surface area measured
Radiation survey equipment used at the Mill for alpha surveys are listed in Appendices
and
3.1.3.1 Calibration and Function Check Frequency
The frequency of calibration is specified in individual instrument user manuals and
manufacturers specifications
During production periods the following frequencies are observed for calibration and
function checks of radiation detection instruments
Calibration Function
Type Frequency Checks
Employee scans month days/week
Radon progeny month each use
Respirator checks month each use
Area fixed scans month Daily or each use
Area wipe scans month Daily or each use
During non-production periods the following frequencies are observed
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Book Radiation Protection Manual Section Page of 15
Calibration Function
Type Frequency Checks
Employee scans month bi-monthly
Radon progeny month each use
Respirator checks month each use
Area fixed scans month Daily or each use
Area wipe scans month Daily or each use
3.1.3.2 Function Check Procedures Alpha Counters and Scaler Instruments
The following steps will be used for function checks for alpha counters and alpha scaler
instruments
Turn the instrument on and place calibrated alpha check source in the detector
holder on or the face of the detector
Count the source for minute and record this value in cpm
Repeat step four more times
Average the five readings and divide the average in cpm by the know activity on the
alpha source This is the efficiency of the instrument and detector
Compare this efficiency with the efficiency obtained from the calibration lab if the
efficiency comparison is within 10%deviation the instrument needs is calibrated if
not the instrument needs to be recalibrated
if this efficiency comparison is within 10%deviation the instrument is in calibration
Proceed with monitoring activities
3.1.3.3 Function Check Procedures ESP-1
There are special performance considerations when using the Eberline Smart Portable
ESP-1 instrument with an Eberline AC-alpha detector because the ESP-1 contains
microcomputer to perform its internal calculations Once the user has adjusted the
calibration constant CC which is special feature of the ESP-the value obtained
during measurement event will be converted to 100%and displayed as such Adjusting
the CC of the ESP-1 in no way changes the laboratory calibration performed on the
instruments The calibration constant is set to value of one at the laboratory and
calibration proceeds as detailed by the manufacturer specifications
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The following steps will be used for function checks for the ESP-
Turn the instrument on and set the calibration constant CC to 1.00 This is the
setting the calibration laboratory uses for performing calibration of the instruments
Place calibrated alpha check source on the face of the detector and count the source
for one minute and record this value in cpm
Repeat step four more times
Average the five readings in cpm and divide by the known activity of the alpha check
source Note use an alpha check source which is the same radioisotope i.e Th-230
or Pu-239 or one of equivalent energy emission for this procedure The instrument
efficiency is now established
Compare the efficiency to the value obtained from the calibration lab If the
efficiency comparison is within 10%deviation the instrument is calibrated if not the
instrument requires recalibration
Set the calibration constant CC to the efficiency value obtained in step For
instance if the efficiency value is 20%from step change the CC from 1.00 to 0.20
This setting changes the calibration constant to the efficiency of the detector by
introducing multiplier into the microprocessor Then individual measurements are
obtained at 100%level
Place calibrated alpha check source on the detector and take five readings Average
the five readings and divide this value by the known activity of the check source
This value should be 100%5%of the known activity of the check source If it is not
within this range 100%5%readjust the CC fine tune slightly and count the source
five times and average Compare the average value to the check source keeping in
mind you want to be within 100 5.0%of the total activity of the check source
Continue this step until that objective is achieved The instrument is not only in
calibration as observed by step it is now functionally capable of measuring at 100%
efficiency Proceed with use
3.1.3.4 Calibration Procedures
All radiation detection instruments used at the Mill are sent to qualified offsite
laboratory every six months for calibration However if additional onsite calibration is
required the calibration procedures are
Set the detector high voltage at the prior determined operating point using an
electrostatic voltmeter
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For counter/scalers radon progeny/wipes close the detector without source present
obtain reading for set time This is background reading
Place calibrated source for the type of radiation being measured in the source holder
and obtain reading
Observe the counts per minute for both the background and the source
Subtract the cpm value of background from the cpm value of the source to obtain the
net cpm
Divide the net cpm value by the known dpm of the source This is the percentage
efficiency of the instrument system for this energy source
By dividing 100 by this efficiency an efficiency factor is obtained
Dpm equals the cpm divided by the efficiency of the instrument detector system
Note curie 2.22 12 dpm
microcurie 2.22 dpm
picocurie 2.22 dpin
3.1.4 Beta-gamma Monitors
Equipment utilized for beta-gamma monitoring is listed in Appendices and
3.1.4.1 Function Check Procedure
The following steps will be used for function checks on beta/gamma instruments
Turn the instrument on and place the calibrated beta/gamma SR-Y-90 check source
on the face of the detector
Let the reading stabilize to constant value
Record this value in cpm
Divide this value by the known activity on the check source This is the efficiency of
the instrument and detector
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Book Radiation Protection Manual Section Page of 15
Compare this efficiency to the efficiency obtained from the calibration laboratory If
the efficiency comparison is within 10%deviation the instrument needs is calibrated
if not the instrument needs to be recalibrated
If this efficiency comparison is within 10%deviation the instrument is in calibration
Proceed with monitoring activities
3.1.4.2 Calibration
All beta-gamma survey instruments are sent out every six months for calibration
Additional calibration if necessary may be performed on site using techniques described
in Reg Guide 8.30 Appendix Beta Calibration of Survey Instruments for calibration
performed by qualified calibration laboratory using the indicated source as listed in
Appendix
3.1.5 GammaMonitors
Instruments for gamma measurements are listed in Appendix
3.1.5.1 Calibration
Independent calibration service laboratories perform calibration every six months
Meters are calibrated to Cesium-137 or other radioisotopes as suggested by the calibration
laboratory or manufacturer Most calibration service laboratories calibrate Beta/Gamma
instruments electronically in accordance with their standard calibration procedures
However electronic calibration basically consists of the steps described below
Connect survey instrument to be calibrated to the model 500
Turn both instruments on
Record high voltage reading on model 500
Set cpm and the range multiplier on the model 500 to the desired meter deflection
The model 500 frequency controls consist of the three-digit readout range selector
coarse tuning know and the fine tuning knob The three-digit readout is in cpm times
the frequency multiplier
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Calibrating survey instruments in cpm
Set model 500 frequency to value that will provide meter deflection on the
survey instruments highest count scale Set pulse height/amplitude to twice
instrument input sensitivity
Adjust the range calibration potentiometer on the survey meter to provide correct
reading record
De-code model 500 frequency to next lower value then do the same for the
survey instrument
Adjust the range calibration potentiometer for correct reading on survey
instrument Record readings
Repeat process until all ranges have been calibrated at meter deflection Record
readings
Return to highest count scale on survey meter
Set model 500 for 1/4 scale deflection readings
Survey instrument should read within 10%of model 500 frequency Record
readings
If readings are outside of the tolerance re-calibrate for meter deflection
Tap instrument meter lightly to check for sticky meter Meter tolerance is
3%from the initial readings to the final reading
Decode 500 to next lower scale Check survey instruments for 14 scale reading
Record
Record input sensitivity
Select the most sensitive amplitude range 0-5 my on the model 500
Observe meter on survey instrument
Increase pulse amplitude switching to next higher range if necessary until the
rate meter indicates stable reading i.e further increase of pulse amplitude does
not cause an increase in meter reading Now decrease pulse height until the
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survey instrument meter reading drops 15 5%Record this pulse height as the
instrument sensitivity
If your instrument has gain or threshold control to set instrument sensitivity set
pulse height on the model 500 to desired sensitivity level Now adjust your
instrument threshold or gain control until the rate meter reading is within 85 5%
of its stable reading value see step Record the pulse height as instrument
sensitivity
Calibrating survey instrument to cps
Set frequency in model 500 Divide model 500 readings by 60 to convert to counts
per second
Repeat calibration steps as in item above
3.1.5.2 Frequency of Calibration
If electronic calibration is performed using the above method by the Radiation Safety
Department the model 500 pulse generator will be sent out for calibration on an annual
basis
3.2 PERSONNEL AIR SAMPLERS
The calibration procedure for personnel air samplers involves primary and secondary
calibration procedures Samplers will be calibrated prior to each use by either of two
methodologies bubble tube or mass flow determinations Air samplers may be calibrated
to standard air conditions
3.2.1 Bubble Tube Calibration Method
The Bubble Tube Calibration Method is primary calibration method and does not
require corrections to or from standard conditions for temperature and pressure Personal
air samplers are calibrated for the flow rate for the sampling being performed typically 2-
liters per minute
The equipment utilized is as follows
Burette 1000 ml capacity 10 ml divisions
Support iron rectangular base with rod
Burette clamps2
Soap solution dish
Tubing Gelman filter holder filter media 0.8 micron glass fiber Gelman type AlE
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Stopwatch
Small screwdriver
Sample pump
The procedures utilized are
Assemble filter train place filter in an in-line filter Attach two lengths of tubing
to each connector of the in-line filter holder
Make sure the Burette is clean Clamp the 1000 ml Burette upside down on the ring
stand with the Burette clamps
Attach the pump to be calibrated to one end of the filter train connect the other end of
the filter train to the small end of the 1000 ml Burette as per Figure
Check all tubing connections for air tightness
Pour approximately inch 12 mm of soap solution into the dish
Start the pump
Raise the dish up under the Burette opening and then immediately lower the dish
This should cause film of soap to form over the Burette opening i.e bubble
Repeat this procedure until the film bubble will travel up the inverted Burette the
length of the graduation marks on the Burette without breaking
When the film bubble has wetted the Burette
inside and will travel the entire length
of the graduated area of the Burette proceed with the actual calibration run
Quickly form three bubbles and start the stopwatch when the middle bubble is at the
bottom graduation line actually the 1000 ml mark but for purposes here it will be
called the zero line
10 Time the travel of the bubble from the zero line to the top line of the graduated
distance ml Since the capacity of the Burette is 1000 ml 1.0 liter then the
volume of air that is displaced above the bubble i.e needed to raise the bubble is
1.0 liter Stopping the stopwatch at the top mark is the time elapsed for the pump to
accomplish this The rate of rise of the bubble through the apparatus is the flow rate
of air being pulled by the pump
11 Increase or decrease the pump collection rate by adjusting the appropriate screw or
knob designed for this purpose
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Book Radiation Protection Manual Section Page 11 of 15
12 Set the pump flow collection rate to the desired valued usually between and liters
per minute for low volume collection pumps and between 30 and 80 liters per minute
for high volume collection pumps
3.2.2 Mass Flow Method
Mass flow meters are manufactured equipment designed to measure air collection flow
rates for variety of purposes Mass flow meters may be subject to temperature and
pressure corrections of air movement depending on whether they are
calibrated/manufactured for standard conditions
Utilizing an air mass flow meter traceable to NBS the airflow rate of pumps can be
quickly adjusted to correct standard flow rate conditions However the mass flow meter
must be calibrated annually using primary calibration method
The equipment consists of the following
Kurz air mass flow model 543 or equivalent
Suitable filter head adapter connections
Filter heads with filter media
Pump to be calibrated
Note The meter is calibrated directly in standard air conditions 25 29.82 Hg
The procedures utilized are
Ensure pump batteries are fully charged
Ensure flow meter batteries are fully charged
Assemble filter train
Connect with suitable adapter the Kurz probe onto the filter train Ensure an
airtight seal with tape if necessary
Set the meter function switch to the highest range 40 std liters per minute
Turn the pump on
Select appropriate range on the meter Do not allow meter needle to be forcibly
pegged
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Adjust the pump flow rate as necessary to desired flow rate Allow the meter to
stabilize before adjustment of the pump
Meter reads directly in standard air conditions correcting for temperature and
barometric pressure
Pump is now calibrated Low volume pumps are set at to 1pm
3.2.3 Electronic Calibration Method
The electronic primary gas flow calibration is the primary calibration method and does
not require corrections to or from standards conditions for temperature and pressure
Personal air samplers are calibrated for the flow rate for the sampling being performed
typically liters per minute
The equipment utilized is as follows
UltraFlo Primary Gas Flow Calibrator or equivalent
Soap solution
Tubing
Small screwdriver
Sample pump
The procedure proceeds as follows
Remove the two nipples on the back of the UltraFlo Primary Gas Flow Calibrator
Attach the connection tubing from the top nipple to the sample pump
Turn calibrator on
Turn sample pump on
Press the plunger style button on top of the soap dispensing portion of the device
Write down the digital reading from the calibrator device
Repeat steps and three times
Take an average of the three readings
If the sample pump requires adjustment take the screwdriver and adjust the set
screw on the face of the sample pump and then repeat steps through
10 After the sample pump is calibrated document the calibration on the Breathing
Zone/Radon Calibration Sheet in the Radiation department
11 Replace nipple caps on the back of the calibrator
3.3 AREA AIR SAMPLERS
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The calibration procedure for area air samplers involves one of the following procedures
Kurz Mass Flow Wet Test Gas Meter or Bubble Tube Method
3.3.1 Kurz Mass Flow Method
Repeat procedures discussed in 3.2.2 except airflow rate is adjusted to 40 slpm and
samplers utilized are
Eberline RAS-1
Scientific Industries Model H25004
Equivalent
3.3.2 Wet Test Gas Meter Method
The wet test gas meter method utilizes Precision Scientific wet test meter rated at one
cubic foot per revolution of the main dial This method is used to calibrate the Kurz air
mass flow meter in addition to direct calibration of the area air samplers
The procedures are
Attached coupling to sampler filter assembly secure it with tape
Connect wet test meter hose to coupling
Check water level of wet test meter The needle should be on slightly above the water
level
Check the thermometer temperature of the wet test meter Record this on the
calibration sheet Assume that the wet and dry bulb temperatures are the same
Turn on the sampler Check the west test meters manometer reading This reading is
obtained by adding the left and right column values typical reading might be .3
Log these values for each ball height on the Static pressure ..H20 column
For the following sampler approximate settings pull one cubic foot of air through the
wet test meter and record the time in seconds for each 20 30 40 and 50 1pm
Sampler Calibration Procedures Calculations and Equations
To convert the static pressure of the manometer attached to the wet test meter from
inches of water to inches of mercury divide the number of inches to water by 13.6
Example 0.4/13.6-0.02941176 Hg
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Book Radiation Protection Manual Section Page 14 of 15
To compute the actual flow rate rate act 1pm first divide the number of cubic
feet by the number of seconds Example ft.3/90 sec .01111 ft.3lawx Convert
the cubic feet to liters The conversion factor is 28.317 Example .01111 ft.3lsec
28.3 17 ft.3 .3 146 Llsec Multiply this by 60 to convert from seconds to minutes
Example .3 146 L/sec 60 sec 1888 L/m or 18.88 1pm
Using the Vapor Pressures of Water chart find the vapor pressure inside the wet
test meter by matching the wet bulb temperature with the corresponding vapor
pressure This number is the vapor pressure at the standard wet bulb Pvpstw
Find the vapor pressure at dewpoint using this formula Pv dewpoint Pvpstw
0.00036 13 td-tw Bp Where dry bulb temp tw wet bulb temp bp
barometric pressure in inches of mercury Assume that the dry bulb temperature
and the wet bulb temperature are the same so the difference between them will
always be zero Thus Pv dewpoint will equal Pvpstw
Determine the actual air density act with this formula
Dact 1.327
td 459.67 0.378 Pv dewpointJ
Where td dry bulb temp in degrees Bp barometric pressure in inches of
mercury Sp static pressure of wet test meter in inches of mercury
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Example
Dact 1.327
70.5 459.67
0.02941 176-0.378 .875
1.327
530.17 24773688 0.33075
0.00250297 24.44293
Dact 0.06117996
Log this in Air Density lbs/ft3 colunm of log sheet
Find the flow rate of the sampler at standard conditions std using this formula
Qstd Qact Dact
std
Where std .075 lbs/ft3
0.061 17996
i.e std 18.88
0.075
18.88 0.8157328
15.40
std 15.40 write this down for each position in the 0.075 column
3.3.3 Bubble Tube Method
Refer to Section 3.2.1 to perform this method
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Book 18 UDEQ Split Sampling Quality Assurance Plan Page of 22
GROUNDWATER QUALITY ASSURANCE PROJECT PLAN
FOR
UDEQ SPLIT SAMPLING
International Uranium USA Corporation
P.O Box 809
BlandingUT 84511
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TABLE OF CONTENTS
SECTION PAGE
white mesa mills groundwater quality assessment project plan
1.0 INTRODUCTION
2.0 DESCRIPTION AND OVERALL DATA QUALITY OBJECTIVES
2.1 INTRODUCTION
2.2 ANALYTICAL OBJECTIVES
2.3 DATA MANAGEMENT OBJECTIVES
2.4 PROJECT SCHEDULE
3.0 PROJECT ORGANIZATION AND RESPONSIBILITIES
3.1 PROJECT ORGANIZATION
3.2 RESPONSIBILITIES OFIUC PERSONNEL
3.3 RESPONSIBILITIES OF CONTRACT LABORATORY
4.0 QUALITY ASSURANCE PARAMETERS
4.1 QUALITY ASSURANCE PARAMETERS
4.1.1 PRECISION
4.1.2 ACCURACY
4.1.3 REPRESENTATIVENESS
4.1.4 COMPLETENESS
4.1.5 COMPARABILITY
4.2 FIELD ANDLABORATORY QUALITY CONTROL
4.2.1 FIELD QC CHECKS
4.2.2 FIELD QC CHECK PROCEDURES 10
4.3 LABORATORY QC CHECKS 11
4.3.1 MATRIXSPIKE 11
4.3.2 LABORATORY DUPLICATES 11
4.3.3 LABORATORY AND PREPARATION BLANKS 12
4.4 MEASUREMENT GOALS 12
4.5 FIELD MEASUREMENTS 12
5.0 SAMPLING PROCEDURES 12
6.0 SAMPLEANDDOCUMENTCUSTODYPROCEDURES 12
7.0 CALIBRATION AND FREQUENCY PROCEDURES 12
8.0 ANALYTICAL PROCEDURES 13
8.1 LABORATORY PROCEDURES 13
8.2 PHYSICAL TESTS AND FIELD PROCEDURES 13
9.0 DATA REDUCTION VALIDATION AND REPORTING 13
10.0 INTERNAL LABORATORY CHECKS 14
11.0 SYSTEM AND PERFORMANCE AUDITS 15
11.1 AUDITPROCEDURE 15
11.2 FOLLOW-UP ACTIONS 15
113 AUDITRECORDS 15
12.0 PREVENTIVE MAINTENANCE 16
13.0 DATA ASSESSMENT PROCEDURES 16
14.0 CORRECTIVE ACTION 17
15.0 QUALITY ASSURANCE REPORTS TO MANAGEMENT 17
16.0 REFERENCES 19
TABLE 1.0 ORGANIZATIONAL STRUCTURE 20
ATTACHMENT INTERPRETATION OF GROUNDWATER VOC RESULTS FROM PVC WELLS.21
ATTAChMENT ESTABLISHMENT OF BACKGROUND AND INTERPRETATION OFRESULT.22
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WHITE MESA MILLS GROUNDWATER QUALITY ASSURANCE PROJECT
PLAN
1.0 INTRODUCTION
This quality assurance program is based on EPA Guideline SW-846
NRC Regulatory Guide 4.14 and 4.15 and is designed to provide specific
guidance and quality assurance requirements for White Mesa Mills
environmental sampling activities This specific Quality Assurance QA Project
Plan is applicable to the UDEQ groundwater split sampling program It presents
the purpose organization and Standard Operating Procedures SOPs pertinent to
conducting split sampling in manner consistent with specific quality assurance
goals
Quarterly sampling of POC monitoring parameters for compliance with NRC
license conditions will be conducted in accordance with the Groundwater
Monitoring Plan and Standard Operating Procedures for Quarterly POC
Monitoring and the Groundwater Quality Assurance Project Plan for Quarterly
POC Monitoring
The quality assurance goals in this Project Plan focus on precision accuracy
completeness representativeness and comparability The QA program addresses
data quality objectives DQOs quality assurance objectives sample and
document custody procedures quality control procedures data evaluation
procedures and analytical procedures
2.0 DESCRIPTION AND OVERALL DATA QUALITY OBJECTIVES
2.1 INTRODUCTION
This document governs environmental sampling activities undertaken in
cooperation with UDEQs request for expanded sampling of groundwater
at the White Mesa Mill
2.2 ANALYTICAL OBJECTIVES
The data quality objective process described in EPA Guideline SW-
846 is used as basis for development of the analytical objectives For
analysis of the groundwater samples analytical objectives have been
developed and are described in detail in Sections 4.0 and 8.0
Analytical objectives include criteria for precision accuracy
representativeness completeness and comparability of the groundwater
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data Analytical methods used vary according to the analyses required and
according to the methods used by the laboratory Procedures regarding
review of data and data validation are included
2.3 DATA MANAGEMENT OBJECTIVES
Procedures are given to document sample quality Procedures include all SOPs
for groundwater monitoring well sampling activities Field logbooks will be kept
as described in Appendix Part II SOP No 1.0 Sample analyses from the in-
house laboratory and from the contract laboratory will be retained in the
monitoring wells file
Analytical results from the additional wells and expanded parameter list of the
UDEQ split sampling program will not be incorporated into the quarterly POC
report to NRC The quarterly POC report will contain only those parameters
which are required by the NRC license conditions and which have been sampled
and analyzed in accordance with the Groundwater Monitoring Plan and Standard
Operating Procedures for Quarterly POC Monitoring and the Groundwater
Quality Assurance Project Plan for Quarterly POC Monitoring Analytical results
and summaries from the additional wells and expanded parameter list will be
provided to IIJC management
2.4 PROJECT SCHEDULE
The groundwater project schedule is discussed in Section 1.0 of Appendix
Part Groundwater Monitoring Plan for UDEQ Split Sampling
3.0 PROJECT ORGANIZATION AND RESPONSIBILITIES
3.1 PROJECT ORGANIZATION
Project organization consists of the Environmental Coordinator reporting
to the Department Head of EA/HS The Department Head of EAIHS has
the overall responsibility for assuring that the QA program is being
followed and that QC measures are adequate The Environmental
Technician reports to the Environmental Coordinator on the progress of
groundwater sampling activities and any problems incurred In addition
both the in-house Chemist and the Laboratory Project Chemist send all
groundwater analyses to the Environmental Coordinator for review An
Organizational Chart is included in Table 1.0
3.2 RESPONSIBILITIES OF IUC PERSONNEL
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The Environmental Technician is responsible for sample collection
sample storage sample management and equipment calibration The
Technician is required to follow all SOPs relating to groundwater
sampling activities The in-house Chemist is responsible for performing
groundwater analyses for chemical analytes specified by EA/HS
department head
The Chemist is also responsible for following U.S EPA analytical
methods in Guideline SW-846 In addition White Mesa Mills
Environmental Coordinator is responsible for directing and coordinating
all environmental sampling activities The Department Head of EAJHS
will supervise all QA/QC measures to assure proper adherence to the QA
program and will determine corrective measures to be taken when
deviations from the program occur
3.3 RESPONSIBILITIES OF CONTRACT LABORATORY
The contract laboratory is responsible for providing sample analyses for
groundwater monitoring and for reviewing all analytical data to assure that
data are valid and of sufficient quality The laboratory is also responsible
for data validation in which 10%of the data is checked in reference to data
quality objectives
In addition the laboratory must adhere to the specified guidelines IUC is
requiring the laboratory to meet The guidelines the contract laboratory is
expected to follow are EPA Guideline SW-846 and NRC
Regulatory Guide 4.14 and 4.15
The contract laboratory will be chosen based on the following criteria
experience in analyzing environmental samples with detail for precision
and accuracy experience with similarmatrix analyses operation of
stringent internal quality assurance program meeting IUs
specifications ability to satisfy radionuclide requirements as stipulated
in NRC Regulatory Guide 4.14 and audit and approval of the
laboratory by IUC Details of quality assurance quality control QAIQC
requirements for laboratory performance are addressed in sections 6.0 and
15.0 respectively
4.0 QUALITY ASSURANCE OBJECTIVES FOR MEASUREMENT OF DATA
The primary QA objective for all White Mesa Mills groundwater sampling
activities is to identify and implement procedures for field sampling laboratory
analyses data management and reporting that will provide data of sufficient
quality to meet groundwater monitoring objectives
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Project objectives are previously discussed in section 2.0 The quality assurance
objectives are to document data quality in terms of precision accuracy
representativeness completeness and comparability
4.1 QUALITY ASSURANCE PARAMETERS
4.1.1 PRECISION
Precision is defined as the measure of variability that exists
between individual sample measurements of the same property
under identical conditions Precision is measured through the use
of sample splits taken at specified regular intervals Split samples
are prepared during laboratory analysis and must contain identical
concentrations of the parameters of concern
Analysis of sample splits generates an estimate of overall precision
in sampling and analysis Laboratory split analyses express
precision as relative percent difference %RPD Field and
laboratory split analyses are evaluated during data validation as
discussed in Section 9.0
4.1.2 ACCURACY
Accuracy is defined as measure of bias in system or as the
degree of agreement between measured value and an accepted or
measured value The accuracy of laboratory analyses is evaluated
based on analyzing standards of known concentration both before
and during analysis Accuracy is also measured by spiking samples
with known concentration of reagent and measuring the actual
versus expected recovery in analysis
Blank analysis also notes bias that may have occurred due to cross
contamination Analytical QC samples which will be used to
control analytical accuracy are discussed in Section 4.3 Accuracy
is moreover measured and evaluated through the Standard
Operating Procedures SOPs Accuracy is evaluated through the
use of blanks Blanks may be field blanks or equipment rinsate
blanks which may demonstrate the bias resulting from
contamination Such contamination may be due to sampling
equipment sample containers or sample handling Section 4.2
addresses quality control samples collected in the field to be used
to evaluate the accuracy of sampling activities The impact of bias
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encountered during sampling will be evaluated during data
validation as discussed in Section 9.0
4.1.3 REPRESENTATIVENESS
Representativeness is defined as the degree to which set of data
accurately represents
the characteristics of population parameter
conditions at sampling point or an environmental condition
Representativeness is controlled by collecting QC samples and
performing all sampling in compliance with the applicable
procedures Detailed sampling procedures are provided QC
samples collected in the field to control data representativeness are
discussed in Section 4.2
4.1.4 COMPLETENESS
Completeness refers to the amount of valid data obtained from
measurement system in reference to the amount that could be
obtained under ideal conditions Laboratory completeness is
measure of the number of samples submitted for analysis compared
to the number of analyses found acceptable after review of the
analytical data
4.1.5 COMPARABILITY
Comparability refers to the confidence with which one set of data
can be compared to another measuring the same property Data
can be prepared based on accuracy precision and
representativeness Data are comparable if sampling conditions
collection techniques measurement procedures methods and
reporting units are consistent for all samples within sample set
Data subject to quality assurance quality control QA/QC
measures are deemed more reliable than data without any QA/QC
measures Quality control samples which help evaluate
comparability are discussed in Section 4.3
4.2 FIELD AND LABORATORY QUALITY CONTROL
4.2.1 FIELD QC CHECKS
Field QC checks consist of field duplicates and rinsate blanks
collected and submitted to the analytical laboratory in order to
assess the quality of data resulting from the field sampling
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program Field duplicates will be analyzed to determine the
reproducibility of sampling and laboratory results
Equipment rinsate blanks will serve as check for cross-
contamination that may have occurred during the sampling process
The Standard Operating Procedures address the topics of
equipment decontamination and sampling procedures to be
followed Equipment rinsate blanks provide check for cross-
contamination by sampling equipment The frequency for
collection of equipment rinsate blanks is described in Part
Appendix Groundwater Monitoring Plan
Field Blanks will be analyzed to evaluate data accuracy through
presentation of possible bias
Trip blanks consist of distilled water samples shipped from the
laboratory carried into the field and returned to the laboratory in
the same cooler or other package as field samples Trip blanks will
be analyzed to determine whether transport field or shipping
conditions have introduced bias or variability into field samples
For the UDEQ split sampling program one trip blank per sampling
date or one trip blank per sample shipping container cooler will
be analyzed for VOCs
4.2.2 FIELD QC CHECK PROCEDURES
Field Duplicates will be used as an additional check on the
precision of laboratory analyses At least one field duplicate will
be collected during each sample event and submitted blind to the
analytical laboratory that is the sample will be numbered as if it
were another sample For the UDEQ split sampling program one
field duplicate will be collected from any one of the perched zone
monitoring wells if well recovery rates and water yields permit
Field QC check procedures will include peer review and approval
of field procedures by the Department Head of EA/HS All
procedures must be signed off by the Department Head of EAIHS
in order to be properly implemented and documented For field
QC check procedures instrument calibration of all field
instruments involved in the sampling process will be made prior to
each day of sampling Procedures for instrument calibration are
contained in the standard operating procedure
4.3 LABORATORY QC CHECKS
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The QC checks for the in-house and contract analytical laboratory will
meet or exceed the quality control measures set forth in the analytical
methods used by the laboratory Laboratory QC samples will assess the
accuracy and precision of the environmental analyses The following
describes the type of QC samples which will be used to assess the quality
of the data
4.3.1 MATRIX SPIKE
matrix spike is an environmental sample to which known
concentrations have been added The spike is taken through the
entire analytical procedure and the recovery of the analytes is
calculated Results are expressed as percent recovery of the known
amount spiked The matrix spike serves as check evaluating the
effect of the sample matrix on the accuracy of analysis
Matrix spike analyses will be documented in the field logbook and
the Chain-of-Custody form by the environmental technician using
sample identification number Extra sample volume may be
collected as needed minimum of in 20 samples shall be
designated for spike analysis The same minimum will hold true
for the in-house laboratory as well as the contract laboratory
The amount of spiked reagent to add to sample can be determined
from the following formula
Ni Vi N2 V2 where Ni is the concentration of sample
water and where N2 is the concentration of the spike reagent Vi is
the volume of the sample water V2 is the volume of reagent that
needs to be added When solving the equation V2 can be
determined
4.3.2 LABORATORY DUPLICATES
laboratory duplicate is taken as split from an environmental
sample duplicate is prepared and analyzed by identical methods
to the original sample Duplicates serve to check precision of the
analysis Results are expressed as relative percent difference
RPD between analytical results for the split and the original
sample Both the in-house and the contract lab will analyze
duplicates
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4.3.3 LABORATORY AND PREPARATION BLANKS
laboratory blank is prepared and analyzed in an identical manner
to the environmental sample preparation blank consists of
analyte-free deionized water analyzed in manner identical to the
environmental sample Contamination detected in analysis of
laboratory or preparation blanks will be used to evaluate any
laboratory contamination of groundwater samples which may have
occurred
4.4 MEASUREMENT GOALS
The objective of quality assurance is to assess the accuracy and precision
of sampling activities and laboratory methodology and to provide
quantifiable data with known accuracy and precision limits
Field activity QC objectives will be fulfilled by the approved sampling and
sample handling procedures described in the Groundwater Monitoring
Plan and the Groundwater SOPs
The accuracy and precision of laboratory analyses will be determined by
analysis of laboratory spiked samples laboratory duplicates and sample
blanks collected and analyzed with frequency as described below
Accuracy is measured as the percent recovery as the percent recovery
of known standard or spiked amount for method-specific
calibration standards and spiked field samples Precision is measured as
relative percent difference RPD for field duplicates
The frequency of the duplicates is for every 20 samples submitted The
frequency for blanks is for every 20 samples submitted Equipment
rinsate blanks will be collected each day groundwater sampling is
conducted and submitted with the quarterly samples Furthermore spike
should be performed for every 20 samples submitted
QA measurement of the representativeness of data is achieved through
analysis of field duplicates assuming that comparable sampling and
analysis procedures have been followed QA measurement of data
comparability is also achieved through analytical methods and laboratory
quality assurance programs
Laboratory quality assurance provides means for establishing consistency
in the performance of analytical procedures and assuring adherence to
analytical methods utilized Laboratory quality control programs include
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traceability of measurements to independent reference materials and
internal controls QA measurement of completeness will be evaluated
during data validation as discussed in Section 9.0 Completeness goals for
groundwater are addressed in Section 4.14
4.5 FIELD MEASUREMENTS
Measurement data will be generated for all groundwater sampling
activities and will include description of weather conditions during the
time of sample collection QA objectives for the data will be achieved by
recording field instrument calibrations and by following preventative
maintenance procedures
5.0 SAMPLING PROCEDURES
Sampling procedures for split sampling are specified in the Groundwater Standard
Operating Procedures for UDEQ Split Sampling These procedures include
procedures for preparation of sampling equipment sample designation sample
preservation and decontamination
6.0 SAMPLE AND DOCUMENT CUSTODY PROCEDURES
Sample and document custody procedures have previously been addressed in
other sections Procedures will include sample handling labeling shipping
Chain-of-Custody documents field documentation and project documentation
Verifiable sample custody will be an integral part of all field and laboratory
operations related to groundwater monitoring Traceable steps will be taken in the
field and laboratory to document that all samples have been properly acquired
preserved and identified
7.0 CALIBRATION AND FREQUENCY PROCEDURES
Calibration and frequency procedures have been previously addressed
Procedures include calibration of field and laboratory equipment and frequency of
calibration fundamental requirement for collection of valid data is the proper
calibration of all analytical instruments Calibration documents that analytical
equipment is operating properly and that data produced are within defined
calibration ranges
8.0 ANALYTICAL PROCEDURES
8.1 LABORATORY PROCEDURES
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The analytical procedures to be used by the in-house laboratory and
contract laboratory will depend on the analysis being done Methods will
vary depending on the laboratory contracted All compliance analyses will
be performed at the contract laboratory However both labs are to meet
the specifications as outlined by IUC
These specifications required both the in-house and contract laboratory to
follow NRC Regulatory Guide 4.14 and EPA Guideline SW-
846 The groundwater limits for radionuclides are given in NRC
Regulatory Guide 4.14 and the contract laboratory is expected to meet
these limits Analytical procedures are discussed in section 11.0
8.2 PHYSICAL TESTS AND FIELD PROCEDURES
Parameters such as pH and specific conductance will be measured upon
sample collection with appropriate instruments in accordance with the
procedures
The contract lab will be required to meet the guidelines specified for LLD
values for radionuclides in groundwater and may deviate from the LLD
values provided that the standard error is not greater than 10%of the
estimated value of the sample
9.0 DATA REDUCTION VALIDATION AND REPORTING
The analytical data generated by the contract laboratory will be evaluated for the
precision completeness accuracy and representativeness using specific data
validation procedures All groundwater data will go through two levels of data
review and validation The first level of review will be by the contract laboratory
data validation specialist will validate all analyses for the contract lab
Full validation will include recalculation of raw data for minimum of one or
more analytes for ten percent of the samples analyzed The remaining 90%of all
data will undergo QC review which will include validating holding times and
QC samples Overall data assessment will be part of the validation process as
well
The laboratory reviewer will evaluate the quality of the data based on NRC
guide 4.14 and on analytical methods used The reviewer will check the
following sample preparation information is correct and complete
analysis information is correct and complete appropriate laboratory SOPs are
being followed analytical results are correct and complete QC samples are
within established control limits blanks are within QC limits special
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sample preparation and analytical requirements have been met and
documentation is complete
The laboratory will prepare and retain full QC and analytical documentation The
laboratory will report the data as group of 20 or less along with the QA/QC
data The contract laboratory will provide the following information cover
sheet listing samples included in report with narrative results of compounds
identified and quantified dilution factors and reporting limits for all
analytes Also to be included are the QA/QC analytical results
The second level of review will be the responsibility of the Environmental
Coordinator The review will be objective and independent since the
Environmental Coordinator is not directly involved in the analysis of the
groundwater samples Additional chemical analyses for groundwater samples will
be provided by the in-house laboratory Other areas of interest for validation
purposes will include the review of sampling procedures rinsate blanks
laboratory blanks laboratory duplicates and spikes Laboratory analyses will also
be checked for completeness upon receipt from the contract laboratory Re-runs
will be required for samples not meeting reporting limits of LLD values
In addition the holding time for groundwater samples varies according to the
analyte being analyzed As part of the data validation process the holding time
will be compared to the date of the laboratory sample analyses and the date of
sample collection to assure validity of the analyses
10.0 INTERNAL LABORATORY CHECKS
Laboratory QA procedures will be followed to ensure proper handling and
tracking of analytical accuracy and precision Accuracy will be evaluated using
spikes blanks and duplicates All out-of-compliance results will be logged by the
laboratory QA officer with corrective actions described as well as the results of
the corrective actions taken All raw and reduced data will be stored according to
the laboratorys record keeping procedures and QA program All records will be
available for on-site inspection at any time during the course of investigation
The contract laboratory will follow specific SOPs and analytical methods used by
the laboratory SOPs will be available for on-site review by non-laboratory
personnel during the course of investigation
If re-runs occur with increasing frequency the QA officer and the project chemist
will be consulted to establish more appropriate analytical approaches to problem
samples
11.0 SYSTEM AND PERFORMANCE AUDITS
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System audits are conducted to verify documentation and implementation of the
QA program The audits also evaluate the effectiveness of the established QA
program and identify any weakness within the program needing improvement
Audits identify deviations from the QA program and verify correction of such
deviations The Department Head of EAJHS will be responsible for initiating and
overseeing system audits
Performance audits are used to assess the accuracy of measurement data through
the use of laboratory performance evaluation and blind check samples Blind
performance evaluation samples will be submitted to the contract laboratory for
analysis
11.1 AUDIT PROCEDURE
The system audits will be conducted by IIJC staff or by other qualified and
approved persons System audits will review field and laboratory
operations including sampling equipment laboratory equipment sampling
procedures and equipment calibrations to evaluate the effectiveness of the
QA program and to identify any weakness that may exist
11.2 FOLLOW-UP ACTIONS
Response to the system audits is required when deviations are found and
corrective action is required The Department Head of EAIHS in
coordination with the Environmental Coordinator will respond to each
Audit Finding Report by completing the Corrective action Reply section
on each form The response is to be completed within 20 days of receipt
and is to state the corrective measures taken for each finding The
response will include the corrective action the date of implementation
and include corrective action to prevent recurrence
113 AUDIT RECORDS
Audit records for all audits conducted to date will be retained in Central
Files These records will contain audit reports written replies records of
completion for corrective actions and any other documents associated
with the audits supporting audit findings or corrective actions
12.0 PREVENTIVE MAINTENANCE
Preventive maintenance concerns the proper maintenance and care of field and
laboratory instruments Preventive maintenance helps ensure that groundwater
data generated will be of sufficient quality to meet QA objectives Both field and
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laboratory instruments have set maintenance schedule to ensure proper
functioning of the instruments Both field and laboratory instruments will be
maintained as per the manufacturers specifications and established sampling
practice
Field instruments will be checked and calibrated prior to use Batteries will be
charged and checked daily or as needed All equipment out of service will be
immediately replaced Field instruments will be protected from adverse weather
conditions during sampling activities Instruments will be stored properly at the
end of each working day Calibration and maintenance problems encountered will
be recorded in the field logbook Calibration and maintenance procedures have
been specified
Both the in-house and the contract laboratory are responsible for the maintenance
of their instruments Preventive maintenance will be performed on scheduled
basis to minimize downtime and the potential interruption of analytical work
13.0 DATA ASSESSMENT PROCEDURES
Data assessment and review will be accomplished by the Project Chemist in
conjunction with data validation and QC review summary of this assessment
of chemical data quality will be reviewed by the Environmental Coordinator Any
problems regarding sample collection shipping handling or analysis will be
taken into consideration when evaluating the quality of the data
Both precision and accuracy of the data will be evaluated to assess the quality of
the data Assessment of data with respect to the quality assurance objectives will
be accomplished through the joint efforts of the Project Chemist Environmental
Coordinator and the Department Head of BAtHS The assessment will evaluate
sample collection sample handling field data validated blank values and any
other data flags or qualifiers
Data assessment for the UDBQ split sampling program will also consider the
impact of PVC wells on the accuracy of VOC and SVOC analytical results as
described in Attachment to this QAPP
14.0 CORRECTIVE ACTION
15.0
Both the field Technician and Project Chemist are responsible for following
procedures in accordance with the protocols established in the Quality Assurance
Project Plan Corrective action should be taken for any procedure deficiencies or
deviations noted in the groundwater monitoring program All deviations from
field sampling procedures will be noted in the field logbook Any QA/QC
problems that arise will be brought to the immediate attention of the
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Environmental Coordinator Laboratory deviations will be recorded by the QA
officer in logbook as well
Corrective actions will be made and documented when procedures are not strictly
in compliance with the established protocol Data associated with these
deviations is considered suspect Additional samples or measurements will be
taken in the field to replace data considered suspect Upon implementation of
corrective action memorandum documenting the field corrective action will be
placed in the monitoring well files and in Central Files
Corrective action for laboratory deviations will be the responsibility of both the
Environmental Coordinator and Laboratory Supervisor Any deviation apparent
during analysis will be addressed and corrective action will be taken when deemed
necessary All corrective measures will be documented and filed
15.0 QUALITY ASSURANCE REPORTS TO MANAGEMENT
The Environmental Technician will report to the Environmental Coordinator
regularly regarding progress of the groundwater sampling program The
technician will also brief the coordinator on any QA/QC issues associated with
groundwater sampling activities The in-house and contract laboratories maintain
detailed procedures for laboratory record keeping Each data set report submitted
to the Environmental Coordinator will contain the laboratorys certification of the
analytical methods performed and identify all QC/QC measures not within the
established control limits Any QA/QC problems will be brought to the
Environmental Coordinators attention as soon as possible
After sampling has been completed and final analyses are completed and
reviewed brief data evaluation summary report will be prepared The report
will summarize the data validation efforts and provide an evaluation of the data
quality in regard to precision accuracy and completeness The final summary
will be prepared by the Project Chemist for the contract lab and by the staff
Chemist at the in-house lab The final summary will be reviewed by the
Environmental Coordinator If UDEQ split sampling and quarterly POC sampling
are conducted on the same dates analytical results from the additional wells and
expanded parameter list of the UDEQ split sampling program will not be
incorporated into the quarterly POC report The quarterly POC report will contain
only those parameters which are required by the NRC license conditions and
which have been sampled and analyzed in accordance with the Groundwater
Monitoring Plan and Standard Operating Procedures for Quarterly POC
Monitoring and the Groundwater Quality Assurance Project Plan for Quarterly
POC Monitoring
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16.0 REFERENCES
Environmental Protection Agency EPA 1986 Test Methods for
Evaluating Solid Waste SW-846 Third Edition November
Environmental Protection Agency EPA 1987 Data Quality
Objectives for Remedial Response Activities Development Process
EPA/540/g-87/003 and Data Quality Objectives for Remedial Response
Activities Example Scenario RIJFS Activities at Site with
Contaminated Soils and Groundwater EPA/540/G-87/004
Environmental Protection Agency EPA 1988a Laboratory
Validation Functional Guidelines for Evaluating Organic Analyses
February
Environmental Protection Agency EPA 1988b Laboratory Data
Evaluation Functional Guidelines for Evaluating Inorganic Analysis July
Environmental Protection Agency EPA 1990 National
Functional Guidelines for Organic Data Review Revised June
Nuclear Regulatory Commission NRC 1980 Radiological
Effluent and Environmental Monitoring at Uranium Mills Regulatory
Guide 4.14 April
Nuclear Regulatory Commission NRC 1979 Quality Assurance
for Radiological Monitoring Programs Effluent Streams and the
Environment Regulatory Guide 4.15 February
Umetco White Mesa Mill 1990 White Mesa Procedures Manual for
Groundwater Hydrology
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TABLE 1.0
ORGANIZATIONAL STRUCTURE
Date 07/99 Revision
Page 18 of 22
DEPARTMENT HEAD OF EA/HS
ENVIRONMENTAL COORDINATOR
ENVIRONMENTAL TECHNICIAN
IN-HOUSE CHEMIST LABORATORY PROJECT CHEMIST
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ATTACHMENT
Interpretation of Groundwater VOC Results from PVC Wells
As has been noted in correspondence between IIJSA and UDEQ EPA and others have
conducted numerous evaluations of what impact PVC well casings may have on
groundwater sampling results for VOCs These studies have often resulted in
significantly different conclusions However the vast majority have concluded that PVC
is capable of sorb ing and leaching organic constituents These varying conclusions reflect
different interpretations of what constitutes significant parameter interference In some
cases PVC interference may be insignificant while in others it may seriously bias the
analytical results Regardless EPA continues to advise against the use of PVC well
casing where dilute organic concentrations are expected or are of interest
With this in mind it should be possible to collect worthwhile groundwater samples from
the existing PVC-Ocased wells at the Mill as long as the results are analyzed with PVC
interference in mind If high concentrations were to be encountered greater than
mgfL it is unlikely that leaching from PVC casing would present any significant bias
However should analytical results indicate low level detection of organic compounds in
number of the wells the detected parameters should be compared to the list of those
known to leach from PVC or glued joints Given that the limit of detection of EPA
method 8260 is ugIL analytical results for parameters known to leach from PVC or
glued joints near the detection level could realistically be produced by PVC interference
and should be attributed to that source
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ATTACHMENT
Establishment of Background and Interpretation of Results from UDEQ Split
Sampling
2.1 Wells to be Sampled for UDEQ Split Sampling Program
The UDEQ split sampling program involves sampling of the following IUSA
wells
Culinary Wells Energy Fuels Wells and
Monitoring Wells MW-i MW-2 MW-3 MW-4 MW-5 MW-li MW-12
MW-14 MW-iS MW-17 MW-18 and MW-19
These wells can be separated into two categories with respect to status of
background values
Wells that have been monitored as part of the ongoing NRC quarterly
monitoring and for which intra-well background has been established for the
POC monitoring parameters Specifically wells MW-5 -ii -12 -14 -15 and
-17 have been monitored and intra-well background established for chloride
nickel potassium and U-Nat
Wells for which background has not been established for some or all of the
extended list of parameters Background has not been established for MW-5
ii -12 -14 -15 and -17 for components of the extended list of parameters
that are not POC monitoring parameters that is any parameters other than the
four identified above For the remaining wells proposed by UDEQ including
the culinary wells and the Ute wells IUC has not established background for
any of the parameters in the extended list
2.2 Background for Wells in the Perched Zone
Due to the temporal and spatial variations in water quality in the perched zone
UDEQ has agreed with JUSA that an intra-well comparison is the most
appropriate method for evaluation of White Mesa Mill groundwater data IUSA
currently utilizes the Shewhart CUSUM control chart method described in Section
3.0 of the White Mesa Mill Points of Compliance POC Report Titan
Environmental September 1994 for establishment of background and evaluation
of ongoing analytical results for the POC parameters reported quarterly for wells
MW-S -11 -12 -14 -15 and -17 EPA recommends this method in their
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guidance document Statistical Evaluation of Groundwater at RCRA Facilities
USEPA April 1989
I1JSA will also utilize the Shewhart-CUSUM method for
Establishing background for additional parameters to be analyzed during the split
sampling program for POC wells MW-5 -11 -12 -14 -15 and 17
Evaluating ongoing analytical results for both POC parameters and additional
parameters to be analyzed during the split sampling program for POC wells MW
5-il -12 -14 -15 and 17
Establishing background for all parameters to be analyzed during the split
sampling program for additional wells MW -1 MW-2 MW-3 MW-4 MW-18
andMW-19
Evaluating ongoing analytical results for all parameters to be analyzed during the
split sampling program for additional wells MW -1 MW-2 MW-3 MW-4 MW-
18 and MW-19
2.3 Background for Entrada/Navajo Wells
IIJSA will also utilize the Shewhart-CUSUM method for
Establishing background for all parameters to be analyzed during the split
sampling program for culinary wells and
Evaluating ongoing analytical results for all parameters to be analyzed during the
split sampling program for culinary wells and
2.4 Consideration of Historic Information in the Evaluation of New
Groundwater Data
In evaluating analytical results from both the perched zone wells in the Dakota
Sandstone and the culinary wells in the Navajo Sandstone consideration will be
given to the fact that previous data not included in the eight periods of data used
to establish background under the Shewhart-CUSUM method indicate that certain
analytes were already elevated in natural background Attachment Table
identifies the parameters that have been shown to be elevated due to natural
geochemical phenomena in both formations
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Book 18 UDEQ Split Sampling Quality Assurance Plan Page 22 of 22
Attachment Table
Summary of Water Quality Results Prior to White Mesa Mill Startup
Background Well or Source Metals Elevated Ions Elevated
Sample Formation Above Acceptable Above Acceptable
Levels Levels
G2R Navajo Sandstone iron
Cottonwood Creek 01 Dakota Sandstone arsenic2 sulfate2
iron2
selenium2
Cottonwood Creek 03 Dakota Sandstone arsenic2 sulfate2
iron2
selenium2
Cottonwood Creek G4 Dakota Sandstone arsenic2 sulfate2
iron2
selenium2
Cottonwood Creek 05 Dakota Sandstone arsenic2 sulfate2
iron2
selenium2
Stock Well G6R Dakota Sandstone arsenic sulfate
iron1
lead1
Stock Well G7R Dakota Sandstone arsenic sulfate
iron1
lead
Culinary Well Navajo Sandstone iron3 sulfate3
Culinary Well Navajo Sandstone sulfate3
Culinary Well Navajo Sandstone sulfate3
Culinary well Navajo Sandstone sulfate3
Notes
Environmental Report Dames Moore 1978 Includes results confinned by Utah State Division of
Health Laboratory
Environmental Statement USNRC 1979 Includes results confirmed by Utah State Division of
Health Laboratory
Pre-Startup Data Review DAppolonia 1981 Includes results confirmed by Utah State Division of
Health Laboratory
C\Documents and settings\dliydenlund\.Local Settings\Temporary Internet FiIesContent.Outlook\15CXRH6Z\UDEQ Groundwater
QA Plan.doc
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WHITE MESA URANIUM MILL
GROUND WATER MONITORING
QUALITY ASSURANCE PLAN QAP
STATE OF UTAH
GROUNDWATER DISCHARGE PERMIT No UGW370004
Denison Mines USA Corp
P.O Box 809
landing UT 84511
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TABLE OF CONTENTS
Page
INTRODUCTION
ORGANIZATION AND RESPONSIBILITIES
2.1 Functional Groups
2.2 Overall Responsibility For the AQ/QC Program
2.3 Data Requestors/Users
2.4 Data Generators
2.4.1 Sampling and QC Monitors
2.4.2 Analysis Monitor
2.4.3 Data Reviewers/Approvers
2.5 Responsibilities of Analytical
Laboratory
QUALITY ASSURANCE OBJECTIVES FOR MEASUREMENT OF DATA
3.1 Precision
3.2 Accuracy 10
3.3 Representativeness 10
3.4 Completeness 10
3.5 Comparability 11
FIELD SAMPLING QUALITY ASSURANCE METHODOLOGY 11
4.1 Controlling Well Contamination 11
4.2 Controlling Depth to Groundwater Measurements 11
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4.3 Water Quality QC Samples 11
4.3.1 VOCTripBlanks 11
4.3.2 Equipment Rinsate Samples 12
4.3.3 Field Duplicates 12
4.3.4 Definition of Batch 12
CALIBRATION 12
5.1 Depth to Groundwater Measurements 13
5.2 Water Quality 13
GROUND WATER SAMPLING AND MEASUREMENT OF FIELD 13
PARAMETERS
6.1 Groundwater Head Monitoring 13
6.1.1 Location and Frequency of Groundwater Head Monitoring 13
6.1.2 Equipment Used For Groundwater Head Monitoring 14
6.1.3 Field Sampling Procedure for Groundwater Head Monitoring 14
6.2 Ground Water Compliance Monitoring 14
6.2.1 Location and Frequency of Groundwater Compliance Monitoring 14
6.2.2 Quarterly and Semi-Annual Sampling Required Paragraphs I.E.1.a orl.E.1.b of the 15
GWDP
6.2.3 Quarterly or Monthly Sampling Required Under Paragraphs I.G or I.G.2 of the 15
GWDP
6.2.4 Sampling Equipment for Groundwater Compliance Monitoring 15
6.2.5 Decontamination Procedure 16
6.2.6 Pre Purging/Sampling 17
Activities
6.2.7 Well Purging/Measurement of Field Parameters 17
6.2.8 Samples to be Taken and Order of Taking Samples 20
6.2.9 Field Duplicate 20
Samples
6.2.10 VOCs and Nutrient Sampling 21
6.2.11 Heavy Metals All Other Non-Radiologics and Gross Alpha Sampling 21
6.2.12 Procedures to Follow After Sampling 24
SAMPLE DOCUMENTATION TRACKING AND RECORD KEEPING 25
7.1 Field Data Worksheets 25
7.2 Chain-Of-Custody and Analytical Request Record 26
7.3 Record Keeping 26
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ANALYTICAL PROCEDURES AND QA/QC 27
8.1 Analytical Quality Control 27
8.1.2 Spikes Blanks and Duplicates 27
8.2 Analytical Laboratory Procedures 28
INTERNAL QUALITY CONTROL CHECKS 31
9.1 Field QC Check Procedures 31
9.1.1 Review of Compliance With the Procedures Contained in this Plan 31
9.1.2 Analyte Completeness Review 31
9.1.3 Blank Comparisons 31
9.1.4 Duplicate Sample Comparisons 31
9.2 Analytical Laboratory QA Reviews 32
9.3 QA Manager Review of Analytical Laboratory Results and Procedures 33
9.4 Analytical Data 34
10 CORRECTIVE ACTION 34
10.1 When Corrective Action is Required 34
10.2 Procedure for Corrective Action 35
11 REPORTING 35
12 SYSTEM AND PERFORMANCE AUDITS 36
12.1 QA Manager to Perform System Audits and Performance Audits 36
12.2 System Audits 36
12.3 Performance Audits 37
12.4 Follow-Up Actions 37
12.5 Audit Records 37
13 PREVENTIVE MAINTENANCE 37
14 QUALITY ASSURANCE REPORTS TO MANAGEMENT 38
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14.1 Ongoing QAIQC Reporting 38
14.2 Periodic Reporting to Management 38
15 AMENDMENT 39
16 REFERENCES 39
Appendices
Appendix A-Chloroform Investigation Monitoring Quality Assurance Program
Li
11
ii
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INTRODUCTION
This Groundwater Monitoring Quality Assurance Plan the Plan details and describes all
sampling equipment field methods laboratory methods qualifications of environmental
analytical laboratories data validation and sampling and other corrective actions necessary
to comply with UAC R3 17-6-6.3I and at the White Mesa Uranium Mill the Mill as
required under paragraph I.H.6 of State of Utah Groundwater Discharge Permit No
UGW370004 the GWDP for the Mill This Procedure incorporates the applicable
provisions of the United States Environmental Protection Agency EPA RCRA
Groundwater Monitoring Technical Enforcement Guidance Document OSWER-9950
September 1986 as updated by EPAs RCRA Ground-Water Monitoring Draft Technical
Guidance November 1992
Activities in an integrated program to generate quality data can be classified as management
i.e quality assurance or QA and as functional i.e quality control or QC The
objective of this Plan is to ensure that monitoring data are generated at the Mill that meet the
requirements for precision accuracy completeness representativeness and comparability
required for management purposes and to comply with the reporting requirements established
by applicable permits and regulations
ORGANIZATION AND RESPONSIBILITIES
2.1 Functional Groups
This Plan specifies roles for QA Manager as well as representatives of three different
functional groups the data users the data generators and the data reviewers/approvers The
roles and responsibilities of these representatives are described below
2.2 Overall Responsibility For the QAJQC Program
The overall responsibility for ensuring that the QAIQC measures are properly employed is
the responsibility of the QA Manager The QA Manager is typically not directly involved in
the data generation i.e sampling or analysis activities At the Mill the QA Manager is the
Mills Radiation Safety Officer RSO or other qualified person designated by Denison
Mines USA Corp DUSA corporate management
2.3 Data Requestors/Users
The generation of data that meets the objectives of this Plan is necessary for management to
make informed decisions relating to the operation of the Mill facility and to comply with the
reporting requirements set out in the GWDP and other permits and applicable regulations
Accordingly the data requesters/users the Data Users are therefore DUSAs corporate
management and regulatory authorities through the implementation of such permits and
regulations The data quality objectives DQOs required for any groundwater sampling
event such as acceptable minimum detection limits are specified in this Plan
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2.4 Data Generators
The individuals who carry out the sampling and analysis activities at the request of the Data
Users are the data generators For Mill activities this involves sample collection record
keeping and QA/QC activities conducted by one or more sampling and quality control/data
monitors each Sampling and QC Monitor The Sampling and QC Monitors are
radiation and environmental technicians or other qualified Mill personnel as designated by
the QA Manager The Sampling and QC Monitors perform all field sampling activities
collect all field QC samples and perform all data recording and chain of custody activities in
accordance with this Plan Data generation at the contract analytical laboratory the
Analytical Laboratory utilized by the Mill to analyze the environmental samples is
performed by or under an employee or agent the Analysis Monitor of the Analytical
Laboratory in accordance with specific requirements of the Analytical Laboratorys own
QA/QC program
The responsibilities of the data generators are as follows
2.4.1 Sampling and QC Monitors
The Sampling and QC Monitors are responsible for field activities These include
Ensuring that samples are collected preserved and transported as specified in Plan
Checking that all sample documentation labels field data worksheets chain-of-
custody records packing lists is correct and transmitting that information along
with the samples to the Analytical Laboratory in accordance with this Plan
Maintaining records of all samples tracking those samples through subsequent
processing and analysis and ultimately where applicable appropriately disposing
of those samples at the conclusion of the program
Preparing quality control samples for field sample collection during the sampling
event
Preparing QC and sample data for review by the QA Manager and
Preparing QC and sample data for reporting and entry into computer data base
where appropriate
2.4.2 Analysis Monitor
The Analysis Monitor is responsible for QA/QC activities at the Analytical Laboratory
These include
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Training and qualifying personnel in specified Analytical Laboratory QC and
analytical procedures prior to receiving samples
Receiving samples from the field and verifying that incoming samples correspond to
the packing list or chain-of-custody sheet and
Verifying that Analytical Laboratory QC and analytical procedures are being
followed as specified in this Plan by the Analytical Laboratorys QA/QC program
and in accordance with the requirements for maintaining National Environmental
Laboratory Accreditation Program NELAP and/or National Voluntary
Laboratory Accreditation Program NAVLAP certification
2.4.3 Data Reviewers/Approvers
The QA Manager has broad authority to approve or disapprove project plans specific
analyses and final reports In general the QA Manager is responsible for reviewing and
advising on all aspects of QA/QC including
Ensuring that the data produced by the data generators meet the specifications set out
in this Plan
Making on-site evaluations and submitting audit samples to assist in reviewing
QA/QC procedures
Determining with the Sampling and QC Monitor and Analysis Monitor appropriate
sampling equipment and sample containers in accordance with this Plan to
minimize contamination and
Supervising all QA/QC measures to assure proper adherence to this Plan and
determining corrective measures to be taken when deviations from this Plan occur
The QA Manager may delegate certain of these responsibilities to one or more Sampling and
QC Monitors or to other qualified Mill personnel
2.5 Responsibilities Of Analytical Laboratory
Unless otherwise specified by DUSA corporate management all environmental analysis of
groundwater sampling required by the GWDP or by other applicable permits will be
performed by contract Analytical Laboratory
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The Analytical Laboratory is responsible for providing sample analyses for groundwater
monitoring and for reviewing all analytical data to assure that data are valid and of sufficient
quality The Analytical Laboratory is also responsible for data validation in accordance with
the requirements for maintaining NELAP and/or NAVLAP certification
In addition to the extent not otherwise required to maintain NELAP and or NAYLAP
certification the Analytical Laboratory must adhere to EPA Guideline SW-846 and to
the extent consistent with NELAP and EPA practices the applicable portions of NRC
Regulatory Guide 4.14
The Analytical Laboratory will be chosen by DUSA and must satisfy the following criteria
experience in analyzing environmental samples with detail for precision and accuracy
experience with similar matrix analyses operation of stringent internal quality
assurance program meeting NELAP and/or NAYLAP certification requirements and that
satisfies the criteria set out in Section below ability to satisfy radionuclide requirements
as stipulated in the applicable portions of NRC Regulatory Guide 4.14 and certified by
the State of Utah for and capable of performing the analytical methods set out in Table
The analytical procedures used by the Analytical Laboratory will be in accordance with Utah
Administrative Code R3 17-6-6.3L
QUALITY ASSURANCE OBJECTIVES FOR MEASUREMENT OFDATA
The objective of this Plan is to ensure that monitoring data are generated at the Mill that meet
the requirements for precision accuracy representativeness completeness and
comparability required for management purposes and to comply with the reporting
requirements established by applicable permits and regulations the Field and Analytical QC
samples described in Sections 4.3 and 8.1 below are designed to ensure that these criteria are
satisfied Data subject to QA/QC measures are deemed more reliable than data without any
QAIQC measures
3.1 Precision
Precision is defined as the measure of variability that exists between individual sample
measurements of the same property under identical conditions Precision is measured
through the analysis of samples containing identical concentrations of the parameters of
concern For duplicate measurements precision is expressed as the relative percent
difference RPD of data pair and will be calculated by the following equation
RPD /2 100
Where original and duplicate are the reported concentration for field duplicate
samples analyses or in the case of analyses performed by the Analytical Laboratory the
percent recoveries for matrix spike and matrix spike duplicate samples EPA SW-846
Chapter Section 5.0 page 28
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3.2 Accuracy
Accuracy is defined as measure of bias in system or as the degree of agreement between
measured value and an accepted or measured value The accuracy of laboratory analyses is
evaluated based on analyzing standards of known concentration both before and during
analysis Accuracy will be evaluated by the following equation EPA SW-846 Chapter
Section 5.0 page 24
Recovery A-B I/C 100
Where
the concentration of analyte in sample
the concentration of analyte in an unspiked sample
the concentration of spike added
3.3 Representativeness
Representativeness is defined as the degree to which set of data accurately represents
the
characteristics of population parameter conditions at sampling point or an
environmental condition Representativeness is controlled by performing all sampling in
compliance with this Plan
3.4 Completeness
Completeness refers to the amount of valid data obtained from measurement system in
reference to the amount that could be obtained under ideal conditions Laboratory
completeness is measure of the number of samples submitted for analysis compared to the
number of analyses found acceptable after review of the analytical data Completeness will
be calculated by the following equation
Completeness Number of valid data points/total number of measurements 100
Where the number of valid data points is the total number of valid analytical measurements
based on the precision accuracy and holding time evaluation Completeness is determined
at the conclusion of the data validation
Executive Secretary approval
will be required for any completeness less than 100 percent
3.5 Comparability
Comparability refers to the confidence with which one set of data can be compared to
another measuring the same property Data are comparable if sampling conditions collection
techniques measurement procedures methods and reporting units are consistent for all
samples within sample set
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FIELD SAMPLING QUALITY ASSURANCE METHODOLOGY
4.1 Controlling Well Contamination
Well contamination from external surface factors is controlled by installation of cap over
the surface casing and cementing the surface section of the drill hole Wells have surface
covers of mild steel with lockable cap cover Radiation Safety staff has access to the keys
locking the wells
Subsurface well stagnation for pumped wells is reduced by pumping two well casing
volumes of water from the wells to the extent practicable This ensures to the extent
practicable that the aquifer zone water is being drawn into the well and is representative
sample
4.2 Controlling Depth to Groundwater Measurements
Monitoring of depth to groundwater is controlled by comparing historical field log data to
actual measurement depth This serves as check of the field measurements
4.3 Water Quality QC Samples
Quality assurance for ground water monitoring consists of the following QC samples
4.3.1 VOC Trip Blanks
Trip blanks will be used to assess contamination introduced into the sample containers by
volatile organic compounds VOCs through diffusion during sample transport and storage
At minimum at least one trip blank will be in each shipping container containing samples
to be analyzed for VOCs Trip blanks will be prepared by the Analytical Laboratory
transported to the sampling site and then returned to the Analytical Laboratory for analysis
along with the samples collected during the sampling event The trip blank will be unopened
throughout the transportation and storage processes and will accompany the technician while
sampling in the field DTG Field and Laboratory Quality Assurance/Quality control 7.8
pages 7-30 7-3
43.2 Equipment Rinsate Samples
Where portable non-dedicated pump is used rinsate sample will be collected prior to
using and after decontaminating the sampling equipment at the beginning of each sampling
event and at the beginning of each day of the sampling event TEGD Field QA/QC Program
page 119 Where non-dedicated bailer is used rinsate sample will be collected prior to
any well sampling or purging and after decontamination at the beginning of each sampling
event and at the beginning of each day of the sampling event In the case of equipment
rinsate blank samples for pump the sample will be prepared by pumping de-ionized water
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into the sample containers In the case of equipment rinsate blank samples for non-
disposable or non-dedicated bailer the sample will be prepared by pouring de-ionized water
over and through the bailer and into the sample containers During quarterly/semi-annual
monitoring events equipment rinsate blanks will need to be analyzed only for the
contaminants required during the accelerated monitoring event
4.3.3 Field Duplicates
One Duplicate set of samples submitted with each Batch defined in Section 4.3.4 of
samples DTG Field and Laboratory Quality Assurance/Quality Control 7.8 taken from
one of the wells being sampled and will be submitted to the Analytical Laboratory and
analyzed for all contaminants listed in Table of the GWDP EPA SW-846 Chapter
Section 3.4.1
4.3.4 Definition of Batch
For the purposes of this Plan Batch is defined as 20 or fewer samples PA SW-846 Chapter
Section 5.0 page 23
CALIBRATION
fundamental requirement for collection of valid data is the proper calibration of all sample
collection and analytical instruments Sampling equipment shall be calibrated in accordance
with manufacturers recommendations and Analytical Laboratory equipment shall be
calibrated in accordance with Analytical Laboratory procedures
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5.1 Depth to Groundwater Measurements
Equipment used in depth to groundwater measurements will be checked prior to each use to
ensure that the Water Sounding Device is functional
5.2 Water Quality
The Field Parameter Meter will be calibrated prior to each sampling event and at the
beginning of each day of the sampling event according to manufacturers specifications for
example by using two known pH solutions and one specific conductance standard
Temperature will be checked comparatively by using thermometer Calibration results will
be recorded on the Field Data Worksheet
GROUND WATER SAMPLING AND MEASUREMENT OF FIELD
PARAMETERS
6.1 Groundwater Head Monitoring
6.1.1 Location and Frequency of Groundwater Head Monitoring
Depth to groundwater shall be measured quarterly in the following wells and piezometers
All Point of Compliance wells listed in paragraphs 6.2.1 and below
Monitoring wells MW-20 and MW-22
All piezometers P-l P-2 P-3 P-4 and P-5
All chloroform contaminant investigation wells required to be monitored during
the quarter under State of Utah Notice of Violation and Groundwater Corrective
Action Order UDEQ Docket No UGQ-20-O1 not already included in paragraph
On November 17 2006 such chloroform contaminant investigation wells
were the following
MW-4 TW4-10
TW4-1 TW4-11
TW4-2 TW4-12
TW4-3 TW4-13
TW4-4 TW4-14
TW4-5 TW4-16
TW4-6 TW4-18
TW4-7 TW4-19
TW4-8 TW4-20
TW4-9 TW4-21
TW4-22
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In any other wells or piezometers required by the Executive Secretary of the Utah
Radiation Control Board as indicated by the Mills RSO
6.1.2 Equipment Used For Groundwater Head Monitoring
Measurement of depth to groundwater is accomplished by using Solinist IT 300 or
equivalent device the Water Sounding Device
6.1.3 Field Sampling Procedure for Groundwater Head Monitoring
In the case of any well that is being sampled for groundwater quality depth to groundwater is
measured prior to sampling
Depth to groundwater is measured from the top of the inner well casing or for the
piezometers from the top of the casing and is recorded on the Field Data Worksheet for
Groundwater described in Section 7.1 the Field Data Worksheet Readings are taken by
lowering the Water Sounding Device into the casing until the Device alarms indicating that
the water surface has been reached The depth to groundwater is then determined by
reference to the distance markings on the line attached to the Device Data is recorded on the
Field Data Worksheet as Depth to Water to the nearest 0.01 of foot
6.2 Ground Water Compliance Monitoring
6.2.1 Location and Frequency of Groundwater Compliance Monitoring
Groundwater quality shall be measured in the following wells at the following frequencies
Semi-annually in the following Point of Compliance wells MW-i MW-2 MW-
MW-5 MW-i2 MW-i5 MW-i7 MW-i8 and MW-19
Quarterly in the following Point of Compliance wells MW-il MW-i4 MW-20
MW-22 MW-26 and MW-32 and
Quarterly in the following new Point of Compliance wells until quarters of
background data are obtained MW-23 MW-24 MW-25 MW-27 MW-28
MW-29 MW-30 and MW-3 Thereafter these wells will be sampled on
quarterly or semi-annual basis as required by the GWDP
Chloroform Investigation sampling will collected from the locations and at the
frequencies listed at Item in the Chloroform Investigation Monitoring Quality
Assurance Program Appendix to this document
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In addition quarterly or monthly sampling may be required for certain parameters in certain
wells for which accelerated monitoring is required under paragraph I.G.1 or I.G.2 of the
GWDP It is important to confirm with the Mills RSO prior to conducting any monitoring
well sampling whether or not any parameters in any wells are subject to this accelerated
monitoring
6.2.2 Quarterly and Semi-Annual Sampling Required Under Paragraphs I.E.1.a or
I.E.1.b of the GWDP
All quarterly and semi-annual samples collected under paragraphs 6.2.1 and above
paragraphs I.E .a or T.E .h of the GWDP shall be analyzed for the following parameters
Field parameters depth to groundwater pH temperature specific conductance
redox potential Eh and turbidity in the manner specified in paragraph 6.2.7
and
Laboratory Parameters
All parameters specified in Table of the GWDP and
ii General inorganics chloride sulfate carbonate bicarbonate sodium
potassium magnesium calcium and total anions and cations
6.2.3 Quarterly or Monthly Sampling Required Under Paragraphs I.G.1 or I.G.2 of the
GWDP
Any quarterly or monthly sampling required under paragraphs I.G or I.G.2 of the GWDP
shall be in the wells and for the specific parameters required by those paragraphs of the
GWDP as specified by the Mills RSO
6.2.4 Sampling Equipment for Groundwater Compliance Monitoring
All equipment used for purging and sampling of groundwater which enters the well or may
otherwise contact sampled groundwater shall be made of inert materials
For the purposes of this QAP the following equipment definitions shall apply
Dedicated Bailer bailer that is dedicated to be used at one specific well
for the use of purging or sampling Said bailer well remain with and in side
the well casing suspended and secured
Non Dedicated Bailer bailer that is used for purging and sampling at
one or more well
Dedicated Pump pump that is dedicated to one specific well for the use
of purging or sampling Said pump well remain with and in side the well
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casing suspended and secured
Non Dedicated Pump pump that is used for purging and sampling at one
or more wells
Groundwater compliance monitoring is accomplished by using the equipment or the
equivalent listed below
Bailer made of inert materials for purging DTG 7.3 page 7-10
If dedicated pump is installed in the well use the dedicated pump otherwise use
1.8 inch outside diameter air-driven sampling pump or equivalent
150 psi air compressor and ancillary equipment or equivalent
Field parameters shall be measured using YSI-556 with Flow Cell Multi-
Parameter Meter system or equivalent that allows continuous stream of water
from the pump to the meter that enables measurements to be taken on real-time
basis without exposing the water stream to the atmosphere The Field Parameter
Meter measures the following parameters
Water temperature
ii Specific conductivity
iiiTotal Dissolved Solids TDS
iv Standard pH
Redox potential Eh
Field parameters are measured by using flow cell system that enables the
measurements to be taken on real-time basis without exposing the water stream to
the atmosphere
Turbidity measuring instrument capable of determining if turbidity is NTU
0.45 micron high capacity disposable inline filters
Field preservation chemicals as provided by the Analytical Laboratory
Five gallon calibrated sample bucket
Stopwatch
Sealed sterile Polyethylene sample containers as provided by the Analytical
Laboratory
De-ionized water
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One new unused clean disposable single check valve bailer or the equivalent for
each well to be sampled for VOCs and
If any portable non-dedicated pumps are used the following equipment
supplies and solutions or the equivalent necessary for decontamination
procedures
15 gallons of de-ionized water
ii gallons of de-ionized water/nonphosphate detergent such as Liqui-Nox
iii5 gallons of de-ionized water/11N03 solution mixture of approximately
and 1/2 gallons of de-ionized water and gallon of HNO3
ivRubber gloves and
Sterile sample containers from the Mill laboratory
6.2.5 Decontamination Procedure
If portable non-dedicated pump is to be used prior to each sampling event at the
beginning of each day during the sampling event and between each sampling location well
decontaminate the portable non-dedicated sampling pump prior to its use for purging or
sampling using the following procedure
wash the pump probe probe sheath and other pump equipment that may come in
contact with the sampling well inner casing or well water the Sampling
Equipment with nonphosphate detergent
rinse the Sampling Equipment with de-ionized water
rinse the Sampling Equipment with dilute .1N hydrochloric or nitric acid and
rinse the Sampling Equipment with de-ionized water
The probe should then be placed in the decontaminated probe sheath or otherwise protected
from contamination until used for purging or sampling
All water produced during decontamination will be containerized Containerized water will
be disposed of in Tailings Cell
All sampling and purging equipment that has been decontaminated as per the foregoing
procedure shall be covered with plastic sheet to shield such equipment from dust or other
materials that may contaminate the equipment when traveling to and between
purging/sampling locations
6.2.6 Pre -Purging Sampling Activities
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If portable non-dedicated pump is to be used prior to commencing the events
sampling activities check the pumping equipment to ensure that no air is leaking
into the discharge line in order to prevent aeration of the sample
If portable non-dedicated pump is to be used prior to each sampling event and at
the beginning of each day during the sampling event decontaminate the sampling
pump using the procedure set forth in Section 6.2.5
If portable non-dedicated pump is to be used after completion of
decontamination and prior to the beginning of each day of each sampling event
prepare one Equipment Rinsate Sample by following the procedure set forth in
Section 4.3.2 and
Prior to leaving the Mill office place the Trip Blanks into cooler that will
preserve the VOC samples The Trip Blanks will accompany the groundwater
samplers throughout the monitoring event
62.7 Well Purging/Measurement of Field Parameters
Remove the well casing cap and measure and record depth to groundwater by
following the procedures set out in paragraph 6.1.3 above
Determine the casing volume in gallons where is colunm height of the water
in the well calculated by subtracting the depth to groundwater in the well from the
total depth of the well O.653h for casing volume and .367h for
casing volume Record the casing volume on the Field Data Worksheet
If the RSO has advised the field technician that immiscible contaminants i.e
LNAPLs or DNAPLs are known to occur or could potentially occur in the
subsurface at the location of the well follow the additional procedures to be
provided by the RSO prior to well purging
Purging Where Use of Pump is Effective See paragraph 6.2.7 below where
bailer is required
If portable non-dedicated pump is used ensure that it has been decontaminated in
accordance with Section 6.2.5 since its last use in different well lower the pump
into the well making sure to keep the pump at least five feet from the bottom of the
well Be sure never to drop the pump into the well as this will cause degassing of the
water upon impact Once the pump is lowered into the well or if the well has
dedicated pump perform the following steps
Commence pumping
ii Determine pump flow rate by using stopwatch and calibrated bucket by
measuring the number of seconds required to fill to the one-gallon mark
Record this in the pumping rate section of the Field Data Worksheet
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iiiCalculate the amount of time to evacuate two casing volumes
ivEvacuate two casing volumes if possible by pumping for the length of time
determined in paragraph iii
Take measurements of field parameters pH specific conductance
temperature redox potential and turbidity during well purging using the
Field Parameter Meter and turbidity measuring instrument These
measurements will be recorded on the Field Data Worksheet Purging is
completed after two casing volumes have been removed
and the field
parameters pH temperature specific conductance redox potential Eh and
turbidity have stabilized to within 10%over at least two consecutive
measurements The groundwater in the well should recover to within at
least 90%of the measured groundwater static surface before sampling In
addition turbidity measurement in the water should be NTU prior to
sampling DTG Well Development 6.7 page 6-48 unless the well is
characterized by water that has higher turbidity flow-cell needs to be
used for field parameters If the well is purged to dryness or is purged such
that full recovery exceeds two hours the well should be sampled as soon as
sufficient volume of groundwater is available to fill sample containers
DTG Well Purging 7.2.4 page 7-9
vi If the well yields two casing volumes the individual performing the
sampling should immediately proceed to Section 6.2.8
vii If the well cannot yield two casing volumes
Evacuate the well to dryness and record the number of gallons
evacuated on the Field Data Worksheet and
Prior to sampling measure and record depth to groundwater on the
Field Data Worksheet following the procedures set out in paragraph
6.1.3 above
Purging Where Use of Pump is Not Effective
For wells where pump is not effective for purging and/or sampling wells with
shallow water columns i.e where the water colunm is less than five feet above the
bottom of the well casing or the well takes over two days to recover from purging
disposable bailer made of inert materials may be used If bailer is used the
following procedure will be followed
Use the sound level instrument to determine the water column and figure the
amount of water that must be evacuated
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ii Attach disposable bailer to rope and reel
iiiLower the bailer into the well and listen for contact with the solution Once
contact is made allow the bailer to gradually sink in the well being careful
not to allow the bailer to come in contact with the bottom sediment
iv After the bailer is full retrieve the bailer and discharge the water from the
bailer into gallon buckets By doing this one can record the number of
gallons purged
vAfter the bailer is emptied lower the bailer back into the well and gain another
sample as before This process will continue until the two casing volumes
have been collected or until no more water can be retrieved When the
process is finished for the well the bailer will be disposed of and
viTake field measurements referred to in paragraph 6.2.7 above from the
water in the buckets
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6.2.8 Samples to be taken and order of taking samples
For each sampling event unless sampling for specific parameter under the accelerated
monitoring requirements of paragraphs I.G or I.G.2 of the GWDP as specified by the RSO
the following separate samples shall be taken in the following order from each monitoring
well
VOCs sample containers 40 ml each bailer is used
Nutrients ammonia nitrate and nitrite sample container 100 ml bailer is
used
Heavy metals sample container 250 ml filtered
All other non-radiologics fluoride general inorganics TDS total cations and
anions sample container 250 ml filtered and
Gross alpha sample container 1000 ml filtered
The sample collection containers and sample volumes for chloroform sampling are
specified at Item of the Chloroform Investigation Monitoring Quality Assurance
Program Appendix to this document
The number of sample containers and the quantities taken shall be as set out above unless
otherwise dictated by the Analytical Laboratory as specified by the RSO
6.2.9 Field Duplicate Samples
One duplicate set of samples is required for each Batch of samples see Section
4.3.4 for definition of Batch EPA SW-846 Chapter Section 3.4.1 Field
duplicate samples will be analyzed for the contaminants listed in Table of the
GWDP
The duplicate samples should be as near to split samples as reasonably practicable
rather than merely taking second set of samples from the same well after the field
samples have been taken from that well This can be accomplished by alternately
partially filling the field sample containers and duplicate containers until both sets of
containers are full
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6.2.10 VOCs and Nutrient Sampling
When sampling for VOCs and Nutrients the following procedure shall be followed
Obtain specifically identified sample containers for the type of sample to be taken
as provided by the Analytical Laboratory
Add the quantity of specified preservative provided by the Analytical Laboratory to
each sample container
Sample the well using an unused clean disposable single check valve bailer or the
equivalent
Sample water should be transferred to sample containers in controlled manner that
will minimize sample agitation and aeration
In the case of VOC samples be sure that the sample containers are filled as full as
possible with no airspace in the containers
After each sample container is filled rinse the lid of the container with water and
tighten lid onto container and
Discard the bailer
6.2.11 Heavy Metals All Other Non-Radiologics and Gross Alpha Sampling
When sampling for heavy metals all other non-radiologics and for gross alpha the following
procedure shall be followed
Obtain the specifically identified sample container for the type of sample to be
taken as provided by the Analytical Laboratory
Add the quantity of specified preservative provided by the Analytical Laboratory to
each sample container
When using pump to sample wells without shallow water columns i.e where the
water column is more than five feet above the bottom of the well casing or the well
takes less than two days to recover from purging
Place new 0.45 micron filter on the sample tubing
ii Pump the sample through the filtration unit and into the sample container at
the same rate or lesser pumping rate than was used to purge the well
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iiiThe pump should be operated in continuous manner so that it does not
produce samples that are aerated in the return tube or upon discharge
ivRemove pump from the well and
If using portable non-dedicated pump decontaminate pump as per Section
6.2.5 Do not place decontaminated pump on the ground or on other
contaminated surfaces
When using bailer to sample wells with shallow water columns i.e where the
water column is less than five feet above the bottom of the well casing or the well
takes over two days to recover from purging then one of the following two
procedures will be used
Filtering Water Samples at the Well Head
The sample water is collected by use of inch Teflon bailer or the
equivalent that is capable of being attached to hand-operated
pressure pump or the equivalent Only disposable parts of the
pressure pump may come into contact with the sample water
Attach the pump to the disposable bailer and activate the pump in
accordance with manufacturers instructions such that the sample
water in the bailer is forced through clean un-used disposable 0.45
micron filter into clean previously unused sample container in
maimer such that only disposable parts of the pump mechanism come
into contact with the sample water
Sample water should be transferred to sample containers in
controlled manner that will minimize sample agitation and aeration
Rinse lid of sample container with any remaining filtered water after
container is filled with filtered water and tighten lid onto container
Unless dedicated to particular well dispose of the bailer filter and
any parts of the pump mechanism that come into contact with the
sample water and
No rinsate sample is needed because everything that comes into
contact with the sample water is clean and unused prior to sampling
and disposed of after sampling the well
ii Filtering Water Samples at the Mill Laboratory
new clean gallon raw sample container must be used to capture
waters needed to be filtered
The sample water is collected by use of inch Teflon bailer or the
equivalent and then discharged into the gallon container
After all the samples have been collected for the well and placed in the
field sample container which contains blue ice to keep the samples at
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the required temperature the sampler will then proceed directly back
to the Mill laboratory and perform the filtration on the sample
Unless the bailer is dedicated to particular well it will be disposed of
after completion of sampling in the well
Upon arrival at the administration building all other samples from the
well that do not require filtration will be placed in the sample holding
refrigerator in the locked sample storage room
The sampler will then carry the sample that requires filtration in the
cooler to the laboratory and set up the equipment to be used for
filtration of the sample
The equipment needed for this process consists of
2000 ml glass filter flask
250 ml bell and glass frit for micro-filtration 0.45 micron
filter setup
0.45 micron filter paper
The glass filter flask and micro-filtration equipment will go through
cleaning and rinsate process The processing will included the
following
Rinsing of the equipment using DI water
Rinsing the equipment with mixture of DI water and HNO3
Rinsing the equipment with mixture of DI water and Liqui
Nox soap
Rinsing the equipment with DI water
Finally the collection of the final process rinsate solutions are
placed in the sample collection cooler and labeled as filtration
equipment rinsate sample
The flask is attached to the vacuum system in the laboratory using
Tygon Vacuum Tubing or the equivalent
The micro-filtrationsystem is then inserted into the filter flask
0.45 micron filter paper is then placed between the bell and the glass
frit and clamped in place to prevent solution leaking out
The water sample is then slowly added into the bell and the vacuum is
turned on
As the vacuum draws the water through the filter paper additional
solutions are added until the flask is full
When the flask is full the vacuum is turned off and the bell is
unclamped from the fit The Tygon tubing is then removed from the
flask The glass frit is then pulled out of the flask
The filtered solutions are then poured into the various remaining
sample collection bottles Sample water should be transferred to
sample containers in controlled manner that will minimize sample
agitation and aeration
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Rinse lid of sample container with any remaining filtered water after
container is filled with filtered water and tighten lid onto container
If additional filtered water is required to complete the sample
requirements the sample bottles will be placed in the field cooler
along with the raw sample and housed there while the filtration system
is being hooked back up and the procedures set out in paragraphs Ito
above are repeated until sufficient sample water has been filtered to fill
up the required number of sample bottles
After all samples from the well that require filtration have been filtered
in accordance with the foregoing procedure and placed in the proper
sample bottles the remainder of the raw sample is then discharged into
the laboratory sink which runs to tails and
The filtered samples are then transported to the locked sample storage
room and placed in the sample holding refrigerator
The time lapse between the actual sampling times to the completion of the
filtration process is approximately hour Samples are always in the field
sample container except for when the raw sample is pulled from the cooler
and poured in the bell on the filter flask
6.2.12 Procedures to Follow After Sampling
In each case once sample is taken identify and label the sample container with
Sample locationlfacility
Date and time of sample
Any preservation method utilized
Samplers initials
Filtered or unfiltered
Parameters requested to be analyzed
Place each sample in an ice-packed cooler immediately upon taking the sample
and labeling the sample container
Replace the casing cap on the well Lock the well
Before leaving the sampling location thoroughly document the sampling event on
the Field Data Worksheet by recording the items required in paragraph 7.1 and
Upon returning to the office the samples must be stored in refrigerator at at no
more than These samples shall be received by the Analytical Laboratory at
no more than Samples will then be re-packed in the plastic ice-packed
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cooler and transported via these sealed plastic containers by postal contract
services to the Analytical Laboratory
SAMPLE DOCUMENTATION TRACKING AND RECORD KEEPING
7.1 Field Data Worksheets
Documentation of observations and data from sampling provide important information about
the sampling process and provide permanent record for sampling activities All
observations and field sampling data will be recorded in waterproof ink on the Field Data
Worksheets which will be maintained on file at the Mill
The Field Data Worksheets will contain the following information
Name of the site/facility
description of sampling event
location of sample well name
samplers names and signatures
dates and times of well purging and sample collection
type of well purging equipment used pump or bailer
previous well sampled during the sampling event
well depth
depth to groundwater before purging and sampling
results of in-field measurements pH specific conductance water
temperature
redox potential Eh measurements
turbidity measurements
calculated well casing volume
volume of water purged before sampling
volume of water purged when field parameters are measured
type and condition of well pump
description of samples taken
sample handling including filtration and preservation
volume of water collected for analysis
types of sample containers and preservatives
weather conditions and external air temperature
name of certified Analytical Laboratory
The Field Data Worksheets will also contain detailed notes describing any other significant
factors during the sampling event including as applicable condition of the well cap and
lock water appearance color odor clarity presence of debris or solids any variances from
this Procedure and any other relevant feature or condition An example of form of Field
Data Worksheet that incorporates this information is attached as Attachment
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7.2 Chain-Of-Custody and Analytical Request Record
Chain-of-Custody and Analytical Request Record form the COC Form provided by
the Analytical Laboratory will accompany the samples being shipped to the Analytical
Laboratory An example of the Analytical Laboratorys Chain of Custody Form is attached
as Attachment If the Chain of Custody Form changes at any time the Company shall
provide copy of the new or revised Chain of Custody Form to the Executive Secretary and
substitute the new form for the old form in Attachment Standard Chain-of-Custody
protocol is initiated for each sample set COC Form is to be completed for each set of
samples collected in shipping container cooler and is to include the following
samplers name
company name
date and time of collection
sample type e.g water
sample location
number of sample containers in the shipping container
analyses requested
signatures of persons involved in the chain of possession
internal temperatures of the shipping container when opened at the laboratory
remarks section to identify potential hazards or to relay other information to the
Analytical Laboratory
Chain-of-Custody reports will be placed inside re-sealable bag and taped to the inside lid
Custody seals will be placed on the outside of each cooler
The person shipping the samples to the Analytical Laboratory will sign the COC Form
document shipment method and send the original and the second copy of the COC Form
with the samples Upon receipt of the samples the person receiving the samples will sign the
COC Form and return the second copy to the Mills RSO
Copies of the COC Forms and other relevant documentation will be retained at the Mill
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7.3 Record Keeping
The Field Data Worksheets are retained at the Mill
Original Certificates of Analysis from the Analytical Laboratory showing the laboratory
analytical results for the water samples are maintained at the Mill
Once all the data for the quarter all wells sampled during the quarter is completed key data
from the Field Data Worksheets and from the Certificates of Analysis are typed into
computer file Key data entered into the computer file will include well I.D sample date
depth to groundwater average field data and all laboratory analytical data These computer
files are maintained at the Mill
ANALYTICAL PROCEDURES AND QA/QC
Analytical Laboratory QA provides means for establishing consistency in the performance
of analytical procedures and assuring adherence to analytical methods utilized Analytical
Laboratory QC programs include traceability of measurements to independent reference
materials and internal controls
8.1 Analytical Quality Control
Analytical QA/QC will be governed by the QA/QC program of the Analytical Laboratory In
choosing and retaining the Analytical Laboratory DUSA shall ensure that the Analytical
Laboratory is certified by the State of Utah and by NELAP and/or NAVLAP is capable of
performing the analytical procedures specified in Section 8.2 and that the QA/QC program
of the Analytical Laboratory includes the spikes blanks and duplicates described in Section
8.1.2
1.2 Spikes Blanks and Duplicates
Analytical Laboratory QC samples will assess the accuracy and precision of the analyses
The following describes the type of QC samples that will be used by the Analytical
Laboratory to assess the quality of the data The following procedures shall be performed at
least once with each Batch of samples
Duplicate Spike Matrix Spike
split/spiked field sample shall be analyzed with every analytical batch Analytes
stipulated by the analytical method by applicable regulations or by other specific
requirements must be spiked into the sample Selection of the sample to be spiked
and/or split depends on the information required and the variety of conditions within
typical matrix The duplicate spike matrix spike sample serves as check
evaluating the effect of the sample matrix on the accuracy of analysis
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Blanks
Each batch shall be accompanied by reagent blank The reagent blank shall be
carried through the entire analytical procedure Contamination detected in analysis of
reagent blanks will be used to evaluate any Analytical Laboratory contamination of
environmental samples which may have occurred
Field Samples/Surrogate Compounds
Every blank standard and environmental sample including matrix spike/matrix
duplicate samples shall be spiked with surrogate compounds prior to purging or
extraction Surrogates are organic compounds which are similar to analytes of
interest in chemical composition extraction and chromatography but which are not
normally found in environmental samples Surrogates shall be spiked into samples
according to the appropriate organic analytical methods
Check Sample
Each analytical batch shall contain number of check samples For each method the
Analytical Laboratory will normally analyze the following check samples or their
equivalents method blank laboratory control spike matrix spike and matrix
spike duplicate or the equivalent with relative percent difference reported
8.2 Analytical Laboratory Procedures
The analytical procedures to be used by the Analytical Laboratory will be as specified
in Table or as otherwise authorized by the Executive Secretary With respect to
Chloroform Investigation sampling the analytical procedures for parameters
monitored under that program are specified at Item of the Chloroform Investigation
Monitoring Quality Assurance Program Appendix to this document
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Table
Contaminant Analytical
Methods
to be Used
Reporting
Limit1
Maximum
Holding
Times
Sample
Preservation
Requirements
Sample
Temperature
Requirements
Nutrients
Ammonia as A4500-
NH3
0.05 mg/L 28 days H2S04 to
pH2
4C
Nitrate Nitrite
as
E353.2 0.1 mg/L 28 days H2S04 to
pH2
4C
Heavy Metals
Arsenic E200.8 jig/L months HNO3 to pHc2 None
Beryllium E200.8 0.50 tgfL months HNO3 to p112 None
Cadmium E200.8 0.50 g/L months HNO3 to pH2 None
Chromium E200.8 25 pg/L months 11N03 to p112 None
Cobalt E200.8 10 j.ig/L months HNO3 to p112 None
Copper E200.8 10 g/L months HNO3 to pH2 None
Iron E200.7 30 jigIL months 11N03 to pH2 None
Lead E200.8 1.0 pg/L months 11N03 to pH2 None
Manganese E200.8 10 jiglL months HNO3 to pH2 None
Mercury E200.8 0.50 jtgfL 28 days HNO3 to p112 None
Molybdenum E200.8 10 jig/L months FINO3 to p112 None
Nickel E200.8 20 pg/L months 11N03 to pH2 None
Selenium E200.8 ig/L months 11N03 to p112 None
Silver E200.8 10 g/L months HNO3 to pH2 None
Thallium E200.8 0.50 igIL months HNO3 to pH2 None
Tin E200.8 100 pg/L months 11N03 to pH2 None
Uranium E200.8 0.30 pgIL months HNO3 to pH2 None
Vanadium E200.8 15 pg/L months 11N03 to p112 None
Zinc E200.8 10 jig/L months 11N03 to pH2 None
Radiologics
Gross Alpha E900.1 1.0 pCifL months HNO3 to pH2 None
Volatile
Organic
Compounds
Acetone 5W8260B 20 pg/L 14 days HC1 to pH2 4C
Benzene 5W8260B 1.0 pgIL 14 days 11Cl to pH2 4C
2-Butanone
MEK
5W8260B 20 pg/L 14 days HCl to pH2 4C
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Others
Field pH S.U
Fluoride
TDS
A45 00-H
A4500-F
A2540
0.01 s.u Immediate None None
Contaminant Analytical
Methods
to be Used
Reporting
Limit1
Maximum
Holding
Times
Sample
Preservation
Requirements
Sample
Temperature
Requirements
Carbon
Tetrachioride
SW8260B 1.0 g/L 14 days HC1 to pH2 4C
Chloroform SW8260B 1.0 jig/L 14 days HC1 to pHc2 4C
Chioromethane SW8260B 1.0 pg/L 14 days HC1 to pFR2 4C
Dichioromethane
Methylene
Chloride
SW8260B 1.0 pgfL 14 days HC1 to pH2 4C
Naphthalene SW8260B 1.0 g/L 14 days HC1 to pH2 4C
Tetrahydrofuran SW8260B 1.0 pg/L 14 days HC1 to pH2 4C
Toluene SW8260B 1.0 pgIL 14 days HC1 to pHc2 4C
Xylenes total SW8260B 1.0 ig/L 14 days HC1 to pHc2 4C
General
Inorganics
Chloride A4500-Cl mgIL 28 days None None
Sulfate A4500-
504E
mgIL 28 days None 4C
Carbonate as
C03
A2320 mg/L 14 days None 4C
Bicarbonate as
HCO3
A2320 mgIL 14 days None 4C
Sodium E200.7 0.5 mg/L months 11N03 to pHc2 None
Potassium E200.7 0.5 mgfL months HNO3 to pHc2 None
Magnesium E200.7 0.5 mg/L months HNO3 to pH2 None
Calcium E200.7 0.5 mg/L months HNO3 to pH2 None
The Analytical Laboratory will be required to meet the reporting limits RLs in the foregoing Table
unless the RI must be increased due to sample matrix interference Le-due to dilution gain in which case the
increased EL will be used or unless otherwise approved by the Executive Secretary
0.1 mg/L
lOmg/L
28 days
days
None
None
None
4C
INTERNAL QUALITY CONTROL CHECKS
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Internal quality control checks are inherent in this Plan The QA Manager will monitor the
performance of the Sample and QC Monitors and to the extent practicable the Analysis
Monitor to ensure that they are following this Plan In addition either the QA Manager or
Sampling and QC Monitor will review and validate the analytical data generated by the
Analytical Laboratory to ensure that it meets the DQOs established by this Plant Finally
periodic system and performance audits will be performed as detailed in Section 12 below
9.1 Field QC Cheek Procedures
The QA Manager will perform the following QAJQC analysis of field procedures
9.1.1 Review of Compliance With the Procedures Contained in this Plan
Observation of technician performance is monitored by the QA Manager on periodic basis
to ensure compliance with this Plan
9.1.2 Analyte Completeness Review
The QA Manager will review all Analytical Results to confirm that the analytical results are
complete i.e there is an analytical result for each required constituent in each well The
QA Manager shall also identify and report all instances of non-compliance and non
conformance see Part I.E .a of the Permit Executive Secretary approval will be required
for any completeness prior to QA/QC analysis less than 100 percent Non-conformance
will be defined as failure to provide field parameter results and analytical results for each
parameter and for each well required in Sections 6.2.2 and 6.2.3 for the sampling event
without prior written Executive Secretary approval
9.1.3 Blank Comparisons
Trip blanks and equipment rinsate samples will be compared with original sample results
Non-conformance conditions will exist when contaminant levels in the blanks/sampless
are within an order of magnitude of the original sample result TEGD Field QA/QC
Program page 119
9.1.4 Duplicate Sample Comparisons
The following analyses will be performed on duplicate field samples
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Relative Percent Difference
RPDs will be calculated in comparisons of duplicate and original field sample results
Non-conformance will exist when the RPD 20%unless the measured activities are less
than times the required detection limit Standard Methods 1998 EPA Contract
Laboratory Program National Functional Guidelines for Inorganic Data Review February
1994 9240.1-05-0 25
Radiologics Counting Error Term
All gross alpha analyses shall be reported with an error term All gross alpha analysis
reported with an activity equal to or greater than the GWCL shall have counting
variance that is equal to or less that 20%of trhe reported activity concentration An error
term may be greater than 20%of the reported activity concentration when the sum of the
activity concentration and error term is less than or equal to the GWCL
Radiologics Duplicate Samples
Comparability of results between the original and duplicate radiologic samples will be
evaluated by determining compliance with the following formula
A-B /sa2sb22
Where
the first duplicate measurement
the second duplicate measurement
sa2 the uncertainty of the first measurement squared
sb2 the uncertainty of the second measurement squared
Non-conformance exists when the foregoing equation
is
EPA Manual for the Certification of Laboratories Analyzing Drinking Water Criteria and
Procedures Quality Assurance January 2005 EPA 815-R-05-004 VI-9
If the QA Managers review finds any situations of non-conformance see Section 10
9.2 Analytical Laboratory QA Reviews
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Full validation will include recalculation of raw data for minimum of one or more analytes
for ten percent of the samples analyzed The remaining 90%of all data will undergo QC
review which will include validating holding times and QC samples Overall data
assessment will be part of the validation process as well
The Analysis Monitor or data validation specialist will evaluate the quality of the data based
on SW-846 the applicable portions of NRC guide 4.14 and on analytical methods used The
reviewer will check the following sample preparation information is correct and
complete analysis information is correct and complete appropriate Analytical
Laboratory procedures are followed analytical results are correct and complete QC
samples are within established control limits blanks are within QC limits special
sample preparation and analytical requirements have been met and documentation is
complete
The Analytical Laboratory will prepare and retain full QC and analytical documentation
The Analytical Laboratory will report the data as group of one batch or less along with the
QA/QC data The Analytical Laboratory will provide the following information cover
sheet listing samples included in report with narrative results of compounds identified
and quantified and reporting limits for all analytes Also to be included are the QA/QC
analytical results
9.3 QA Manager Review of Analytical Laboratory Results and Procedures
The QA Manager shall perform the following QA reviews relating to Analytical Laboratory
procedures
Reporting Limit RL Comparisons
The QA Manager shall confirm that all reporting limits used by the Analytical Laboratory are
in conformance with the reporting limits set out on Table Non-conformance shall be
defined as reporting limit that violates these provisions unless the reporting limit must
be increased due to sample matrix interference i.e due to dilution gain or reporting
limit that exceeds the respective GWQS listed in Table of the GWDP
Laboratory Methods Review
The QA Manager shall confirm that the analytical methods used by the Analytical
Laboratory are those specified in Table unless otherwise approved by the Executive
Secretary Non-conformance shall be defined when the Analytical Laboratory uses analytical
methods not listed in Table and not otherwise approved by the Executive Secretary
Holding Time Examination
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The QA Manager will review the analytical reports to verify that the holding time for each
contaminant was not exceeded Non-conformance shall be defined when the holding time is
exceeded
Sample Temperature Examination
The QA Manager shall review the analytical reports to verify that the samples were received
by the Analytical Laboratory at temperature no greater than the approved temperature listed
in Table Non-conformance shall be defined when the sample temperature is exceeded
9.4 Analytical Data
All QA/QC data and records required by the Analytical Laboratorys QA/QC program shall
be retained by the Analytical Laboratory and shall be made available to DUSA as requested
Analytical data submitted by the Analytical Laboratory should contain the date/time the
sample was collected the date/time the sample was received by the Analytical Laboratory
the date/time the sample was extracted if applicable and the date/time the sample was
analyzed
All out-of-compliance results will be logged by the Analysis Monitor with corrective actions
described as well as the results of the corrective actions taken All raw and reduced data will
be stored according to the Analytical Laboratorys record keeping procedures and QA
program All Analytical Laboratory procedures and records will be available for on-site
inspection at any time during the course of investigation
If re-runs occur with increasing frequency the Analysis Monitor and the Mills QA Manager
will be consulted to establish more appropriate analytical approaches for problem samples
10 CORRECTIVE ACTION
10.1 When Corrective Action is Required
The Sampling and QC Monitors and Analytical Laboratory are responsible for following
procedures in accordance with this Plan Corrective action should be taken for any procedure
deficiencies or deviations noted in this Plan All deviations from field sampling procedures
will be noted on the Field Data Worksheets or other applicable records Any QA/QC
problems that arise will be brought to the immediate attention of the QA Manager
Analytical Laboratory deviations will be recorded by the Analysis Monitor in logbook as
well
When non-conformance is identified DUSA shall
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When non-conformance occurs as specified in Sections 9.1.3 9.1.4 or 9.3 the data
shall be qualified to denote the problem In addition DUSA shall determine the root
cause and provide specific steps to resolve problemss in accordance with the
procedure set forth in Section 10.2 Any non-conformance with QAP requirements
in given quarterly ground water monitoring period will be corrected and reported to
the Executive Secretary on or before submittal of the next quarterly ground water
monitoring report
When sample is lost sample container broken or the sample or analyte was
omitted resample within 10 days of discovery and analyze again in compliance with
all requirements of this Plan The results for this samples should be included in the
same quarterly monitoring report with other samples collected for the same sampling
event and
For any other material deviation from this Plan the procedure set forth in Section
10.2 shall be followed
10.2 Procedure for Corrective Action
The need for corrective action for non-conformance with the requirements of this Plan may
be identified by system or performance audits or by standard QA/QC procedures The
procedures to be followed if the need for corrective action is identified are as follows
Identification and definition of the problem
Assignment of responsibility for investigating the problem
Investigation and determination of the cause of the problem
Determination of corrective action to eliminate the problem
Assigning and accepting responsibility for implementing the corrective action
Implementing the corrective action and evaluating its effectiveness and
Verifying that the corrective action has eliminated the problem
The QA Manager shall ensure that these steps are taken and that the problem which led to the
corrective action has been resolved memorandum explaining the steps outlined above will
be placed in the applicable monitoring files and the Mill Central Files and the corrective
action will be documented in Report prepared in accordance with Section 11
11 REPORTING
As required under paragraph I.F of the GWDP the Mill will send groundwater
monitoring report to the Executive Secretary on quarterly basis Both the Routine
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Groundwater Monitoring
Quality Assurance Plan QAP Page 37 of 43
Groundwater Monitoring Reports pertinent to Part I.F of the Permit and Chloroform
Investigation Reports shall be submitted according to the following schedule
Quarter Period Due Date
First January March June
Second April June September
Third July September December
Fourth October December March
The Routine Groundwater Monitoring Reports pertinent to Part I.F of the Permit will
include the following information
Description of monitor wells sampled
Description of sampling methodology equipment an decontamination
procedures to the extent they differ from those described in this Plan
summary data table of historic groundwater levels for each monitor well
and piezometer
summary data table showing the results of the sampling event listing all
wells and the analytical results for all constituents and identifying any
constituents that are subject to accelerated monitoring in any particular wells
pursuant to Part I.G of the GWDP or are out of compliance in any particular
wells pursuant to Part I.G.2 of the GWDP
Copies of Field Data Worksheets
Copies of Analytical Laboratory results
Copies of Chain of Custody Forms
Water Table Contour Map showing groundwater elevation data for the
quarter will be contemporaneous for all wells on site not to exceed
maximum time difference of five calendar days
Evaluation of groundwater levels gradients and flow directions
Quality assurance evaluation and data validation description see Section for
further details
All non-conformance with this Plan and all corrective actions taken
Recommendations and Conclusions
With respect to the chloroform investigation reporting requirements these are specified at
Item of the Chloroform Investigation Monitoring Quality Assurance Program Appendix
to this document
In addition an electronic copy of all analytical results will be transmitted to the Executive
Secretary in comma separated values CSV format or as otherwise advised by the Executive
Secretary
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Groundwater Monitoring
Quality Assurance Plan QAP Page 38 of 43
Further reporting may be required as result of accelerated monitoring under paragraphs
I.G and LG.2 of the GWDP The frequency and content of these reports will he defined by
DUSA corporate management working with the Executive Secretary
12 SYSTEM AND PERFORMANCE AUDITS
12.1 QA Manager to Perform System Audits and Performance Audits
DUSA shall perform such system audits and performance audits as it considers necessary in
order to ensure that data of known and defensible quality are produced during sampling
program The frequency and timing of system and performance audits shall be as determined
by DUSA
12.2 System Audits
System audits are qualitative evaluations of all components of field and Analytical
Laboratory QC measurement systems They determine if the measurement systems are being
used appropriately System audits will review field and Analytical Laboratory operations
including sampling equipment laboratory equipment sampling procedures and equipment
calibrations to evaluate the effectiveness of the QA program and to identify any weakness
that may exist The audits may be carried out before all systems are operational during the
program or after the completion of the program Such audits typically involve comparison
of the activities required under this Plan with those actually scheduled or performed
special type of systems audit is the data management audit This audit addresses only data
collection and management activities
12.3 Performance Audits
The performance audit is quantitative evaluation of the measurement systems of program
It requires testing the measurement systems with samples of known composition or behavior
to evaluate precision and accuracy With respect to performance audits of the analytical
process either blind performance evaluation samples will be submitted to the Analytical
Laboratory for analysis or the auditor will request that it provide results of the blind studies
that the Analytical Laboratory must provide to its NELAP and/or NAVLAP accreditation
agency on an annual basis The performance audit is carried out without the knowledge of
the analysts to the extent practicable
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Ground water Monitoring
Quality Assurance Plan QAP Page 39 of 43
12.4 Follow-Up Actions
Response to the system audits and performance audits is required when deviations are found
and corrective action is required Where corrective action is required the steps set out in
Section 10.2 will be followed
12.5 Audit Records
Audit records for all audits conducted will be retained in Mill Central Files These records
will contain audit reports written records of completion for corrective actions and any other
documents associated with the audits supporting audit findings or corrective actions
13 PREVENTIVE MAINTENANCE
Preventive maintenance concerns the proper maintenance and care of field and laboratory
instruments Preventive maintenance helps ensure that monitoring data generated will be of
sufficient quality to meet QA objectives Both field and laboratory instruments have set
maintenance schedule to ensure proper functioning of the instruments
Field instruments will be maintained as per the manufacturers specifications and established
sampling practice Field instruments will be checked and calibrated prior to use in
accordance with Section Batteries will be charged and checked daily when these
instruments are in use All equipment out of service will be immediately replaced Field
instruments will be protected from adverse weather conditions during sampling activities
Instruments will be stored properly at the end of each working day Calibration and
maintenance problems encountered will be recorded in the Field Data Worksheets or
logbook
The Analytical Laboratory is responsible for the maintenance and calibration of its
instruments in accordance with Analytical Laboratory procedures and as required in order to
maintain its NELAP and/or NAVLAP certifications Preventive maintenance will be
performed on scheduled basis to minimize downtime and the potential interruption of
analytical work
14 QUALITY ASSURANCE REPORTS TO MANAGEMENT
14.1 Ongoing QA/QC Reporting
The following reporting activities shall be undertaken on regular basis
The Sample and QC Monitors shall report to the QA Manager regularly regarding
progress of the applicable sampling program The Sample and QC Monitors will
also brief the QA Manager on any QA/QC issues associated with such sampling
activities
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Groundwater Monitoring
Quality Assurance Plan QAP Page 40 of 43
The Analytical Laboratory shall maintain detailed procedures for laboratory record
keeping Each data set report submitted to the Mills QA Manager or his staff will
identify the analytical methods performed and all QA/QC measures not within the
established control limits Any QA/QC problems will be brought to the QA
Managers attention as soon as possible and
After sampling has been completed and final analyses are completed and reviewed
brief data evaluation summary report will be prepared by the Analytical Laboratory
for review by the QA Manager by Sampling and QC Monitor or by such other
qualified person as may be designated by the QA Manager The report will be
prepared in accordance with NELAP and/or NAVLAP requirements and will
summarize the data validation efforts and provide an evaluation of the data quality
14.2 Periodic Reporting to Management
The QA Manager shall present report to DUSAs ALARA Committee at least once per
calendar year on the performance of the measurement system and the data quality These
reports shall include
Periodic assessment of measurement quality indicators i.e data accuracy precision
and completeness
Results of any performance audits including any corrective actions
Results of any system audits including any corrective actions and
Significant QA problems and recommended solutions
15 AMENDMENT
This Plan may be amended from time to time by DUSA only with the approval of the
Executive Secretary
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Groundwater Monitoring
Quality Assurance Plan QAP Page 41 of 43
16 REFERENCES
16.1 United States Environmental Protection Agency November 2004 Test Methods for
Evaluating Solid Waste EPA SW-846
16.2 United States Environmental Protection Agency September 1986 RCRA Ground
Water Monitoring Technical Enforcement Guidance Document TEGD Office of Solid
Waste and Emergency Response OSWER-9950.1
16.3 United States Environmental Protection Agency November 1992 RCRA Ground
water Monitoring Draft Technical Guidance DTG Office of Solid Waste
16.4 Standard Methods for the Examination of Water and Wastewater 20th Edition 1998
American Public Health Association American Water Works Association Water
Environment Federation Washington D.C 1-7
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Groundwater Monitoring
Quality Assurance Plan QAP Page 42 of 43
ATTACHMENT
WHITE MESA URANIUM MILL
FIELD DATA WORKSHEET FOR GROUND WATER
Description of Sampling Event______________________________________________________
Sampler
Location well name_______________________Name and initials__________________________
Date and Time for Purging _______________and Sampling if different_____________________
Well Purging Equip Used pump or _bailer Well Pump if other than Bennet___________
Sampling Event________________________Prey Well Sampled in Sampling Event_______
pH Buffer 7.0 pH Buffer 4.0
Specific Conductance _________uMHOS/cm Well Depth
Depth to Water Before Purging Casing Volume Well .653h
Well .367h
Conductance avg pH of Water avg________________________
Well Water Temp avg Redox Potential Eh Turbidity
Weather Cond.___________________Ext Amb Temp.prior to sampling event__________
Time__________Gal Purged___________Time__________Gal Purged
Conductance_________________________Conductance____________________________
pH pH__________________________________
Temperature Temperature
Redox Potential Eh__________________Redox Potential Eh_____________________
Turbidity___________________________Turbidity______________________________
Time__________Gal Purged___________Time___________Gal Purged
Conductance_________________________Conductance____________________________
pH_______________________________pH__________________________________
Temperature Temperature
Redox Potential Eh___________________Redox Potential Eh______________________
Turbidity___________________________Turbidity______________________________
Mill Groundwater Discharge Permit Date6-18-08 Revision-3
Groundwater Monitoring
Quality Assurance Plan QAP Page 43 of 43
Volume of Water Purged When Field Parameters are Measured____________________________
Pumping Rate Calculation
Flow Rate in gpm Time to evacuate two casing volumes 2V
5/60 _________________T2V/Q _____________________
Number of casing volumes evacuated if other than two___________________________________
If well evacuated to dryness number of gallons evacuated________________________________
Name of Certified Analytical Laboratory if Other Than Energy Labs_________________________
Type of Sample Sample
Taken
circle
Sample Volume
indicate if other
than as specified
below
Filtered
circle
Preservative Added
circle
VOCs 3x40m1 HCL
Nutrients 100 ml H2S04
Heavy Metals 250 ml HNO3
All Other Non-
Radiologics
250 ml No Preservative Added
Gross Alpha 1000 ml H2S04
Other specify Sample volume
If preservative is used
Specify Type and Quantity
of Preservative
Comments
09/08 Revision Denison 1.3
Cell 4A BAT Monitoring Operations and Maintenance Plan
Introduction
Construction of Cell 4A was authorized by the Utah Department of Environmental
Quality Division of Radiation Control DRC on June 25 2007 The construction
authorization provided that Cell 4A shall not be in operation until after BAT
Monitoring Operations and Maintenance Plan is submitted for Executive Secretary
review and approval The Plan shall include requirements in Part F.3 of the Groundwater
Discharge Permit No UGW370004 GWDP and full fill the requirements of Parts
I.D.6 I.E.8 and I.F.8 of the GWDP
Cell Desi2n
Tailings Cell 4A consists of the following major elements
Dikes consisting of earthen embankments of compacted soil constructed
between 1989-1990 and composed of four dikes each including 15-foot
wide road at the top minimum On the north east and south margins these
dikes have slopes of 3H to lv The west dike has interior slope of 2H to
lv Width of these dikes varies each has minimum crest width of at least
15 feet to support an access road Base width also varies from 89-feet on the
east dike with no exterior embankment to 211-feet at the west dike
Foundation including subgrade soils over bedrock materials Foundation
preparation included excavation and removal of contaminated soils
compaction of imported soils to maximum dry density of 90%Floor of
Cell 4A has an average slope of 1%that grades from the northeast to the
southwest corners
Tailings Capacity the floor and inside slopes of Cell 4A encompass about 40
acres and have maximum capacity of about 1.6 million cubic yards of
tailings material storage as measured below the required 3-foot freeboard
Liner and Leak Detection Systems including the following layers in
descending order
Primary Flexible Membrane Liner FML consisting of impermeable 60
mil high density polyethylene HDPE membrane that extends across both
the entire cell floor and the inside side-slopes and is anchored in trench
at the top of the dikes on all four sides The primary FML will be in direct
physical contact with the tailings material over most of the Cell 4A floor
area In other locations the primary FML will be in contact with the
slimes drain collection system discussed below
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
Leak Detection System includes permeable HDPE geonet fabric that
extends across the entire area under the primary FML in Cell 4A and
drains to leak detection sump in the southwest corner Access to the leak
detection sump is via an 18-inch inside diameter ID PVC pipe placed
down the inside slope located between the primary and secondary FML
liners At its base this pipe will be surrounded with gravel filter set in
the leak detection sump having dimensions of 10 feet by 10 feet by feet
deep In turn the gravel filter layer will be enclosed in an envelope of
geotextile fabric The purpose of both the gravel and geotextile fabric is to
serve as filter
Secondary FML consisting of an impermeable 60-mil HDPE membrane
found immediately below the leak detection geonet Said FML also
extends across the entire Cell 4A floor up the inside side-slopes and is
also anchored in trench at the top of all four dikes
Geosynthetic Clay Liner consisting of manufactured geosynthetic clay
liner GCL composed of 0.2-inch of low permeability bentonite clay
centered and stitched between two layers of geotextile Prior to disposal
of any wastewater in Cell 4A the Permittee shall demonstrate that the
GCL has achieved moisture content of at least 50%by weight This
item is revised requirement per
DRC letter to DUSA dated September
28 2007
Slimes Drain Collection System including two-part system of strip drains
and perforated collection pipes both installed immediately above the primary
FML as follows
Horizontal Strip Drain System is installed in herringbone pattern
across the floor of Cell 4A that drain to backbone of perforated
collection pipes These strip drains are made of prefabricated two-part
geo-composite drain material solid polymer drainage strip core
surrounded by an envelope of non-woven geotextile filter fabric The strip
drains are placed immediately over the primary FML on 50-foot centers
where they conduct fluids downgradient in southwesterly direction to
physical and hydraulic connection to the perforated slimes drain collection
pipe series of continuous sand bags filled with filter sand cover the
strip drains The sand bags are composed of woven polyester fabric
filled with well graded filter sand to protect the drainage system from
plugging
Horizontal Slimes Drain Collection Pipe System includes backbone
piping system of 4-inch ID Schedule 40 perforated PVC slimes drain
collection SDC pipe found at the downgradient end of the strip drain
lines This pipe is in turn overlain by berm of gravel that runs the entire
diagonal length of the cell surrounded by geotextile fabric cushion in
immediate contact with the primary FML In turn the gravel is overlain
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
by layer of non-woven geotextile to serve as an additional filter material
This perforated collection pipe serves as the backbone to the slimes
drain system and runs from the far northeast corner downhill to the far
southwest corner of Cell 4A where it joins the slimes drain access pipe
Slimes Drain Access Pipe consisting of an 18-inch ID Schedule 40 PVC
pipe placed down the inside slope of Cell 4A at the southwest corner
above the primary FML Said pipe then merges with another horizontal
pipe of equivalent diameter and material where it is enveloped by gravel
and woven geotextile that serves as cushion to protect the primary FML
reducer connects the horizontal 18-inch pipe with the 4-inch SDC pipe
At some fliture time pump will be set in this 18-inch pipe and used to
remove tailings wastewaters for purposes of de-watering the tailings cell
Dike Splash Pads minimum of eight 10-foot wide splash pads are
installed on the interior dike slopes to protect the primary FML from abrasion
and scouring by tailings sluny These pads will consist of an extra layer of 60
mil HDPE membrane that will be placed down the inside slope of Cell 4A
from the top of the dike and down the inside slope The pads on the north side
of the Cell will extend to point 5-feet beyond the toe of the slope to protect
the liner bottom during initial startup of the Cell The exact location of the
splash pads is detailed on the As-Built Plans and Specifications
Emergency Spillway concrete lined spillway constructed near the western
corner of the north dike to allow emergency runoff from Cell into Cell 4A
This spillway will be limited to 6-inch reinforced concrete slab set directly
over the primary FML in 4-foot deep trapezoidal channel No other spillway
or overflow strncture will be constructed at Cell 4A All stormwater runoff
and tailings wastewaters not retained in Cells and will be managed and
contained in Cell 4A including the Probable Maximum Precipitation and
flood event
Cell Operation
Solution Discharge
Cell 4A will initially be used for storage and evaporation of process solutions
from the Mill operations These process solutions will be from the
uraniumlvanadium solvent extraction circuit or transferred from Cell
evaporation pond or the free water surface from Cell The solution will be
pumped to Cell 4A through inch or inch diameter HDPE pipelines The initial
solution discharge will be in the southwest corner of the Cell The discharge pipe
will be routed down the Splash Pad provided in the corner of the Cell to protect
the pipeline running from the solution reclaim barge The solution will be
discharged in the bottom of the Cell away from any sand bags or other
installation on the top of the FML Building the solution pool from the low end of
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
the Cell will allow the solution pool to gradually rise around the slimes drain
strips eliminating any damage to the strip drains or the sand bag cover due to
solution flowing past the drainage strips The solution will eventually be
discharged along the dike between Cell and Cell 4A utilizing the Splash Pads
described above The subsequent discharge of process solutions will be near the
floor of the pond through discharge header designed to discharge through
multiple points thereby reducing the potential to damage the Splash Pads or the
Slimes Drain system At no time will the solution be discharged into less than
feet of solution As the cell begin to fill with solution the discharge point will be
pull back up the Splash Pad and allowed to continue discharging at or near the
solution level
Initial Solids Discharge
Once Cell 4A is needed for storage for tailings solids the slurry discharge from
No CCD thickener will be pumped to the cell through inch or inch diameter
HDPE pipelines The pipelines will be routed along the dike between Cell and
Cell 4A with discharge valves and drop pipes extending down the Splash Pads to
the solution level One or all of the discharge points can be used depending on
operational considerations Solids will settle into cone or mound of material
under the solution level with the courser fraction sealing out closer to the
discharge point The initial discharge locations are shown on Figure Figure
illustrates the general location of the solution and slurry discharge pipelines and
control valve locations The valves are or stainless steel knife-gate valves
The initial discharge of slurry will be at or near the toe of the Cell slope and then
gradually moved up the slope continuing to discharge at or near the water
surface This is illustrated in Section A-A on Figure Because of the depth of
Cell 4A each of the discharge points will be utilized for an extended period of
time before the cone of material is above the maximum level of the solution The
discharge location will then moved further to the interior of the cell allowing for
additional volume of solids to be placed under the solution level The solution
level in the cell will vary depending on the operating schedule of the Mill and the
seasonal evaporation rates The tailings slurry will not be allowed to discharge
directly on to the Splash Pads in order to further protect the FML The tailings
slurry will discharge directly in to the solution contained in the Cell onto an
additional protective sheet or on to previously deposited tailings sand
Equipment Access
Access will be restricted to the interior portion of the cell due to the potential to
damage the flexible membrane liner Only rubber tired all terrain vehicles or foot
traffic will be allowed on the flexible membrane liner Personnel are also
cautioned on the potential damage to the flexible membrane liner through the use
and handling of hand tools and maintenance materials
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
Reclaim Water System
pump barge and solution recovery system will be installed in the southwest
corner of the cell to pump solution from the cell for water balance purposes or for
re-use in the Mill process Figure illustrates the routing of the solution return
pipeline and the location of the pump barge The pump barge will be constructed
and maintained to ensure that the flexible membrane liner is not damaged during
the initial filling of the cell or subsequent operation and maintenance activities
The condition of the pump barge and access walkway will be noted during the
weekly Cell inspections
Interim Solids Discharge
Figure illustrates the progression of the slurry discharge points around the east
side of Cell 4A Once the tailings solids have been deposited along the north and
east sides of the Cell the discharges points will subsequently be moved to the
sand beaches which will eliminate any potential for damage to the liner system
Liner Maintenance and QAQC
Any construction defects or operational damage discovered during observation of
the flexible membrane liner will be repaired tested and documented according to
the procedures detailed in the approved Revised construction Quality
Assurance Plan for the Construction of the Cell 4A Lining System May
2007 by GeoSyntec Consultants
BAT Performance Standards for Tailings Cell 4A
DUSA will operate and maintain Tailings Cell 4A so as to prevent release of wastewater
to groundwater and the environment in accordance with this BAT Monitoring Operations
and Maintenance Plan pursuant to Part I.H 19 of the GWDP These performance
standards shall include
Leak Detection System Pumping and Monitoring Equipment the
leak detection system pumping and monitoring equipment includes
submersible pump pump controller water level indicator head
monitoring and flow meter with volume totalizer The pump controller
is set to maintain the maximum level in the leak detection system at no
more than foot above the lowest level of the secondary flexible
menbrane second leak detection pump with pressure transducer flow
meter and manufacturer recommended spare parts for the pump controller
and water level data collector is maintained in the Mill warehouse to
ensure that the pump and controller can be replaced and operational within
24 hours of detection of failure of the pumping system The root cause
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
of the equipment failure will be documented in report to Mill
management with recommendations for prevention of re-occurrence
Maximum Allowable Head the Permittee shall measure the fluid head
above the lowest point on the secondary flexible membrane by the use of
procedures and equipment specified in the White Mesa Mill Tailings
Management System and Discharge Minimization Technology
DMT monitoring Plan 3/07 Revision Denison-3 or the currently
approved DMT Plan Under no circumstance shall fluid head in the leak
detection system sump exceed 1-foot level above the lowest point in
the lower flexible membrane liner
Maximum Allowable Daily LDS Flow Rates the Permittee shall
measure the volume of all fluids pumped from the LDS on weekly
basis and use that information to calculate an average volume pumped
per day Under no circumstances shall the daily LDS flow volume
exceed 24160 gallons/day The maximum daily LDS flow volume will
be compared against the measured cell solution levels detailed on the
attached Table to determine the maximum daily allowable LDS flow
volume for varying head conditions in the cell.
3-foot Minimum Vertical Freeboard Criteria the Permittee shall
operate and maintain wastewater levels to provide 3-foot Minimum of
vertical freeboard in Tailings Cell 4A Said measurements shall be
made to the nearest 0.1 foot
Slimes Drain Recovery Head Monitoring immediately after the
Permittee initiates pumping conditions in the Tailings Cell 4A slimes
drain system monthly recovery head tests and fluid level measurements
will be made in accordance with plan approved by the DRC Executive
Secretary The slimes drain system will pumping and monitoring
equipment includes submersible pump pump controller water level
indicator head monitoring and flow meter with volume totalizer
Routine Maintenance and Monitoring
Trained personnel inspect the White Mesa tailings system on once per day basis Any
abnormal occurrences or changes in the system will be immediately reported to Mill
management and maintenance personnel The inspectors are trained to look for events
involving the routine placement of tailings material as well as events that could affect the
integrity of the tailings cell dikes or lining systems The daily inspection reports are
summarized on monthly basis and reviewed and signed by the Mill Manager
Solution Elevation
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
Measurements in Cell 4A are to be taken by survey on weekly basis as follows
The survey will be performed by the Mills Radiation Safety Officer or
designee the Surveyor with the assistance of another Mill worker the
Assistant
ii The survey will be performed using survey instrument the Survey
Instrument accurate to 0.01 feet such as Sokkai No B2 or
equivalent together with survey rod the Survey Rod having visible
scale in 0.01 foot increments
iiiThe reference Points the Reference Points for Cells 4A are known
points established by Registered Land Surveyor For Cell 4A the
Reference Point is piece of metal rebar located on the dike between Cell
and Cell 4A The elevation at the top of this piece of rebar the
Reference Point Elevation for Cell 4A is at 5607.83 feet above mean sea
level amsl
iv The Surveyor will set up the Survey Instrument in location where both
the applicable Reference Point and pond surface are visible For Cell 4A
this is typically on the road between Cell and Cell4A approximately 100
feet east of the Cell 4A Reference Point
Once in location the Surveyor will ensure that the Survey Instrument is
level by centering the bubble in the level gauge on the Survey Instrument
viThe Assistant will place the Survey Rod vertically on the Cell 4A
Reference Point The Assistant will ensure that the Survey Rod is vertical
by gently rocking the rod back and forth until the Surveyor has established
level reading
vii The Surveyor will focus the cross hairs of the Survey Instrument on the
scale on the Survey Rod and record the number the Reference Point
Reading which represents the number of feet the Survey Instrument is
reading above the Reference Point
The Assistant will then move to designated location where the Survey
Rod can be placed on the surface of the main solution pond in Cell 4A
The designated location for Cell 4A is in the northeast corner of the Cell
where the side slope allows for safe access to the solution surface
The approximate coordinate locations for the measuring points for Cell 4A
is 2579360 east and 320300 north These coordinate locations may vary
somewhat depending on solution elevations in the Cell
The Assistant will hold the Survey Rod vertically with one end of the
Survey Rod just touching the pond surface The Assistant will ensure that
the Survey Rod is vertical by gently rocking the rod back and forth until
the Surveyor has established level reading
viii The Surveyor will focus the cross hairs of the Survey Instrument on the
scale on the Survey Rod and record the number the Pond Surface
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
Reading which represents the number of feet the Survey Instrument is
reading above the pond surface level
The Surveyor will calculate the elevation of the pond surface in feet amsl
by adding the Reference Point Reading for the Cell and subtracting the
Pond Surface Reading for the Cell and will record the number accurate to
0.01 feet
Leak Detection System
The Leak detection system is monitored on continuous basis by use of
pressure transducer that feeds water level information to an electronic data
collector The water levels are measured every hour and the infonnation
is stored for later retrieval The water levels are measured to the nearest
0.10 inch The data collector is currently programmed to store days of
water level information The number of days of stored data can be
increased beyond days if needed The water level data is downloaded to
laptop computer on weekly basis and incorporated into the Mills
environmental monitoring data base and into the files for weekly
inspection reports of the tailings cell leak detection systems Within 24
hours after collection of the weekly water level data the information will
be evaluated to ensure that the water level in the leak detection sump
did not exceed the allowable level 5556.14 feet amsl and the average
daily flow rate from the LDS did not exceed the maximum daily allowable
flow rate at any time during the reporting period For Cell 4A under no
circumstance shall fluid head in the leak detection system sump exceed
1-foot level above the lowest point in the lower flexible membrane liner
To determine the Maximum Allowable Daily LDS Flow Rates in the Cell
4A leak detection system the total volume of all fluids pumped from the
LDS on weekly basis shall be recovered from the data collector and that
information will be used to calculate an average volume pumped per day
Under no circumstances shall the daily LDS flow volume exceed 24160
gallons/day The maximum daily LDS flow volume will be compared
against the measured cell solution levels detailed on the attached Table
to determine the maximum daily allowable LDS flow volume for varying
head conditions in Cell 4A Any abnormal or out of compliance water
levels must be immediately reported to Mill management The data
collector is also equipped with an audible alarm that sounds if the water
level in the leak detection sump exceeds the allowable level 5556.14 feet
amsl The current water level is displayed at all times on the data
collector and available for recording on the daily inspection form The
leak detection system is also equipped with leak detection pump EPS
Model 25S05-3 stainless steel or equal The pump is capable of
pumping in excess of 25 gallons per minute at total dynamic head of 50
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Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
feet The pump has 1.5 inch diameter discharge and operates on 460
volt phase power The pump is equipped with pressure sensing
transducer to start the pump once the level of solution in the leak detection
sump is approximately 2.25 feet elevation 5555.89 above the lowest
level of the leak detection sump inches above the lowest point on the
lower flexible membrane liner to ensure the allowable 1.0 foot 5556.14
feet amsl above the lowest point on the lower flexible membrane liner is
not exceeded The attached Figure Leak Detection Sump Operating
Elevations illustrates the relationship between the sump elevation the
lowest point on the lower flexible membrane liner and the pump-on
solution elevation for the leak detection pump The pump also has manual
start and stop controls The pump will operate until the solution is drawn
down to the lowest level possible expected to be approximately inches
above the lowest level of the sump approximate elevation 5554.0 The
pump discharge is equipped with 1.5 inch flow meter EPS Paddle
Wheel Flowsensor or equal that reads the pump discharge in gallons per
minute and records total gallons pumped The flow rate and total gallons
is recorded by the Inspector on the weekly inspection form The leak
detection pump is installed in the horizontal section of the 18 inch
horizontal perforated section of the PVC collection pipe The distance
from the top flange face at the collection pipe invert to the centerline of
the 22.5 degree elbow is 133.4 feet and the vertical height is
approximately 45 feet The pump is installed at least feet beyond the
centerline of the elbow The bottom of the pump will be installed in the
leak detection sump at least 135.4 feet or more from the top of the flange
invert pressure transducer installed with the pump continuously
measures the solution head and is programmed to start and stop the pump
within the ranges specified above The attached Figure illustrates the
general configuration of the pump installation
second leak detection pump with pressure transducer flow meter and
manufacturer recommended spare parts for the pump controller and water
level data collector will be maintained in the Mill warehouse to ensure that
the pump and controller can be replaced and operational within 24 hours
of detection of failure of the pumping system The root cause of the
equipment failure will be documented in report to Mill management with
recommendations for prevention of re-occurrence
Slimes Drain System
pump Tsurumi Model KTZ23.7-62 stainless steel or equal will be
placed inside of the slimes drain access riser pipe and near as possible to
the bottom of the slimes drain sump The bottom of the slimes drain sump
is 38 feet below water level measuring point at the centerline of the
Page
Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
slimes drain access pipe near the ground surface level The pump
discharge will be equipped with inch flow meter EM Model 33 or
equal that reads the pump discharge in gallons per minute and records
total gallons pumped The flow rate and total gallons will be recorded by
the Inspector on the weekly inspection form
ii The slimes drain pump will be on adjustable probes that allows the pump
to be set to start and stop on intervals determined by Mill management
iiiThe Cell 4A slimes drain pump will be checked weekly to observe that it
is operating and that the level probes are set properly which is noted on
the Weekly Tailings Inspection Form If at any time the pump is observed
to be not working properly it will be repaired or replaced within 15 days
ivDepth to wastewater in the Cell 4A slimes drain access riser pipe shall be
monitored and recorded weekly to determine maximum and minimum
fluid head before and after pumping cycle respectively All head
measurements must be made from the same measuring point to the
nearest 0.01 foot The results will be recorded as depth-in-pipe
measurements on the Weekly Tailings Inspection Form
On monthly basis the slimes drain pump will be turned off and the
wastewater in the slimes drain access pipe will be allowed to stabilize for
at least 90 hours Once the water level has stabilized based on no change
in water level for three successive readings taken no less than one
hour apart the water level of the wastewater will be measured and
recorded as depth-in-pipe measurement on the Monthly Inspection Data
form by measuring the depth to water below the water level measuring
point on the slimes drain access pipe
The slimes drain pump will not be operated until Mill management has
determined that no additional process solutions will be discharged to Cell 4A and
the Cell has been partially covered with the first phase of the reclamation cap
The long term effectiveness and performance of the slimes drain dewatering will
be evaluated on the same basis as the currently operating slimes drain system for
Cell
Tailintzs Emcr2encies
Inspectors will notify the Radiation Safety Officer and/or Mill management immediately
if during their inspection they discover that an abnormal condition exists or an event has
occurred that could cause tailings emergency Until relieved by the Environmental or
Radiation Technician or Radiation Safety Officer inspectors will have the authority to
direct resources during tailings emergencies
Any major catastrophic events or conditions pertaining to the tailings area should be
reported immediately to the Mill Manager or the Radiation Safety Officer one of whom
Page 10
Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
will notify Corporate Management If dam failure occurs notify your supervisor and the
Mill Manager immediately The Mill Manager will then notify Corporate Management
MSHA 303-231-5465 and the State of Utah Division of Dam Safety 801-538-7200
Cell 4A Solution Freeboard Calculation
The maximum tailings cell pond wastewater levels in Cells 1-I Cell Cell and Cell 4A
are regulated by condition 10.3 of the White Mesa Mill le.2 Materials License
Condition 10.3 states that Freeboard limits for Cells 1-1 and shall be set
periodically in accordance with the procedures set out in Section 3.0 to Appendix
of the previously approved NRC license application including the October 13 1999
revisions made to the January 10 1990 Drainage Report The freeboard limit for
Cell shall be recalculated annually in accordance with the procedures set in the
October 13 1999 revision to the Drainage Report The 1990 Drainage Report uses
the Local 6-hour Probable Maximum Precipitation PMP event for calculating the
freeboard requirements for each of the tailings cells The PMP for the White Mesa site is
10 inches
Based on the PMP storm event the freeboard requirement for Cell is maximum
operating water level of 5615.4 feet above mean sea level amsl The Cell freeboard
limit is not affected by operations or conditions in Cells or 4A
Cell has no freeboard limit because the Cell is 99%frill of tailings solids and all
precipitation falling on Cell and the adjacent drainage area must be contained in Cell
The flood volume from the PMP event over the Cell and Cell pond areas plus the
adjacent drainage areas is 123.4 acre-feet of water According to the freeboard
calculation procedures this volume currently must be contained in the existing 24-acre
pool area in Cell This results in maximum operating water level in Cell of 5601.6
feet amsl
The Cell 4A design includes concrete spillway between Cell and Cell 4A with the
invert elevation feet below the top of the Cell dike at an elevation of 5604.5 feet
amsl Once Cell 4A is placed in operation the cell would be available for emergency
overflows from Cell but as long as the freeboard limit in Cell is maintained at 5601.6
it is extremely unlikely that Cell 4A would see any overflow water from Cell unless the
full PMP event were to occur Should Cell receive the full PMP volume of 123.4 acre
feet of water approximately 62 acre feet of that volume would flow through the spillway
into Cell 4A
The flood volume from the PMP event over the Cell 4A area is 36 acre-feet of water 40
acres plus the adjacent drainage area of 3.25 acres times the PMP of 10 inches This
would result in total flood volume of 98 acre-feet including the 62 acre-feet of solution
from Cell The freeboard depth required for Cell 4A from the PMP event would be
2.44 feet plus wave mn-up depth of 0.77 feet from the 1990 Drainage Report for
Page 11
Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
total freeboard requirement of 3.2 feet This calculation is illustrated on Attachment
The Groundwater Quality Discharge Permit No UGW370004 for the White Mesa Mill
requires that the minimum freeboard be no less than 3.0 feet for any of the existing Cell
construction but based on the above calculation the freeboard would be set 3.2 feet
below the top of liner The freeboard for Cell 4A would therefore be 5595.3 amsl top of
liner 5598.5 3.2 feet Figure Hydraulic Profile Schematic shows the relationship
between the Cells and the relative elevations of the solution pools and the spillway
elevations
If Cell 4A were required to store the entire PMP event for Cell Cell and Cell 4A the
required storage volume would be approximately 160 acre-feet of solution This would
increase the necessary freeboard to 4.77 feet
The required freeboard for Cell 4A will be recalculated annually along
with the re
calculation of the Cell freeboard requirement calculation of the current freeboard
calculation for both Cells is attached to this Plan
Page 12
Cell 4A BAT Monitoring Operations and Maintenance Plan 09/08 Revision Denison 1.3
Attachments
Figure Initial Filling Plan GeoSyntec Consultants
Figure Initial Filling Plan Details and Sections GeoSyntec Consultants
Figure Initial Filling Plan Solution and Slurry Pipeline Routes GeoSyntec
Consultants
Figure Interim Filling Plan GeoSyntec Consultants
Figure Leak Detection System Sump GeoSyntec Consultants
Figure Leak Detection Sump Operating Elevations
Figure Hydraulic Profile Schematic
Cell and Cell 4A Freeboard Calculation
Table Calculated Action leakage Rates for Various Head Conditions
Cell 4A White Mesa Mill Blanding Utah GeoSyntec Consultants
10 White Mesa Mill Tailings Management System and Discharge Minimization
Technology DMT Monitoring Plan 3/07 Revision DUSA-2 32 pages or
currently approved version of the DMT
Page 13
2/
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Table
Calculated Action Leakage Rates GeoSyntec Consultants
for Various Head Conditions
Cell 4A White Mesa Mill
Blanding Utah
Head Above Liner
System feet
Calculated Action Leakage
Rate gallons/acrelday
222.04
10 314.01
15 384.58
20 444.08
25 496.50
30 543.88
35 587.46
37 604.01
No PBL-4 INTERNATIONAL URANIUM USA CORPORATION
Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date March 15 2001 Title Clearance of Linde Material Intermodal Containers
Purpose
The purpose of this Procedure is to document the steps to be followed to ensure that prior to
receipt of Linde materials at the White Mesa Mill the Mill the materials have been properly
sampled and analyzed in accordance with the IT Corporation Sampling and Analysis Plan the
IT SAP and the IT Contained-Tn Sampling Work Plan and have satisfied other applicable
requirements This procedure may be amended subject to approval by IUSAs Safety and
Environmental Review Panel SERP from time to time as appropriate
Clearance Procedure for Linde Materials
The following steps must be followed before any Linde materials may be received at the Mill for
processing
2.1 IT will conduct sampling of the Linde materials at the Linde site in accordance with the IT
SAP and IT Contained-In Sampling Work Plan for total VOCs and total SVOCs IT will
forward the sample results immediately upon receipt to IUSA or JUSAs independent
RCRA consultant 1JSAs RCRA consultant and the New York State Department of
Environmental Conservation NYSDEC IT will transmit sample results to TUSA under
cover letter which states that chemical data in each package has been reviewed by IT all
results are consistent with the current Radioactive Material Profile Record RMPR The
date of the referred RMPR should be noted all results are below NYSDECs TAGM 3028
contained out action levels as referenced in the Linde Site Contained-Tn Sampling Work
Plan and the sample locations are within the geographical areas that are included within
the contained-in area IT has been instructed to have the sampling results transmitted to
IUSA prior to the IMCs associated with the sampling results arriving at the Mill
2.2 IUSAs RCRA consultant will review the sample results and if available confirmation
letter from NYSDEC to confirm that
the results are consistent with the referenced RMPR
none of the sample results indicate the existence of chemical components not listed in
IUSAs Lists of Acceptable Contaminants attached hereto as Attachment
the sample locations are within the geographical areas that are included within the
contained-in area and
all results for VOCs and SVOCs other than PAils are below NYSDECs TAGM
3028 contained out action levels as referenced in Attachment
If JUSAs RCRA Consultant identifies that the IT cover letter is inconsistent with any of the four
conditions listed above or is lacking any information referred to in 2.1 IUSAs RCRA
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Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date March 15 2001 Title Clearance of Linde Material Intermodal Containers
Consultant will advise either the Vice President Regulatory Affairs or his designee who will
determine whether or not the letter is acceptable
2.3 If
the analysis of the sample results indicates that all four conditions detailed in Section
2.2 are satisfied
then no further actions are required under this Section 2.3
If
IUSAs RCRA consultant identifies some chemical components other than any
chemical components that have been determined to be due solely to Lab influence
that could possibly be listed hazardous wastes and are identified in Attachment then
the following steps will be taken
IUSA will advise IT that further technical review is required to determine
whether the new constituents is not from RCRA listed source from
RCRA listed source but can be contained-out under TAGM or from RCRA
listed source and cannot be contained-out under TAGM
ii IT will perform RCRA analysis to determine if the new compound is
RCRA listed waste IUSA will assist IT in this analysis as appropriate
iii IUSAs RCRA consultant will prepare technical memorandum for review by
IUSAs SERP Committee addressing whether or not the new compound is
listed hazardous waste and whether or not the new compound may pose any
material handling safety or environmental impacts at the Mill IT the
generator after performing its own RCRA analysis will make the final
determination and advise IUSA in writing of the determination results before
IMCs containing material associated with the sample results undergoing listed
waste determination reach the Mill
iv meeting of IUSAs SERP will be scheduled to review ITs analysis and
recommendations IUSAs RCRA consultants analysis and any other
pertinent information to determine whether or not the new chemical
components are listed hazardous wastes or whether they are not listed
hazardous wastes
If the SERP concludes that the compound is not RCRA listed waste
then it will be added to the list of acceptable compounds for the Mill
found in Attachment IT will provide IUSA an updated revision
with date of the Preliminary Material Characterization Report
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Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date March 15 2001 Title Clearance of Linde Material Intermodal Containers
PMCR as soon as possible No change to the RMPR will be
required for this situation
If the contaminant is determined to be subject to the TAGM by IT and
NYSDEC IT will provide IUSA written confirmation of this
determination together with an updated revision with date of the
PMCR as soon as possible JUSAs SERP will review the
determination and if agreed to Attachment will be updated IT will
also be required to submit an updated RMPR to IUSA addressing this
determination
If the SERP concludes that the compound resulted from RCRA listed
source but it is not added to the TAGM list by NYSDEC then any
materials that based on IT confirmatory excavation results contain
such compound will not be shipped to the Mill or if received at the
Mill will be returned to IT
If
IUSAs RCRA Consultant is unable to confirm that all of the conditions set out in
Section 2.2 and have been satisfied IUSAs RCRA Consultant will advise
the Vice President Regulatory Affairs or his designee of this fact and the Vice
President Regulatory Affairs or his designee will make determination as to what
additional steps if any are required in order to clear the material that is characterized
by the sample results for receipt at the Mill
2.4 Periodically IUSA will arrange to send to the Utah Department of Environmental QualityUDEQcopyofallsampleresultsfromITthathave been received and technically
reviewed If any SERP actions are required to have been taken with respect to any of that
data copies of the applicable SERP reports will also be sent to the UDEQ
2.5 UDEQ has advised IUSA that they will contact IUSA if they have any concerns with any of
the data or SERP reports that have been sent to them They have agreed that it is not
necessary for IUSA to contact UDEQ regarding any of the sampling data or accompanying
analysis subject to Section 2.6 below
2.6 If any of the sample data indicates the presence of an anomaly i.e an unusual new
chemical component that does not fit within the general rationale that has been applied to
date for other chemical components then IUSA will contact UDEQ to confirm that UDEQ
is satisfied with IUSA technical review and that the anomaly is not listed hazardous
waste At the time of sending in such sample data IUSA will contact Don Verbica or
equivalent at UDEQ to arrange for discussion of the sample results and JUSA will
receive verbal or written confirmation from Don Verbica or equivalent that UDEQ is
satisfied that the anomaly is not listed hazardous waste
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Rev No R-0 STANDARD OPERATING PROCEDURES Page of
Date March 15 2001 Title Clearance of Linde Material Intermodal Containers
2.7 Simultaneously with the steps set out in Sections 2.3 to 2.5 above IUSAs RCRA
Consultant or other person designated by the Vice President Regulatory Affairs will
correlate sample results from IT to IMC Shipper numbers sent to the Mill in accordance
with the following procedure
For each IMC find the Shipper Number Linde-It on IT Linde Site to JUG Ship Log
the Ship Log sheet Find the Sample It corresponding to each IMC on the Ship
Log Fill in the Sample It column in for each IMC on the IT Data Checklist form
When JUSAs RCRA Consultant or designee has determined that set of sampling
results are acceptable via the process in either Section 2.2 or 2.3 above IUs RCRA
Consultant or designee will indicate that the IMCs associated with those results should
receive interim clearance for entrance to the Mill by filling in dates in the columns
VOC OK and SVOC OK in the IT Data Checklist form and the column IMCs
Interim Cleared in the Linde Lot Control database
2.8 As soon as IUSAs RCRA Consultant and Vice President Regulatory Affairs or his
designee have determined that one or more IMCs has satisfied all of the following criteria
By following the procedure contained in Section 2.7 above IUSAs RCRA Consultant
or designee has determined that the IT sample results have been received with respect
to all materials contained in that batch of IMCs and
No new chemical components other than chemical components that have been
determined to be due to Lab influence have been identified in any of the sample
results relating to that batch of IMCs or if any new chemical components have been
identified the procedures set out in Section 2.3 above have been followed
I1Js RCRA Consultant together with either IUSA Vice President Regulatory Affairs
or his designee will prepare memorandum advising IUSA President or his designee of
that fact including the identification numbers of the IMCs
2.9 Upon receipt of the memorandum referred to in Section 2.8 IUSAs President or his
designee will advise the Plant Manager in writing of the IMCs acceptable for receipt at the
Mill
2.10 Upon receipt of the memorandum the Mill staff will follow the receipt procedures as
detailed in SOP PBL-2 Intermodal Container Acceptance Handling and Release for receipt
of the IMCs at the Mill
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ATTACHMENT
LISTS OF ACCEPTABLE CONTAMINANTS
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Attachment Table
List of Contaminants in Linde Uranium Material
RCRA FOOl
Acceptable When Contained Out Subject to NYSDEC TAGM 3028
Volatile Organic Chemical VOC Contaminant TAGM Action
Level_ug/kg
Carbon tetrachioride 4900
Chlorobenzene 1800000
12-Dichioroethene total cis and trans isomers
cis and trans 12 DCE
cis-780000
trans-1600000
trans-12-Dichloroethene trans 12 DCE 1600000
12 Dichloroethane 12 DCA 7000
Methylene chloride 85000
Tetrachioroethene PCE 12000
111 -Trichioroethane 111 TCA 7000000
Trichlorethene TCE 58000
Attachment Table
List of Contaminants in Linde Uranium Material
Other Acceptable Contaminants
Volatile Organic Chemical VOC Contaminant TAGM Action
Level_uglkg
Acetone 7800000
Butanone 47000000
Benzene 22000
Bromoform 81000
Carbon disulfide 7800000
Chloroform 100000
Chioromethane 49000
11 -Dichioroethene 1100
Ethylbenzene 7800
Hexachioroethane 46000
Pentachlorophenol 3000
11 22-Tetrachloroethane 3200
Toluene 18000000
Trichiorofluoromethane 23000000
Vinyl chloride 340
Xylene total 160000000
NYSDEC requires that contaminants from both RCRA-listed and non-listed waste sources must not exceed TAGM
3028 action levels
Attachment Table continued
List of Contaminants in Linde Uranium Material
Other Acceptable Contaminants
Semi-Volatile Organic Chemical SVOC
Contaminant
TAGM Action
Level ug/kg
Acenaphthene 4700000
Acenaphthylene
Anthracene 23000000
Benzo anthracene 900000
Benzo pyrene 90
Benzo fluoranthene 900
Benzo ghi perylene ---
Benzo fluoranthene 9000
Bis 2-ethyihexyl phthalate 46000
Chrysene 88000
Dibenz ah anthracene 90
Dibenzofuran ---
Di-n-butyl phthalate 7800000
Fluoranthene 3100000
Fluorene 3100000
2-Methylnaphtahalene ---
Methyiphenol ---
Naphthalene 310000
N-nitrosodiphenylamine 130000
Phenanthrene ---
Pyrene 2300000
Polychiorinated biphenyls PCBs Arochiors
1248 1254 1260
50000
TAGM action levels have not been established for some contaminants
No PBL-6 INTERNATIONAL URANIUM USA CORPORATION
Rev No R-1 STANDARD OPERATING PROCEDURES Page of
Date Feb 14 2003 Title Heritage Alternate Feed Management
1.0 Purpose
The following procedure applies to acceptance of alternate feed materials from Heritage
Minerals Inc HMI which International Uranium USA Corporation IUSA determines
to potentially contain levels of thorium that require that special procedures be followed
which are over and above those required for conventional ores or other alternate feed
materials This procedure may be amended subject to approval by I1JSAs Safety and
Environmental Review Panel SERP from time to time as appropriate to incorporate
information and results obtained from the evaluation of health physics surveys
monitoring and controls implemented pursuant to keeping radiological exposures to
employees the public and the environment As Low As Reasonably Achievable
ALARA
The methods set forth in this Standard Operating Procedure SOP are based on the
assumption that the HMI materials will be delivered to the White Mesa Mill in 20-ton
intermodal containers IMCs Should the delivery method be modified IUSA will
revise this SOP to address the selected mode of delivery
2.0 Ore Receiving
For material receiving procedures see Section 2.0 of White Mesa Mill SOP PBL-2
Intennodal Container Acceptance Handling and Release
3.0 Ore Dumping
After the IMC has been dropped off in the Restricted Area connect the Bartlett
tipper to the chassis with loaded IMC and transport across the truck scales
After weighing the IMC move the tipper and chassis onto the ore storage pad
Enter the loaded weight of the IMC on the IMC SWT
Remove the tarp on the back of the IMC and open the tailgate
Dump the material in the IMC onto the ore storage pad
After all material has been removed from the IMC transport the empty IMC back
across the scales for an empty weight
Record the empty weight on the appropriate IMC SWT
At the end of each day turn in outbound SWT to Mill Records Manager
The Mill Records Manager will fill out Daily Materials Receipts form to obtain
the net weight of the material in each IMC
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Rev No R-1 STANDARD OPERATING PROCEDURES Page of
Date Feb 14 2003 Title Heritage Alternate Feed Management
After weighing the IMC the Bartlett tipper will deposit the IMC in designated
area within the Restricted Area for decontamination
10 Use front-end loader or similar equipment to push material into the designated
ore lot pile
11 The HMI material will be stored in one stockpile to enhance dust control and
minimize exposure risks The stockpile size not including the cover material will
not exceed height of 10 feet
12 Dust suppression measures will include the following
The stockpile will be wet down at least once per day until such
time that it is covered
The completed stockpile will be covered with Ashland material or
another suitable material to provide cover of the stockpile to
reduce the potential of dusting and provide temporary radiation
cover
All stockpiles will be inspected at least once per day to ensure the
integrity of the covering
In the event of wind speeds in excess of 20 MPH all dumping
activities will cease immediately
4.0 Radiation Monitoring during Ore Receipt
Due to the potential for higher concentrations of thoron and other potential radiological
hazards during HMI material receipt and handling Radiation Work Permit RWP will
be issued during the initial receipt of HivIl material The RWP will list the health physics
controls required personal protective equipment dust control monitoring and survey
requirements necessary to assess the radiological exposure potential to employees
operating under the RWP
As soon as the results of the monitoring activity conducted in accordance with the
conditions indicated by the RWP have been evaluated the added radiological surveys
applicable to the particular HMI material will be established communicated to the
Radiation Safety Technicians RSTs conducted and documented Irrespective of the
added surveys selected the following radiological surveys will be performed routinely
for the duration of the receipt of HMI material Based upon results of monitoring and
dose calculations recognizing that there may be potential for higher than normal
radiological exposures the Mill Radiation Safety Officer RSO may recommend that
personnel be rotated from area to area periodically in order to reduce potential exposure
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Rev No R-1 STANDARD OPERATING PROCEDURES Pa ge 30
Date Feb 14 2003 Title Heritage Alternate Feed Management
4.1 Area Airborne Sampling
Weekly area airborne sampling will be conducted in the areas of the Mill listed
below twenty-four hour air sample will be collected at flow rate of 40 liters
per minute or greater After sufficient data has been collected and reviewed by
the RSO and ALARA Committee area airborne sampling frequency may be
reduced to once every two weeks during the receiving of HMI mill feed
HMI Stockpile area
Scalehouse area
The above samples will be analyzed for gross alpha
4.2 DAC Determination
composite feed sample of HMI material was analyzed for radioisotropic
composition The data were used by the RSO to establish derived air
concentration DAC
The DAC for the HMI material that was established based upon data gathered
under RWP370 and which will be applied during processing of the HMI
material is 1.24ff2 pCi/cc based on thorium
If air sample results indicate an airborne radioactive dust concentration of 25%of
the thorium DAC in any of the areas sampled during processing then the air
sample frequency will be increased to daily in those areas until mitigative
measures have reduced concentrations below 25%of the thorium DAC for two
consecutive days
4.3 Breathing Zone Samplipg
Breathing zone air samples will be collected once per week on select
individuals who perform routine work tasks associated with receiving
operations After sufficient data has been collected and reviewed by the
RSO and ALARA Committee breathing zone sampling frequency may be
reduced to once every two weeks or greater during the receiving of HMI
materials
Breathing zone air samples will be collected from individuals who
perform work tasks under an RWP
In addition to the above sampling under and further breathing zone
samples may be collected from individuals at the discretion of the RSO
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Rev No R-l STANDARD OPERATING PROCEDURES Page of
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4.4 Surveys For External Radiation
All employees working with HMI material will wear personal radiation
monitoring device The devices will be collected quarterly and the results
entered on individual exposure forms
Beta/gamma dose rate measurements will be performed weekly in all areas
of the Mill operations These data will be used to perform monthly dose
rate calculations
Individuals who perform work tasks that are anticipated to exhibit the
highest potential dose rate exposures may be directed by the RSO at his
discretion to wear monthly personal radiation monitoring devices
4.5 Surveys for Radon-222 Radon-220 and Their Daughters
Weekly measurements of radon daughter concentrations for both Ra-222 and Ra
220 will be conducted in those areas of the Mill listed above in Section 4.1 of this
SOP If radon daughter concentrations from either the uranium or thorium parent
are less than 25%of the limit 0.08 working level for Ra-222 or 0.25 working
level for Ra-220 the sampling frequency will be decreased to monthly
5.0 Radiation Monitoring during
Ore Processing
Radiation Work Permit RWP will be issued during the initial processing of HMI
material The RWP will list the health physics controls required personal protective
equipment dust control monitoring and survey requirements necessary to assess the
radiological exposure potential to employees operating under the RWP
As soon as the results of the monitoring activity conducted in accordance with the
conditions indicated by the RWP have been evaluated any added radiological surveys
applicable to the HMI material will be established communicated to the Radiation Safety
Technicians RSTs conducted and documented frrespective of the added surveys
selected the following radiological surveys will be performed routinely for the duration
of the processing of HMI material that is from the time the material is fed to process to
tailings disposition Based upon results of monitoring and dose calculations the RSO
may recommend that personnel be rotated from area to area periodically in order to
reduce potential exposure
5.1 Area Airborne Sampling
Initial area airborne sampling will be conducted during HMI material feeding at
locations where it is known that the potential for dust normally exists during
material feed operations specifically alongside the portable and the stationery
grizzly and at the belt drop chute into the trommel Samples will also be taken
during initial ore feeding operations
in any other areas which show evidence of
dusting At minimum initial area air samples will be collected for at least two
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hours at collection flow rate of 40 liters per minute or greater These samples
will be analyzed for gross alpha using
standard laboratory methods described in
Mill Radiation Protection SOPs but applying the modified DAC limits for HMI
material that were established with RWP 370 detailed in Section 4.2 above
As processing progresses additional area air samples will be collected and
analyzed using the same air sampling procedures described above in areas such
as the Leach area or any other process areas in which the RSO determines it
would be useful to quantify the potential for air emissions
5.2 DAC Determination
As noted above in Section 4.2 composite feed sample of HivIl material was
analyzed for radioisotropic composition The data were used by the RSO to
establish derived air concentration DAC 1.24W2 RCi/cc based on thorium
If air sample results indicate an airborne radioactive dust concentration of 25%of
the thorium DAC in any of the areas sampled during processing then the air
sample frequency will be increased to daily in those areas until mitigative
measures have reduced concentrations below 25%of the thorium DAC for two
consecutive days
5.3 Breathing Zone Sampling
Breathing zone air samples will be collected for at least four hours at
collection flow rate of four liters per minute during initial HMI material
processing for select individuals performing material feed operations
namely the loader and tromrnel operators
Breathing zone air samples will he collected from individuals who
perform work tasks under an RWP
In addition to the above sampling under and further breathing zone
samples may be collected from individuals at the discretion of the RSO
5.4 Tailings Management
Tailings resulting from processing HMI material will be deposited in an area of
the tailings system that will ensure that the material is fully submerged beneath
pond liquid and/or tailings slurry from non-HMI alternate feed materials until
such time as the first layer of interim cover or random fill is placed on the tailings
system This will minimize the potential for thoron gas to escape to the
atmosphere Mill Management and the RSO will coordinate efforts to ensure that
operations personnel are provided direction regarding placement of HMI tailings
In addition the weekly tailings inspections reports will document the placement
of HMI tailings during the preceding week
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Rev No R-1 STANDARD OPERATING PROCEDURES Page of
Date Feb 14 2003 Title Heritage Alternate Feed Management
5.5 Surveys For External Radiation
All employees working with HMI material will wear personal radiation
monitoring device The devices will be collected quarterly and the results
entered on individual exposure forms
Beta/gamma dose rate measurements will be performed weekly in all areas
of the Mill operations These data will be used to perform monthly dose
rate calculations
Individuals who perform work tasks that are anticipated to exhibit the
highest potential dose rate exposures will wear monthly personal radiation
monitoring devices
5.6 Surveys for Radon-222 Radon-220 and Their Daughters
Monthly measurements of radon daughter concentrations for both Ra-222
and Ra-220 will be conducted in those areas of the Mill listed above in
Section 5.1 of this SOP If radon daughter concentrations from either the
uranium or thorium parent is greater than 25%of the limit 0.08 working
level for Ra-222 or 0.25 working level for Ra-220 the sampling frequency
will be increased to weekly in areas where these levels are routinely
encountered The radiation safety staff will check all ventilation systems
in the Mill daily
6.0 Decontamination and Release of IMCs
For intermodal release procedures see White Mesa Mill Standard Operating Procedure
PBL-2 Intennodal Container Acceptance Handling and Release
7.0 Hazard Identification and Safety
In addition to the usual safety procedures required for work at the Mill the following
safety procedures are to be followed for projects involving HMI materials
7.1 Required Personnel Protective Equipment PPE
In all areas of the Mill covered by this procedure hard hats safety glasses and
steel-toed shoes are required as minimum These must be worn in all areas of
the Mill with the exception of the Administration Building
The following are required while handling HMI material
Coveralls
Leather or rubber gloves
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Date Feb 14 2003 Title Heritage Alternate Feed Management
Rubber Boots or Booties
Respiratory protection as directed by the RSO or specified in an
RWP Respiratory protection will be used during initial receipt
and handling of HMI feed materials and until material-specific
DAC values are set In addition all individuals who work in areas
where there is likelihood that the airborne concentration DAC
limits for either uranium radon thoron or thorium will exceed
25%of the DAC will be required to wear respiratory protection as
directed by the RSO See section 8.1.2 below
7.2 Industrial Hazards and Safety
Use caution when chassis are backing onto the Ore Pad
Ensure that all personnel within 50 feet of the area where the IMC is
hooked up to the Bartlett tipper are aware that dumping is about to
commence
Bartlett tipper operators must use caution during the dumping process
Move at least 25 feet away from the rear of the IMC during the initial
dumping operation
Do not place any part of your body inside the IMC when the chassis is
being tipped and the tailgate is open The IIvIC could be lowered or
accidentally fall at any time which would cause the tailgate to close
rapidly and result in injury Only work under the tailgate after it has
been properly blocked open
Be aware of high-pressure wash water
When the crane is in operation make sure all personnel except the
persons in charge of the tag lines are 50 feet away from the IMC
being moved The persons in charge of the tag lines should never be
underneath the IMC that is being moved
Be aware of slippery conditions on the ore pad during periods of
inclement weather
Be aware of the potential for ice build-up on and around the
decontamination pad during periods of cold weather
Use caution when entering or exiting equipment Be sure to use the
ladders and hand rails Do not jump off of the equipment
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Rev No R-1 STANDARD OPERATING PROCEDURES Page of
Date Feb 14 2003 Title Heritage Alternate Feed Management
8.0 Radiological and Environmental Concerns
Environmental radiation monitoring is routinely performed at the White Mesa Mill at
sufficient frequency quarterly and semiannually that any potential impact to the public
and or the environment would be identified
8.1 Airborne Radiation Protection
The areas of the ore storage pad used for HMI material will only be posted
as either Radiation Area and/or Airborne Radioactivity Area in
accordance with 10 CFR 20.1902
All personnel involved with material handling will be required to wear
full face respirator until such time that review of the air samples by the
RSO and ALARA committee indicate that this level of protection is not
needed Employees will be notified of any changes to the respiratory
protection requirements by memorandum
Subsequent to approvals by the RSO and ALARA Committee for reduced
posting if based on air sampling an area exhibits 25%of the DAC limits
for either uranium or thorium it will be posted Respiratory Protection
Required
All individuals who work in areas where there is likelihood that the
airborne concentration DAC limits for either uranium radon thoron or
thorium will exceed 25%of the DAC will be required to wear respiratory
protection As directed by written memorandum from the RSO one of the
following respirators will be selected
Full Face Respirator
ii Powered Air Purifying Respirator
iii Self Contained Breathing Apparatus SCBA
Personal air monitoring will be conducted as per Section of the White
Mesa Mill Radiation Protection Manual and Sections 4.2 and 5.2 above
8.2 Urinalysis
All personnel involved with the dumping and stockpiling of HMI material and
RSTs involved in monitoring described in this SOP will submit urine sample
every two weeks at minimum or at greater frequency if so directed by the
provisions of an RWP Personnel involved in processing of HMI material will
submit urine samples at the usual frequency prescribed in Mill Radiation
Protection SOPs These samples will be analyzed for uranium content
C\.Documents and Settings\dfrydenlund\.Local Settings\Temporary Internet
Files\Content.Outlook\15CXRH6Z\PBL-6_Heritage Alternate Feed Management_rev 02 14 03.doc
No PBL-6 INTERNATIONAL URANIUM USA CORPORATION
Rev No R-1 STANDARD OPERATING PROCEDURES Page of
Date Feb 14 2003 Title Heritage Alternate Feed Management
Evaluation and corrective actions will be conducted pursuant to guideline
provisions contained in Regulatory Guide 8.22 Bioassay at Uranium Mills In
vivo lung counting may be implemented if circumstances suggest an
overexposure or uptake of either uranium or thorium has occurred In vivo
counting will be conducted at the discretion of the RSO and ALARA Committee
8.3 Personal Hygiene
All personnel involved with the dumping stockpiling or processing of
HMI material will be required to wear coveralls
All personnel will survey their hands boots and clothing for surface
contamination prior to eating or leaving the restricted area
C\Documents and Settings\dfrydenlund\Local Settings\Temporary Internet
Files\Content.Outlook\I5CXRH6Z\PBL-6_Heritage Alternate Feed Management_revi 02 14 03.doc
RECLAMATION PLAN
The Reclamation Plan White Mesa Mill Blanding Utah Source Material License No SUA
1358 Docket No 40-8681 Revision 3.0 JuLy 2000 the Reclamation Plan copy of which
has been provided was transmitted to the Executive Secretary1 by letter dated and is hereby
incorporated by reference The financial surety including the amount for the long term care
fund currently required under Mill License condition 9.5 is $11893975 This amount is
reviewed annually by Denison and the Executive Secretary as required by Mill License
condition 9.5
Part I.D of the GWDP provides that upon commencement of decommissioning Denison shall
reclaim the Mill site and all related facilities stabilize the tailings cells and construct cover
system over the tailings cells in compliance with all engineering design and specifications in the
Mills Reclamation Plan
In that respect Part I.D.6 of the GWDP provides that before reclamation and closure of any
tailings disposal cell the Mill shall ensure that the final design construction and operation of the
cover system at each tailings cell will comply with all requirements of the approved Reclamation
Plan and will for period of not less than 200 years meet the following minimum performance
requirements
Minimize infiltration of precipitation or other surface water into the tailings including
but not limited to the radon barrier
Prevent the accumulation of leachate head within the tailings waste layer that could rise
above or over-top the maximum FML liner elevation internal to any disposal cell i.e
create bathtub effect and
Ensure that groundwater quality at the compliance monitoring wells does not exceed the
Groundwater Quality Standards or Groundwater Compliance Limits specified in the
GWDP
Part I.D.7 also provides that the Co-Executive Secretary reserves the right to require
modifications to the Reclamation Plan for purposes of compliance with the Utah Groundwater
Quality Protection Regulations including but not limited to containment and control of
contaminants or discharges or potential discharges to Waters of the State
hi order to ensure that the Reclamation Plan meets the requirements of the Utah Groundwater
Quality Protection Regulations Part I.H 11 of the GWDP requires that Denison submit for Co
Executive Secretary approval an infiltration and contaminant transport modeling report that
demonstrates the long-term ability of the tailings cells cover system to adequately contain and
control tailings contaminants and protect nearby groundwater quality of the uppermost aquifer
Such Report shall demonstrate how the tailings cell engineering design and specifications will
comply with the minimum performance requirements of Part I.D.6 of the GWDP Denison
submitted work plan for such modeling report for Co-Executive Secretary approval on
74
This page was revised on August 14 2009
September 2005 as required and is currently in the process of completing such report
Ti
74
This page was revised on August 14 2009
RECLAMATION PLAN
The Reclamation Plan White Mesa Mi14 Blanding Utah Source Material License No SUA
1358 Docket No 40-8681 Revision 3.0 July 2000 the Reclamation Plan copy of which
has been provided to the Executive Secretary is hereby incorporated by reference The financial
surety including the amount for the long term care fund currently required under Mill License
condition 9.5 is $11893975 This amount is reviewed annually by Denison and the Executive
Secretary as required by Mill License condition 9.5
Part I.D of the GWDP provides that upon commencement of decommissioning Denison shall
reclaim the Mill site and all related facilities stabilize the tailings cells and construct cover
system over the tailings cells in compliance with all engineering design and specifications in the
Mills Reclamation Plan
In that respect Part I.D.6 of the GWDP provides that before reclamation and closure of any
tailings disposal cell the Mill shall ensure that the final design construction and operation of the
cover system at each tailings cell will comply with all requirements of the approved Reclamation
Plan and will for period of not less than 200 years meet the following minimum performance
requirements
Minimize infiltration of precipitation or other surface water into the tailings including
but not limited to the radon barrier
Prevent the accumulation of leachate head within the tailings waste layer that could rise
above or over-top the maximum FML liner elevation internal to any disposal cell i.e
create bathtub effect and
Ensure that groundwater quality at the compliance monitoring wells does not exceed the
Groundwater Quality Standards or Groundwater Compliance Limits specified in the
GWDP
Part I.D.7 also provides that the Co-Executive Secretary reserves the right to require
modifications to the Reclamation Plan for purposes of compliance with the Utah Groundwater
Quality Protection Regulations including but not limited to containment and control of
contaminants or discharges or potential discharges to Waters of the State
In order to ensure that the Reclamation Plan meets the requirements of the Utah Groundwater
Quality Protection Regulations Part I.H 11 of the GWDP requires that Denison submit for Co
Executive Secretary approval an infiltration and contaminant transport modeling report that
demonstrates the long-term ability of the tailings cells cover system to adequately contain and
control tailings contaminants and protect nearby groundwater quality of the uppermost aquifer
Such Report shall demonstrate how the tailings cell engineering design and specifications will
comply with the minimum performance requirements of Part I.D.6 of the GWDP Denison
submitted work plan for such modeling report for Co-Executive Secretary approval on
September 2005 as required and is currently in the process of completing such report
74
This page was revised on August 14 2009
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ATTACHMENT
CHANNEL AND TOE APRON
DESIGN CALCULATIONS
OF
WHITE MESA FACILITIES
BLANDING UTAH
PREPARED BY
INTERNATIONAL URANIUM USA CORP
INDEPENDENCE PLAZA
1050 17TH STREET SUITE 950
DENVER CO 80265
ATTACHMENT 7-RESPONSE TO NRC COMMENTS 7/17/98
TABLE OF SIX-HOUR LOCAL PMP RAINFALL DEPTH VS DURATION FOR WHITE MESA MIL
6-Hour Storm Rainfall is 10 inches ref Hydrologic Design Report for White Mesa Mill 1990
6/1 Hr Ratio for WHITE MESA is 1.22 Figure 4.7 and Table 4.4 HMR 49
ONE-HOUR PMP IS 8.20 inches at 5000 ft elevation
97.0%or 7.95 inches at 5600 ft elevation
Plot of data is adaptation of Figure 12.10 HMR 55A to site rainfall
Average elevation of site in vicinity of base of cell 4Aeach tanks
TIME DISTRIBUTION OF FIRST ONE HOUR OR THE ONE-HOUR PMP
after Table 2.1 NUREG CR 4620
DURATION OF RAINFALL DEPTH IN INCHES AT AVERAGE ELEVATION OF
HOURS 1-HR PMP based on Table 6.3A HMR 49
0.25
0.5
0.75
74
89
95
100
111
116
119
121
122
5000 ft
0.00
6.07
7.30
7.79
8.20
9.10
9.51
9.75
9.92
10.00
5600
0.00
5.88
7.08
7.55
7.95
8.83
9.22
9.46
9.62
9.70
RAINFALL RAINFALL OF RAINFALL DEPTH IN
DURATION DURATION ONE-HOUR AT ELEVATION
MINUTES HOURS PMP
2.5
10
15
20
30
45
60
0.04
0.08
0.17
0.25
0.33
0.50
0.75
1.00
27.5
45
62
74
82
89
95
100
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2.25
3.69
5.08
6.07
6.72
7.30
7.79
8.20
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2.19
3.58
4.93
5.88
6.52
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ATTACHMENT 11 RESPONSES TO NRC COMMENTS 7117198
RATIONAL METHOD CALCULATION OF PMF PEAK DISCHARGE VELOCITY AND DEPTH THROUGH CELL DISCHARGE CHANNEL
FLOW PATH
ELEMENT
ELEMENT
LENGTH
MAX
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MIN GRADIENT
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degrees
tc
hours
RAINFALL
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SURFACE
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acres
PEAK
DISCHARGE
cfs
LONGEST 4800 5655 5610 0.0094 0.54 0.54 7.20 13.43 143 1344
FLOW PARAMETERS IN CELL DISCHARGE CHANNEL AT PEAK PMF DISCHARGE
Bedrock Channel
Channel
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ft
Channel
Side
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fl/ft
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ft
Crosa Section
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ar2
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Rft
aRA.S7 Velocity
Allowable
Peak
Velocity
fps
COE 1970
100 31 0.0100 0.025 226 1.62 169.9 1.54 226.95 7.96 8-10
Bedrock Channel 120 31 0.0100 0.025 226 1.45 180.3 1.40 225.46 7.45 8-10
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6.5.8 MILDOS AREA Modeling
For purposes of this Application the MILDOS AREA modeling for the Mill was updated
assuming the Mill was processing high grade Arizona Strip ores at full capacity Section
3.13.42.6 of the Environmental Report discusses this modeling in detail and concludes that1
based on modeling predictions even miming at full capacity in high-grade Arizona Strip ores the
maximum potential doses to the public are well within applicable regulatory standards and
ALARA goals
6.5.9 Summary of Effectiveness of Environmental Controls and Monitoring
As is evident from the various historic environmental monitoring results discussed in this
Section the Mill has operated in compliance with all applicable regulatory standards and
ALARA goals and in maimer that has not resulted in any significant impacts to public health
safety or the environment The MILDOS AREA modeling confirms that based on modeling
predictions the current design and operation controls at the Mill are sufficient to result in
operations at full capacity processing high-grade ores that are within the regulatory standards and
applicable ALARA goals
As result of these historic monitoring results and updated modeling it is evident that the Mills
equipment facilities and procedures are adequate to minimize danger to public health or the
environment and that renewal of the Mills License will not be inimical to the health and safety
of the public
65
This page was revised on August 14 2009
6.5.8 MILDOS AREA Modeling
For purposes of this Application the MILDOS AREA modeling for the Mill was updated
assuming the Mill was processing high grade Arizona Strip ores at full capacity Section
3.13.2.6 of the Environmental Report discusses this modeling in detail and concludes that based
on modeling predictions even running at full capacity in high-grade Arizona Strip ores the
maximum potential doses to the public are well within applicable regulatory standards and
ALARA goals
6.5.9 Summary of Effectiveness of Environmental Controls and Monitoring
As is evident from the various historic environmental monitoring results discussed in this
Section the Mill has operated in compliance with all applicable regulatory standards and
ALARA goals and in manner that has not resulted in any significant impacts to public health
safety or the environment The MILDOS AREA modeling confirms that based on modeling
predictions the current design and operation controls at the Mill are sufficient to result in
operations at full capacity processing high-grade ores that are within the regulatory standards and
applicable ALARA goals
As result of these historic monitoring results and updated modeling it is evident that the Mills
equipment facilities and procedures are adequate to minimize danger to public health or the
environment and that renewal of the Mills License will not be inimical to the health and safety
of the public
65
This page was revised on August 14 2009
Letter of August 14 2009 to the Executive Secretary of the Utah Radiation Control Board
APPENDIX
STORM WATER
BEST MANGEMENT PRACTICES PLAN
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Blanding Utah
June 2008
Prepared by
Denison Mines USA Corp
1050 17th Street Suite 950
Denver CO 80265
TABLE OF CONTENTS
1.0 Purpose
2.0 Scope
3.0 Responsibility
4.0 Best Management Practices
4.1 General Management Practices Applicable to All Areas
4.2 Management Practices for Process and Laboratory Areas
4.3 Management Practices for Maintenance Activities
4.4 Management Practices for Ore Pad Tailings Area and heavy Equipment
Operations
Figures
Figure White Mesa Mill Site Map
Figure Mill Site Drainage Basins
Figure IUSA Mill Management Organization Chart
Figure JUSA Corporate Management Organization Chart
Tables
Table White Mesa Mill Management Personnel Responsible for Implementing
This BMPP
Appendices
Appendix White Mesa Mill Spill Prevention Control and Countermeasures Plan
Appendix White Mesa Mill Emergency Response Plan
Best Management Practices Plan
Revision 1.3 June 12 2008
1.0 INTRODUCTION/PURPOSE
Denison Mines USA Corp DUSA operates the White Mesa Uranium Mill the Mill in
Blanding Utah The Mill is net water consumer and is zero-discharge facility with respect to
water effluents That is no water leaves the Mill site because the Mill has
no outfalls to public stormwater systems
no surface runoff to public stormwater systems
no discharges to publicly owned treatment works POTW5 and
no discharges to surface water bodies
The State of Utah issued Groundwater Discharge Permit No UGW3 70004 to DUSA on March
2005 As part of compliance with the Permit DUSA is required to submit Stormwater Best
Management Practices Plan BMPP to the Executive Secretary of the Division of Radiation
Control Utah Department of Environmental Quality This BMPP presents operational and
management practices to minimize or prevent spills of chemicals or hazardous materials which
could result in contaminated surface water effluents potentially impacting surface waters or
ground waters through runoff or discharge connections to stormwater or surface water drainage
routes Although the Mill by design cannot directly impact stormwater surface water or
groundwater the Mill implements these practices in good faith effort to minimize all sources of
pollution at the site
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
2.0 SCOPE
This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in
process operations laboratory operations and maintenance activities and minimize spread of
particulates from stockpiles and tailings management areas at the Mill Storage of ores and
alternate feeds on the ore pad and containment of tailings in the Mill tailings impoundment
system are not considered spills for the purposes of this BMPP
The Mill site was constructed with an overall grade and diversion ditch system designed to
channel all surface runoff including precipitation equivalent to Probable Maximum
PrecipitationlProbable Maximum Flood PMP/PMF storm event to the tailings management
system In addition Mill tailings all other process effluents all solid waste and debris except
used oil and recyclable materials and spilled materials that cannot be recovered for reuse are
transferred to one or more of the tailings cells in accordance with the Mills NRC license
conditions All of the process and laboratory building sinks sumps and floor drains are tied to
the transfer lines to the tailings impoundments site map of the Mill is provided in Figure
sketch of the site drainage basins is provided in Figure
As result unlike other industrial facilities whose spill management programs focus on
minimizing the introduction of chemical and solid waste and wastewater into the process sewers
and storm drains the Mill is permitted by NRC license to manage some spills via draining or
washdown to the process sewers and ultimately the tailings system However as good
environmental management practice the Mill attempts to minimize
the number and size of material spills and
the amount of unrecovered spilled material and washwater that enters the process sewers
after spill cleanup
Section 4.0 itemizes the practices in place at the Mill to meet these objectives
Requirements and methods for management recordkeeping and documentation of hazardous
material spills are addressed in the DUSA White Mesa Mill Spill Prevention Control and
Countermeasures SPCCPlan Revised February 2007 the Emergency Response Plan
ERP also revised in February 2007 and the housekeeping procedures incorporated in the
White Mesa Mill Standard Operating Procedures SOPs The SPCC plan and the ERP are
provided in their entirety in Appendices and respectively
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
3.0 RESPONSIBILITY
All Mill personnel are responsible for implementation of the practices in this BMPP DUSA
White Mesa Mill management is responsible for providing the facilities or equipment necessary
to implement the practices in this BMPP
The Mill Management Organization is presented in Figure The DUSA Corporate
Management Organization is presented in Figure
An updated spill prevention and control notification list is provided in Table
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.0 BEST MANAGEMENT PRACTICES
summary list and inventory of all liquid and solid materials managed at the Mill is provided in
Tables through
4.1 General Management Practices Applicable to All Areas
4.1.1 Keep Potential Pollutants from Contact with Soil and Surface Water
Store hazardous materials and other potential pollutants in appropriate containers
Label the containers
Keep the containers covered when not in use
4.1.2 Keep Potential Pollutants from Contact with Precipitation
Store bulk materials in covered tanks or drums
Store jars bottle or similar small containers in buildings or under covered areas
Replace or repair broken dumpsters and bins
Keep dumpster lids and large container covers closed when not in use to keep
precipitation out
4.1.3 Keep Paved Areas from Becoming Pollutant Sources
Sweep paved areas regularly and dispose of debris in the solid waste dumpsters or
tailings area as appropriate
4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the
Process and Reagent Storage Area
Diversion ditches drainage
channels and surface water control structures in and around
the Mill area will be inspected at least weekly in accordance with the regularly scheduled
inspections required by Groundwater Discharge Permit No UGW370004 and
Byproduct Materials License UT1 900479 Areas requiring maintenance or repair such
as excessive vegetative growth channel erosion or pooling of surface water runoff will
be report to site management and maintenance departments for necessary action to repair
damage or perform reconstruction in order for the control feature to perform as intended
Status of maintenance or repairs will be documented during follow up inspections and
additional action taken if necessary
4.1.5 Recycle Fluids Whenever Possible
When possible select automotive fluids solvents and cleaners that can be recycled or
reclaimed
When possible select consumable materials from suppliers who will reclaim empty
containers
Keep spent fluids in properly labeled covered containers until they are picked up for
recycle or transferred to the tailings area for disposal
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.2 Management Practices for Process and Laboratory Areas
4.2.1 Clean Up Spills Properly
Clean up spills with dry cleanup methods absorbents sweeping collection drums
instead of water whenever possible
Clean spills of stored reagents or other chemicals immediately after discovery
Groundwater Discharge Permit No UGW370004 Section I.D.8.c
Recover and re-use spilled material whenever possible
Keep supplies of rags sorbent materials such as cat litter spill collection drums and
personnel protective equipment PPE near the areas where they may be needed for
spill response
If spills must be washed down use the minimum amount of water needed for effective
cleanup
4.2.2 Protect Materials Stored Outdoors
If drummed feeds or products must be stored outdoors store them in covered or diked
areas when possible
If drummed chemicals must be stored outdoors store them in covered or diked areas
when possible
Make sure drums and containers stored outdoors are
in good condition and secured
against wind or leakage Place any damaged containers into an overpack drum or second
container
4.2.3 Water Management
When possible recycle and reuse water from flushing and pressure testing equipment
When possible wipe down the outsides of containers instead of rinsing them off in the
sink
When possible wipe down counters and work surfaces instead of hosing or rinsing them
off to sinks and drains
4.2.4 Materials Management
Purchase and inventory the smallest amount of laboratory reagent necessary
Do not stock more of reagent than will be used up before its expiration date
All new construction of reagent storage facilities will include secondary containment
which shall control and prevent any contact of spilled reagents or otherwise released
reagent or product with the ground surface Groundwater Discharge Permit No
UGW370004 Section I.D.3.e
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.3 Management Practices for Maintenance Activities
4.3.1 Keep Clean Dry Shop
Sweep or vacuum shop floors regularly
Designate specific areas indoors for parts cleaning and use cleaners and solvents only in
those areas
Clean up spills promptly Dont let minor spills spread
Keep supplies of rags collection containers and sorbent material near each work area
where they are needed
Store bulk fluids waste fluids and batteries in an area with secondary containment
double drum drip pan to capture leakage and contain spills
4.3.2 Manage Vehicle Fluids
Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as
possible Use drip pans or plastic tarps to prevent spillage and spread of fluids
Promptly contain and transfer drained fluids to appropriate storage area for reuse recycle
or disposal
Recycle automotive fluids if possible when their usefhl life is finished
4.3.3 Use Controls During Paint Removal
Use drop cloths and sheeting to prevent windborne contamination from paint chips and
sandblasting dust
Collect contain and transfer as soon as possible accumulated dusts and paint chips to
disposal location in the tailings area authorized to accept waste materials from
maintenance or construction activities
4.3.4 Use Controls During Paint Application and Cleanup
Mix and use the right amount of paint for the job Use up one container before opening
second one
Recycle or reuse leftover paint whenever possible
Never clean brushes or rinse or drain paint containers on the ground paved or unpaved
Clean brushes and containers only at sinks and stations that drain to the process sewer to
the tailings system
Paint out brushes to the extent possible before water washing water-based paint or
solvent rinsing oil-based paint
Filter and reuse thinners and solvent whenever possible Contain solids and unusable
excess liquids for transfer to the tailings area
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.4 Management Practices for Ore Pad Tailings Area and Heavy Equipment
Detailed instructions for ore unloading dust suppression and tailings management are provided
in the Mill SOPs
4.4.1 Wash Down Vehicles and Equipment in Proper Areas
Wash down trucks trailers and other heavy equipment only in areas designated for this
purpose such as washdown pad areas and the truck wash station
At the truck wash station make sure the water collection and recycling system is working
before turning on water sprays
4.4.2 Manage Stockpiles to Prevent Windborne Contamination
Water spray the ore pad and unpaved areas at appropriate frequency in accordance with
Mill SOPs
Water spray stockpiles as required by opacity standards or weather conditions
Dont over-water Keep surfaces moist but minimize runoff water
4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources
Schedule excavation grading and other eartbmoving activities when extreme dryness and
high winds will not be factor to prevent the need for excessive dust suppression
Remove existing vegetation only when absolutely necessary
Seed or plant temporary vegetation for erosion control on slopes
Page
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Home Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.166
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Home Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE
REAGENT YARD LIST
REAGENtt2J JAN1TVYLBS NUMBEROFT cApACrry
STGMGETANKS .GALLdN
ADOGEN 2382 6120
ADVANTAGE 1O1M 2475
AMERSJTE2
AMINE 2384 19440
AMMONIUM SULFATE BULK 54000
AMMONIUM SULFATE BAGS 4300
ANHYDROUS AMMONIA 107920 31409
CHEMFAC 100 12800
CLARIFLOC N-1O1P 3000
DECYLALCOHOL 45430
DIESEL FUEL 250
6000
FLOCCULENT M1O11N 30550
FLOCCULENT M1302C 3550
GRINDING BALLS 48290
ISODECANOL 45430
KEROSENE 1344 10152
MACKANATE 3150
MILLSPERSE 802 1410
NALCO 2458
NALCO 8815
PERCOL 351 1500
PERCOL 406 13950
PERCOL 745
POLOX 10360
POLYHALL YCF
PROPANE 30000
SALT BAGS 39280
SALT BULK
SODA ASH BAGS 39280
SODA ASH BULK 84100 16921
8530
SODIUM CHLORATE 101128 17700
10500
SODIUM HYDROXIDE 19904
SULFURIC ACID 4801440 1600000
269160
UNLEADED GASOLINE 3000
USED OIL 5000
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
Chemical in Lab RQ2 Quantity In Stock
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
68 kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
Chemical in Volatiles and RQ2 Quantity In Stock
Flammables Lockers ABC
Chloroform 4.54 kg
Formaldehyde 45.4 kg IL of 37%solution
Nitrobenzene 454 kg 12L
Toluene 454 kg 12
Chemical in Acid Shed RQ2 Quantity In Stock
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Pad 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
.___________0T14INV
STORAG
ttMPOUNa
Acetic Acid Glacial 1000 lbs gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 lbs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs kg 11 lbs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
REAGENT RQ2 QUANTITY IN
REAGENT YARD
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfioc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
PRODUCT QUANTITY IN
WAREHOUSE
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
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Mill Site Drainage Basins
Figure
White Mesa Mill
Mill Management Organization Chart
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APPENDICES
APPENDIX
WRITE MESA MIELL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
FOR CHEMICALS AND PETROLEUM PRODUCTS
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Bland ing Utah 84511
February 2007
Prepared by
Denison Mines USA Corp
1050 7th Street Suite 950
Denver Colorado 80265
TABLE OF CONTENTS
SECTION PAGE
1.1 Objective
.2 Responsibilities
1.3 Drainage Basins Pathways and Diversions
1.4 Description of Basins
1.4.1 Basin Al
1.4.2 Basin A2
1.4.3 Basin Bl
1.4.4 Basin B2
1.4.5 Basin B3
1.4.6 Basin
1.4.7 Basin
1.4.8 Basin
1.5 Potential Chemical Spill Sources And Spill Containment
1.5.1 ReagentTanks
1.5.2 Ammonia
1.5.3 Ammonium Meta Vanadate
1.5.4 Caustic Storage Sodium Hydroxide
1.5.5 Sodium Carbonate
1.5.6 Sodium Chlorate
1.5.7 Sulfuric Acid
1.5.8 Vanadium Pentoxide
1.5.9 Kerosene Organic
1.6.0 Used/Waste Oil
SECTION PAGE
1.6.1 Propane
1.7 Potential Petroleum Sources And Containment
1.7.1 Petroleum Storage Tanks
1.7.1.1 Diesel
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.2 Unleaded Gasoline
1.7.2.3 Pump Station
1.7.2.4 Truck Unloading
1.8 Spill Discovery And Remedial Action
1.9 Spill Incident Notifications
1.9.1 External Notification
1.9.2 Internal Notification 11
1.10 Records And Reports 12
1.11 Personnel Training And Spill Prevention Procedures 12
1.11.1 Training Records 12
1.11.2 Monitoring Reports 13
1.12 Revision 13
1.13 Summary 13
1.14 Mill Manager Approval 14
1.15 Certification by Registered Professional Engineer 14
LIST OF TABLES
Table 1.0 Mill Organization Chart
Table 2.0 Reagent Tank List
Table 3.0 Laboratory Chemical Inventory List
Table 4.0 Reagent Yard/Small Quantity Chemicals List
Table 5.0 Reagent Yard/Bulk Chemicals List
Table 6.0 Petroleum Products and Solvents List
LIST OF FIGURES
Figure Mill Site Layout
Figure Mill Site Drainage Basins
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS
1.1 OBJECTIVE
The objective of the Spill Prevention Control and Countermeasures SPCC
Plan is to serve as site-specific guideline for the prevention of and response to
chemical and petroleum spills and as guidance document for compliance with
Groundwater Discharge Permit No UGW370004 The plan outlines spill
potentials containment areas and drainage characteristics of the White Mesa
Mill site The plan addresses chemical spill prevention spill potentials spill
discovery and spill notification procedures The Oil Pollution Prevention Sections
of the Clean Water Act 40 CFR 112 to 117 also referred to as the Spill
Prevention Control and Countermeasures SPCCrules establish
requirements that apply to facilities which could reasonably be expected to
discharge oil in quantities that may be harmful as described in that Act into or
upon the navigable waters of the United States or that may affect natural
resources of the United States Section 112 states that the Act is not applicable
to facilities that are not subject to the authority of the Environmental
Protection Agency EPA for one of the following reasons
Due to its location the facility could not reasonably be expected to
discharge oil into navigable waters of or impact natural resources of the
U.S or
The facility is subject to authority of the Department of Transportation as
defined in Memorandum of Understanding MOU between the
Secretary of Transportation and the EPA Administrator or
The facility does not exceed either the underground or the above ground
storage capacity 42000 gallons and 1320 gallons respectively
prescribed in the rules
The Mill could not reasonably be expected as described in the SPCC regulation
to discharge oil into the navigable waters or impact natural resources of the
U.S The Mill site was constructed with an overall grade and diversion ditch
system designed to channel the non-recovered portion of any material spill to the
tailings management system Hence it is not reasonable to expect that surface
spills will ever reach navigable waters or natural resources of the U.S or Utah
Therefore the SPCC reporting requirements in the Clean Water Act are not
applicable to the Mill However as good environmental management practice
the Mill has implemented the spill management program described in this
document which is consistent with the intent of the Clean Water Act to the
extent practicable Although the Mill by design cannot directly impact navigable
waters of the U.S and as result spills that may occur but are retained within
the site would not be reportable the Mill implements these practices in good
faith effort to minimize all potential sources of pollution at the site
Storage of ores and alternate feeds on the ore pad and containment of tailings
in the Mill tailings impoundment system are not considered spills for the
purposes of this SPCC
Ammonia is the only chemical that has the potential to leave the site and would
do so as vapor
Figure Site Layout Map shows map of the mill site including the locations of
the chemical tanks on-site Figure shows the basins and drainage ditch areas
for the mill site Table 1.0 is an organization chart for Mill operations Table 2.0
lists the reagent tanks and their respective capacities Table 3.0 lists the
laboratory chemicals their amounts and their reportable quantities Table 4.0
lists the operations chemicals Table 5.0 lists the chemicals in the reagent yard
their amounts and their reportable quantities Table 6.0 lists the petroleum
products and solvents on site
1.2 RESPONSIBILITIES
Person in charge of facility responsible for spill prevention
Mr Richard Bartlett Interim Mill Manager
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 459-2495 home
Person in charge of follow-up spill record keeping and/or reporting
Mr David Turk Department Head Health Safety and Environmental
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 678-7802 home
Refer to Section 1.9 Spill Incident Notification for list of company personnel
to be notified in case of spill In addition an organizational chart is provided
in Table 1.0
1.3 DRAINAGE BASINS PATHWAYS AND DIVERSIONS
The main drainage pathways are illustrated in Figure The map shows
drainage basin boundaries flow paths constructed diversion ditches tailings
cells the spillway between Cell and dikes berms and other relevant
features The White Mesa Mill is zero discharge facility for process liquid
wastes The mill area has been designed to ensure that all spills or leaks
from tanks will drain toward the lined tailings cells
The tailings cells in turn are operated with sufficient freeboard minimum of
three feet to withstand 100%of the PMP Probable Maximum Precipitation
This allows for maximum of 10 inches of rain at any given time
1.4 DESCRIPTION OF BASINS
Precipitation and unexpected spills on the mill property are contained within
their respective drainage basins Runoff would ultimately drain into one of
the three lined tailings cells
1.4.1 Basin Al
Basin Al is north of Cell 1-I and Diversion Ditch No The basin
contains 23 acres all of which drain into Westwater Creek This area is
not affected by mill operations
14.2 Basin A2
Basin A2 contains all of Cell 1-I including an area south of the Diversion
Ditch No The basin covers 84 acres Any runoff from this basin
would be contained within Cell 1-I
1.4.3 Basin BI
Basin Bl is north of the mill property and is not affected by mill
operations The basin contains 45.4 tributary acres Runoff from this
basin drains into flood retention area by flowing through Diversion Ditch
No Diversion Ditch No drains into Westwater Creek
1.4.4 Basin B2
Basin B2 is northeast of the mill and contains only 2.6 acres Runoff from
this basin would drain into Diversion Ditch No Diversion Ditch No
ultimately drains into Diversion Ditch No This basin is not affected by
mill operations
1.4.5 Basin B3
Basin B3 contains most of the mill area buildings ore stockpiles process
storage tanks retention ponds spill containment structures pipelines
and roadways The normal direction of flow in this basin is from the
northwest to the southwest Any runoff from this basin would drain into
Cell 1-I The basin contains 64 acres This basin has sufficient
freeboard to withstand 100%of the PMP Probable Maximum
Precipitation This allows 10 inches of rain for any given storm event
1.4.6 Basin
Basin contains all of Cell The basin consists of 80.7 acres This
basin contains earth stockpiles and the heavy equipment shop The
direction of flow in this basin is to the southwest All runoff in this basin
would be channeled along the southern edge of the basin Runoff would
then flow into Cell via the spillway from Cell to Cell
1.4.7 Basin
Basin contains all of Cell This basin consists of 78.3 acres including
portion of the slopes of the topsoil stockpile and random stockpile The
basin contains all flows including those caused by the PMF
1.4.8 Basin
Basin contains Cell 4A and consists of 43.3 acres All anticipated flows
including those caused by the PMF will be contained within the basin and
will flow directly into Cell 4A
1.5 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL
CONTAINMENT
This section details potential sources of chemical spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States Reportable
Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act
It is not expected that any spill would reach navigable waters of the United States
However if spill of volume listed below occurs and remains on the mill site which is
the more likely scenario then management is to be notified so that proper internal
evaluations of the spill are made
1.5.1 Reagent Tanks Tank list included in Table 2.0
1.5.2 Ammonia
The ammonia storage tanks consist of two tanks with capacity of
31409 gallons each The tanks are located southeast of the Mill building
Daily monitoring of the tanks for leaks and routine integrity inspections will be
conducted to minimize the hazard associated with ammonia The reportable
quantity for an ammonia spill is gallons
Ammonia spills should be treated as gaseous Ammonia vapors will be
monitored closely to minimize the hazard associated with inhalation If
vapors are detected efforts will be made to stop or repair the leak
expeditiously Ammonia is the only chemical as vapor that has the
potential to leave the site
1.5.3 Ammonia Meta Vanadate
Ammonia meta vanadate is present in the SX building as the process
solutions move through the circuit to produce the vanadium end product
But the primary focus will be on the transportation of this chemical The
reportable quantity for an ammonia meta vanadate spill is 1000 pounds
1.5.4 Caustic Storage Sodium Hydroxide
The caustic storage tank is located on splash pad on the northwest corner
of the SX building The tank has capacity of 19904 gallons The tank
supports are mounted on concrete curbed catchment pad that directs spills
into the sand filter sump in the northwest corner of the SX building The
reportable quantity for sodium hydroxide spill is 85 gallons
1.5.5 Sodium Carbonate Soda Ash
The soda ash solution tank has capacity of 16921 gallons and is located in
the northeast corner of the SX building The smaller soda ash shift tank has
capacity of 8530 gallons and is located in the SX building Spills will be
diverted into the boiler area and would ultimately drain into Cell 1-I There is
no reportable quantity associated with sodium carbonate spill
1.5.6 Sodium Chlorate
Sodium chlorate tanks consist of two fiberglass tanks located within dike
east of the SX building The larger tank is used for dilution purposes and has
maximum capacity of 17700 gallons The smaller tank serves as
storage tank and has capacity of 10500 gallons Daily monitoring of the
tanks for leaks and integrity inspections will be conducted to minimize the
hazard associated with sodium chlorate
Sodium chlorate that has dried and solidified becomes even more of safety
hazard due to its extremely flammable nature The reportable quantity for
sodium chlorate spill is 400 gallons
1.5.7 Sulfuric Acid
The sulfuric acid storage tanks consist of one large tank with the capacity of
16000000 gallons and two smaller tanks with capacities of 269160 gallons
each
The large tank is located in the northwest corner of mill area basin B3 and is
primarily used for acid storage and unloading The tank support for the large
tank is on mound above depression which would contain significant
spill All flows resulting would be channeled to Cell 1-I The tank is equipped
with high level audible alarm which sounds prior to tank overflows
concrete spill catchment with sump in the back provides added
containment around the base of the tank However the catchment basin
would not be able to handle major tank failure such as tank rupture The
resulting overflow would flow towards Cell 1-I
The two smaller storage tanks are located within an equal volume spill
containment dike east of the mill building The tanks are not presently in
use but are equipped with high level audible alarms
The reportable quantity for sulfuric acid spill is 65 gallons 1000 pounds
1.5.8 Vanadium Pentoxide
Vanadium pentoxide is produced when vanadium is processed through the
drying and fusing circuits and is not present in the vanadium circuit until after
the deammoniator Efforts will be made to minimize leaks or line breaks that
may occur in processes in the circuit that contain vanadium pentoxide
Special care will be taken in the transportation of this chemical The
reportable quantity for vanadium pentoxide spill is 1000 pounds
1.5.9 Kerosene Organic
The kerosene storage area is located in the central mill yard and has
combined capacity of 10152 gallons in three tanks Any overflow from these
three tanks would flow around the south side of the SX building and then into
Cell 1-I These tanks have drain valves which remain locked unless
personnel are supervising draining operations The reportable quantity for
kerosene spill is 100 gallons
1.6.0 Used Waste Oil
Used Waste oil for parts washing is located north of the maintenance shop
in tank and has capacity of 5000 gallons The tank is contained within
concrete containment system Ultimate disposal of the used oil is to an EPA
permitted oil recycler Any oil escaping the concrete containment system will
be cleaned up Soil contaminated with used oil will be excavated and
disposed of in Cell
1.6.1 Propane
The propane tank is located in the northwest corner
of the mill yard and has
capacity of 30000 gallons Daily monitoring of the tank for leaks and
integrity inspections will be conducted to minimize potential hazards
associated with propane leaks Propane leaks will be reported immediately
There is no reportable quantity associated with propane spill
1.7 POTENTIAL PETROLEUM SPILL SOURCES AND
CONTAINMENT
This section details potential sources of petroleum spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States It is not
expected that any spill would reach navigable waters of the United States However if
spill of volume listed below occurs and remains on the mill site which is the more
likely scenario then management is to be notified so that proper internal evaluations of
the spill are made
1.7.1 Petroleum Tanks
1.7.1.1 Diesel
Two diesel storage tanks are located north of the mill building The tanks
have capacities of 250 gallons each One of the diesel tanks is for the
emergency generator The other tank is located in the pumphouse on an
elevated stand Spillage from either tank would ultimately flow into Cell 1-I
The reportable quantity for diesel spill is 100 gallons
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.1 Diesel
The diesel tank is located on the east boundary of Basin B3 and has
capacity of 6000 gallons The tank is contained within concrete catchment
pad The reportable quantity for diesel spill is 100 gallons
1.7.2.2 Unleaded Gasoline
The unleaded gasoline tank is located next to the diesel tank The unleaded
gasoline tank has capacity of 3000 gallons and is contained within the
same containment system as the diesel tank The reportable quantity for an
unleaded gasoline spill is 100 gallons
1.7.2.3 Pump Station
Both the diesel and the unleaded gasoline tanks will be used for refueling
company vehicles used around the mill site The pump station is equipped
with an emergency shut-off device in case of overflow during fueling In
addition the station is also equipped with piston leak detector and
emergency vent Check valves are present along
with tank monitor
console with leak detection system The catchment is able to handle
complete failure of one tank However if both tanks failed the concrete
catchment pad would not be able to contain the spill In this case
temporary berm would need to be constructed Absorbent diapers or floor
sweep would be used in an effort to limit and contain the spill The soil would
be cleaned up and placed in the authorized disposal area in Cell
1.7 2.4 Truck Unloading
In the event of truck accident resulting in an overturned vehicle in the mill
area proper reporting and containment procedures will be followed when
warranted such as when oil or diesel fuel is spilled Proper clean-up
procedures will be followed to minimize or limit the spill The spill may be
temporarily bermed or localized with absorbent compounds Any soils
contaminated with diesel fuel or oil will be cleaned up and placed in the
authorized disposal area in Cell
1.8 SPILL DISCOVERY AND REMEDIAL ACTION
Once chemical or petroleum spill has been detected it is important to take
measures to limit additional spillage and contain the spill that has already
occurred Chemical or petroleum spills will be handled as follows
The Shift Foreman will direct efforts to shut down systems if
possible to limit further release
The Shift Foreman will also secure help if operators are requiring
additional assistance to contain the spill
The Shift Foreman is also obligated to initiate reporting procedures
Once control measures have begun and personal danger is
minimized the Shift Foreman will notify the Production
Superintendent Maintenance Superintendent or Mill Manager
The Production or Maintenance Superintendent will notify the Mill
Manager who in turn will notify the Environmental Health and Safety
Manager
The Mill Manager will assess the spill and related damage and direct
remedial actions The corrective actions may include repairs clean
up disposal and company notifications Government notifications
may be necessary in some cases
If major spill continues uncontrolled these alternatives will be considered
Construct soil dikes or pit using heavy equipment
Construct diversion channel into an existing pond
Start pumping the spill into an existing tank or pond
Plan further clean-up and decontamination measures
1.9 SPILL INCIDENT NOTIFICATION
1.9.1 External Notification
As stated in Section 1.1 spills are not expected to reach navigable waters of
the United States If spill of reportable quantity occurs then mill and
corporate management must be notified and they will evaluate whether or not
the following agencies must be notified
EPA National Response Center 1-800-424-8802
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah 801/538-7200
Water Quality Division 801/538-6146
In case of tailings dam failure contact the following agencies
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah Natural Resources 801/538-7200
1.9.2 Internal Notification
Internal reporting requirements for incidents spills and significant spills are
as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions and accidents
Government investigations information requests or enforcement
actions
Private actions or claims corporate or employee
Deviations from corporate policies or government requirements by
management
Which have or could result in the following
Death serious injury or adverse health effects
Property damage exceeding $1000000
10
Government investigation or enforcement action which limits
operations or assesses penalties of $100000 or more
Publicity resulted or anticipated
Substantial media coverage
Report At The Beginning Of The Next Day
Event Criteria
Was reported to government agency as required by law
Worker employee or contractor recordable injury or illness associated
with release
Community impact-reported or awareness
Publicity resulted or anticipated
Release exceeding the reportable quantities listed in Section 1.5 for
each specific process material waste or by-product
In the event of spill of reportable quantity the Mill Manager is required to
call the Corporate Environmental Manager or the President and Chief
Executive Officer The individual first discovering the spill will report it to the
Shift Foreman Production Superintendent or Maintenance Superintendent
who will in turn ensure that the Mill Manager is notified The Environmental
Health and Safety Manager will also be contacted by the Mill Manager
Name Title Home Phone
Mill Personnel
Richard Bartlett Interim Mill Manager 435 678-2495
Wade Hancock Maintenance Foreman 435 678-2753
David Turk Environmental Health and
Safety Manager 435 678-7802
N/A Production Superintendent
N/A Maintenance Foreman
Scot Christensen Mill Shift Foreman 435 678-2015
Corporate Personnel
Ronald Hochstein President and Chief Operating Officer 604 377-1167
David Frydenlund Vice President and General Counsel 303 221-0098
In the event the next person in the chain-of-command cannot be reached
then proceed up the chain-of-command to the next level Table 1.0 shows the
organizational chart for the mill site
11
1.10 RECORDS AND REPORTS
The following reports and records are to be maintained in Central Files by the
Environmental Health and Safety Manager for inspection and review for
minimum of three years
Record of site monitoring inspections
Daily Tailings Inspection Data
Weekly Tailings Inspection and Survey
Monthly Tailings Inspection Pipeline thickness
Quarterly Tailings Inspection
Tank to soil potential measurements
Annual bulk oil and fuel tank visual inspections
Tank and pipeline thickness tests
Quarterly and annual PCB transformer inspections if transformer
contains PCBs
Tank supports and foundation inspections
Spill Incident Reports
Latest revision of SPCC plan
1.11 PERSONNEL TRAINING AND SPILL PREVENTION
PROCEDURES
All new employees are instructed on spills at the time they are employed and
trained They are briefed on chemical and petroleum spill prevention and
control They are informed that leaks in piping valves and sudden
discharges from tanks should be reported immediately Abnormal flows from
ditches or impoundments are of immediate concern In addition safety
meeting is presented annually by the Environmental Health and Safety
Manager to review the SPCC plan
1.11.1 Training Records
Employee training records on chemical and petroleum spill prevention are
maintained in the general safety training files
1.11.2 Monitoring Reports
Shift logs shall provide checklist for inspection items
12
1.12 REVISION
This procedure is to be reviewed by the mill staff and registered
professional engineer at least onc eve ry th ree years and updated when
circumstances warrant revision
1.13 Summary
Below is table listing the specific reportable quantities associated with the
major chemical and petroleum products on-site
CHEMICAL REPORTABLE
QUANTITY RQ
AMMONIA 100 POUNDS
AMV 1000 POUNDS
SODIUM
HYDROXIDE
1000 POUNDS
SODA ASH No Reportable
Quantity
SODIUM
CHLORATE
400 GALLONS
SULFURIC ACID 1000 POUNDS
VANADIUM
PENTOXIDE
1000 POUNDS
KEROSENE 100 GALLONS
OIL No Reportable
Quantity
PROPANE No Reportable
Quantity
DIESEL
UNLEADED
FUEL
100 GALLONS
13
1.14 MILL MANAGER APPROVAL
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with the Standard Operating Procedures
currently in effect
4/Car
Richard Bartlett
Interim Mill Manager
1.15 CERTIFICATION BY
REGISTERED PROFESSIONAL ENGINEER
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with good engineering practices
Harold Roberts
Registered Professional Engineer
State of Utah No 165838
14
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Home Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.166
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Home Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE 2.0
REAGENT TANK LIST
QUANTITY REAGENT CAPACITY GAL
DIESEL 250
KEROSENE 10152
USED/WASTE OIL 5000
DIESEL 6000
UNLEADED 3000
PROPANE 30000
AMMONIA 31409
SODIUM HYDROXIDE 19904
SODA ASH SOLUTION 16921
SODA ASH SHIFT 8530
SODIUM CHLORATE 17700
SODIUM CHLORATE 10500
SULFURIC ACID 1600000
SULFURIC ACID 269160
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
Jj
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
6.8 kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
tIfethia11nVlatiIØiandi QUntiW1nSbŁkT
FlammablestockerstBCL
--
--
-t
r-c-
Chloroform 4.54 kg
Formaldeh1e 45.4 kg IL of 37%solution
Nitrobenzene 454 kg 12L
Toluene 454 kg 12L
RyH QUahtitWitStokH
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
tHEMICAtI ItJJIT fiQZIt QIJANTIfiN
STCRAE
-T7-6OMROUND
Acetic Acid Glacial 1000 lbs gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 Ibs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs 5kg IlIbs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal 5kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
Sulfuric Acid
Floc 301
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
Hype nbc 102
Ammonia East Tank
Ammonia West Tank
Kerosene
Salt Bags
Ammonium Hydrogendifluonide
Soda Ash Dense Bag
Phosphoric Acid
Polyox
illsperse
Nalco TX760
Nalco 7200
Tributyl phosphate
Distillates
Diesel
Gasoline
Alamine 336 drums
Fboc 109
Floc 208
Floc 904
Hyperfloc 624
Salt Bulk solids
Salt Bulk solutions
Caustic Soda
Ammonium Sulfate
Sodium Chlorate
Alamine 335 Bulk
Alamine 310 Bulk
lsodecanol
Vanadium Pentoxide3
Yellowcake3
Ammonia Meta Vanadate
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
REAGENT RQ2 QUANTITYIN
REAGENTXARD
0b0 lbs
None
None
100 lbs
100 lbs
100 gal
None
None
None
5000 lbs
None
None
None
None
None
None
100 gal
100 gal
None
None
None
None
None
None
None
1000 lbs
None
None
None
None
None
1000 lbs
None
1000 lbs
9000000 lbs
1200 lbs
1500 lbs
lbs
105000 lbs
500 gal
2000 lbs
20450 lbs
lbs
6300 lbs
490 lbs
1410 lbs
barrels
1590 lbs
9450 lbs
100 gal
Approx 3300 gal
Approx 6000 gal
lbs
lbs
lbs
lbs
lbs
lbs
lbs
lbs
lbs
20000 lbs
lbs
lbs
lbs
30000 lbs
100000 lbs
lbs
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distfllates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT -.QUANTIfl4N
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
GR
I
Z
Z
L
Y
DE
c
O
N
T
A
M
I
N
A
T
I
O
N
PA
D
DIE
S
E
L
SA
M
P
L
E
PL
A
N
TLi
rt
_
2r
se
n
t
pi
vs
e
t
Figure
White Mesa Mill
Mill Site Drainage Basins
APPENDIX
WRITE MESA MILL
EMERGENCY RESPONSE PLAN
EMERGENCY RESPONSE PLAN
REVISION 1.1
Denison Mines USA Corp
nn..4.aa--iaiiVVIIIICIVICScLIVEIlI
Blanding Utah
April14 1986
REVISED
February 16 2007
Distribution List
Ron Hochstein
Rich Bartlett
David Turk
Michael Spillman
Mill Shift Foremen
Blanding Fire Department
San Juan County EMS Coordinator
State of Utah Department of Radiation Control
Revision Date January 16 2006
TABLE OF CONTENTS
Page
Number
1.0 Introduction .1
2.0 White Mesa Mill Background .1
3.0 Plan Objectives
4.0 Description of Facilities
4.1 Fire Water Supply and Alarm Systems
4.2 Office Building and Laboratory
4.3 Solvent Extraction Building
4.4 Mill Building
4.5 Maintenance Shop/Warehouse/Change Room Building
4.6 Reagent and Fuel Storage
4.7 Boiler House
4.8 Sample Plant
5.0 Organization and Responsibilities
5.1 Mill Manager/Incident Commander
5.2 Operations Superintendent
5.3 Radiation Safety Officer/Fire Chief
5.4 Maintenance Supervisor
5.5 Laboratory Supervisor
5.6 Shift Foremen
5.7 Scale House Personnel
5.8 Emergency Response Teams
6.0 Specific Emergencies 10
6.1 Fire 10
6.2 Chemical or Gas Release 10
6.3 Earthquake 10
6.4 Terrorist/Bomb Threat 10
6.5 Tailings Dam Break and Major Floods 10
7.0 Evacuation Procedure 11
7.1 Notification 11
7.2 Assembly 11
7.3 Specific Procedures for Operations Personnel 11
8.0 Off-Site Emergency Equipment/Personnel Release 11
9.0 Emergency Equipment 12
9.1 Fire Hose 12
9.2 Self Contained Breathing Apparatus
12
9.3 Spill Clean-up Equipment 12
9.4 Fire Fighting PPE 12
10.0 Emergency Transportation 13
11.0 Emergency Evacuation Drills 13
EXHIBITS
Emergency Notification List E-
Internal Notifications E-2
Site Layout Map E-3
Main Shut-off Valves E-4
APPENDICES
Emergency Procedure Response to Fire A-I
Emergency Procedure Response to Chemical or Gas Release A-2
Emergency Evacuation Procedure A-3
FIGURES
Fire System Schematic F-I
i-i
INTERNATIONAL URANIUM USA CORPORATION
Rev No RI
Date Sept 29 2005 WRITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
INTRODUCTION
This Emergency Response Plan is written not only to comply with Federal State and local
regulations but even more importantly to reduce the risk to our employees and that of the
community in regards to Health Safety and Environmental Emergencies
This plan includes the following
evaluation of the potential risks for fire explosions gas releases chemical spills and
floods including tailings dam failure
specific emergency programs for each potential event
definition of administrative response actions and
definition of the emergency response contacts both internal and external
The White Mesa Mill the Mill operates under the following regulatory agencies
Utah State Department of Environmental Quality Division of Radiation Control
Mine Safety and Health Administration
Environmental Protection Agency
Utah State Department of Environmental Quality Division of Air Quality and
Utah State Division of Natural Resources Bureau of Dam Safety
WIIITE MESA MILL OVERVIEW
The Mill processes conventional uranium or uranium/vanadium ores to recover uranium and
vanadium In addition to the processing of conventional ores the Mill also processes alternate
feed materials using similar process steps and chemicals The conventional ore is stored on the
Ore Pad shown in Exhibit Alternate feed materials are also stored on the Ore Pad and may
be stored in bulk form lined burrito bags liners or drums The descriptions of each alternate
feed material are maintained by the Mills Radiation Safety Officer
The Mill utilizes semi-autogenous grind circuit followed by hot sulfuric acid leach and
solvent extraction process to extract uranium and vanadium from ores using large amounts of
sulfuric acid sodium chlorate kerosene amines ammonia and caustic soda in the process The
reagent storage tank locations are described in further detail in Section 4.6
Emissions from the Mill process are in the form of air emissions from exhaust stacks and
solid/liquid tailings which are stored in the Mills tailings cells located west/southwest of the
main Mill building The major exhaust stack parameters are shown in the following table
Description
Height
ft from surface
Diameter
inches
Estimated Flow Rate
cfln
Leach Exhaust l00 36 13700
Yellow Cake Drying
stacks
--85 18 4000 per stack
Vanadium Roasting
Fusion
85 38 4100
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There are also smaller exhaust stacks associated with the Laboratory in the Mill Administration
building and the boiler exhaust stack
The Mills tailings cells are comprised of four below grade engineered cells Cell 1-I and
4A Liquids are stored in Cell 1-I and Cell the active tailings cell The liquid in the tailings
cells is very acidic In addition to the tailings cells there is also an emergency lined catchment
basin west of the Mill building Solutions in this basin or the tailings cells should not be used to
fight fires in the Mill facility
The products of the Mill include ammonium metavanadate AMV vanadium pregnant liquor
VPL vanadium pentoxide V205 and yellowcake or uranium concentrate U3O8 The V205
and U308 products are packaged in steel drums for shipment The AMY is packaged in either
steel drums or super-saks while the VPL is sold in liquid form in bulk
Master files containing Material Safety Data Sheets for all materials in use at the Mill are
maintained at the Safety Office Mill Maintenance Office Mill Laboratory and Mill Central
Control Room Copies are also on file at the Blanding Clinic Doctors Offices Blanding Fire
House and Office of the San Juan County Emergency Medical Coordinator
The nearest residence to the Mill is approximately one mile to the north of the Mill the next is
residence approximately two miles north of the Mill followed by the community of White Mesa
about 3.5 miles to the south The City of Blanding is located approximately miles to the
northeast
The Mill site is near Utah State Highway 191 and can be accessed by paved access road from
the highway to the Mill facilities
PLAN OBJECTIVES
The primary objectives of this plan are
To save lives prevent injuries prevent panic and minimize property/environmental
damage to the lowest possible level
To evacuate and account for all people in the area including visitors truck drivers
contractors etc
To provide assembly areas that are as safe as possible and which can be reached without
traveling through hazardous area Assembly areas will be properly manned to deal with
sick or injured persons and provisions will be made to evacuate those persons to proper
shelter
To make adequately trained personnel available to cope with rescue and recovery
operations as directed by the Incident Commander
DESCRIPTION OF FACILITIES
The Mill facilities are shown on the Site Layout Map included as Exhibit
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INTERNATIONAL URANIUM USA CORPORATION
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4.1 Fire Water Supply and Alarm Systems
4.1.1 Fire Water Supply
The fire water supply facilities include
400000 gallon Storage Tank of which 250000 gallons are reserved for fire emergencies
Centrifugal diesel driven pump rated at 2000 gpm at 100 psi This pump starts
automatically when the pressure in the fire main drops below 100 psi See Figure Fire
System Schematic
When more water is needed for an emergency an additional source is the Recapture Reservoir
supply pipeline which can be utilized in emergencies at rate of about 1200 gpm
4.1.2 Alarm System
The alarm systems include the following
public address system
hand held radios
siren
4.2 Office Building and Laboratory
4.2.1 Office Building
The office building approximately 10000 square feet contains the administration offices
radiation health and safety offices and the Mill laboratory The central file vault and the main
computer system are also in this building The ambulance is kept on the west side of the office
building near the safety office entrance
4.2.2 Laboratory
The laboratory facilities contain the following
three flammable cabinets keys required
chemical storage room south of main lab
six fume hoods hoods 12 and are in the center of the laboratory and hoods and
are along the west wall Hoods and are no longer in service Hoods and are on
the west side and are on the east side of the center cluster of hoods with being in
front Only hoods and may be used for perchloric acid
outside laboratory chemical storage north of office building key required
perchloric acid storage vault located underground west of office building key required
wide variety of chemicals in small quantities are located in the laboratory These chemicals
range from acids to bases along with flammable metal compounds and peroxide forming
compounds Oxidizers and organic chemicals which have strong potential of producing
harmful vapors if the containers are damaged to the point that the chemicals are exposed are
stored in storage room in the laboratory There are no acids stored in this storage room The
acids including but not limited to sulfuric nitric acetic perchloric phosphoric and hydrochloric
acids are stored in the main laboratory area in 2.5 liter or 500-mi bottles MSDS books for all
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chemicals in the laboratory are located in the Laboratory Safety Department Mill Maintenance
office and Mill Central Control room
4.2.3 Electrical
Electrical transfonners and electrical switches are located in the laboratory at the east end of the
chemical storage room
4.2.4 Fire Protection System
The fire protection systems in the office building and laboratory include
fire hose station located on the east end of the office building The station includes two
sets of turnout gear two SCBA units and Incident Commander materials
automatic wet sprinlder system which is actuated at 212
portable dry chemical extinguishers strategically located throughout the building
4.3 Solvent Extraction Building
The solvent extraction SX building approximately 21000 square feet houses the uranium and
vanadium solvent extraction circuits and the ELUEX circuit The SX circuits may contain up to
200000 gallons kerosene 757000 liters which has flash point of 185
Associated equipment in the SX building includes temporary boiler located at the southwest
end of the SX building which maintains the temperature for the fire system
Chemicals which may be encountered in the SX building include
Kerosene
Caustic Soda
Anhydrous Ammonia
Sulthric Acid
Salt Brine
Soda Ash
Ammonium Sulfate
Amines
Alcohol
Sodium Chlorate
Sodium Vanadate
Propane
The VPL product is stored in the SX building
4.3.1 Electrical
All electrical switches are located outside in the MCC room north of the SX building The main
control panel for all of the equipment is located in the Central Control Room in the main Mill
building
4.3.2 Fire Protection System
The SX building fire protection systems include
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wet AFFF foam sprinider system with heat actuated sprinkler heads that release at
12F
portable dry chemical extinguishers strategically located throughout the building
For fire hydrant and hose cabinet locations in the SX building refer to the Fire System Schematic
included as Figure in this Plan
4.4 MIII Building
The mill building approximately 22000 square feet contains process equipment related to
grind leach counter current decantation precipitation drying and packaging of uranium and
vanadium products
Chemicals which may be encountered in the mill building include
Caustic Soda
Anhydrous Ammonia
Sulfuric Acid
Soda Ash
Ammonium Sulfate
Sodium Chlorate
Sodium Vanadate
Propane
The finished products which are contained in the mill building include AMY V7O5 and U3O3 or
yellowcake
4.4.1 Electrical
The main electrical switch gear is located west of the SAG mill on the ground floor in the north
west corner of the mill building Circuit control panels are located in the SAG mill control room
the central control room the vanadium roaster control room and the AMY area
4.4.2 Fire Protection System
The main mill building fire protection systems include
portable dry chemical extinguishers strategically located throughout the building
water hoses throughout the building
For fire hydrant and hose cabinet locations in the Mill building refer to the Fire System
Schematic included as Figure of this Plan
4.5 Maintenance Shop/Warehouse/Change Room Building
This building approximately 20000 square feet contains the main maintenance shop area
located on the north end of the building the main warehouse located on the south end of the
building and the personnel change rooms and lunchltraining room located on the extreme south
end of the building on the ground and second floors
Within the maintenance shop area are the following work area and specialty shops
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the main maintenance shop area contains welding and cuffing equipment lathes presses
and drill presses
carpenter shop which contains various saws and planes Fiberglass work is also done
within this shop area and it is located at the northwest end of the maintenance shop area
an electrical shop which is located south of the carpenter shop
heavy equipment maintenance shop area is located at the north end of the maintenance
shop in the center of the building
rubber room for rubber lining of equipment is located east of the equipment shop area
the maintenance shop office instrument shop and tool room are located at the south end
of the maintenance shop area
The warehouse area contains primarily dry good storage for repair parts and consumables for the
operation of the Mill There is an electrical water heater for the change room which is located in
the warehouse area at the south end
Within the warehouse and maintenance shops there are some oils and chemicals stored in the
following locations
smail quantities of flammable material such as starting fluid and spray paint are kept in
the warehouse
drums of new oil and anti-freeze are stored along the east wall of the equipment
maintenance area and on the east side of the warehouse on oil storage racks
used oil is stored in tank located northeast of the equipment shop The tank has
capacity of approximately 5800 gailons
in the main maintenance shop area and the rubber room there are flammable storage
cabinets and east of the warehouse there is trailer which is used to store flammable
items such as rubber cements paints and fiberglass resins
compressed gas cylinder storage both empty and full is located outside east of the
maintenance shop
4.5.1 Electrical
The main electrical circuit breaker for the maintenance shop and warehouse building is located
on the east wail inside the Maintenance shop Auxiliary electrical panels for the change room
and warehouse are located in the southwest corner of the warehouse area
4.5.2 Fire Protection System
The fire protection system within the maintenance shop/warehouse/change room building
includes
wet automatic sprinkler system that releases at 212
portable dry chemical extinguishers strategically located throughout the maintenance
area warehouse area and the change room and lunch room
For fire hydrant and hose cabinet locations refer to the Fire System Schematic Figure
4.6 Reagent and Fuel Storage
The following lists the reagents and fuel stored at the Mill site
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sulfuric acid tank located northwest of the mill building which has capacity of
approximately 1.4 million gallons
storage tank for propane is located on the north edge of the mill site northwest of the
mill building It has storage capacity of 30000 gallons
four sodium chlorate tanks located east of SX building north of the office building and
east of the pulp storage tanks The two tanks east of the SX building are for sodium
chlorate storage and the other two tanks are for dilution of the sodium chlorate
two anhydrous ammonia tanks located east of the SX building with capacity of 31409
gallons each
three kerosene tanks located east of the SX building with capacity of 10152 gallons
each
one caustic soda tank north of the SX building with capacity of 19904 gallons
three soda ash tanks which are located east of the SX building One tank is the dry soda
ash tank with capacity of 70256 gallons Two of the tanks are soda ash dilution tanks
with capacities of 16921 gallons each
diesel fuel and gasoline are stored in two tanks located on the eastern side of the ore pad
The gasoline storage capacity is 3200 gallons while diesel storage capacity is 8000
gallons
Other reagents are stored in steel barrels or super sacs in reagent yard located east of the office
building Typical reagents which are stored in this yard include
polymers and flocculants
boiler feed water chemicals
methanol
tributyl phosphate
dirty soda ash and ammonium sulfate
SX ainines and emulsion breakers
decyl alcohol
minimal amounts of acid in barrels
used oil in drums and overpacks
4.7 Boiler Facilities
The main building approximately 12400 square feet is located on the west side of the Mill site
and contains air compressors and water treatment facilities To the north of the main building is
building which houses propane-fired boiler The vanadium oxidation tank oxidation
thickener and pH adjustment tank are located south of the boiler house facilities
4.7.1 Electrical
The main electrical panel for the boiler house is located outside of the building on the south
wall
4.7.2 Fire Protection System
The fire protection system for the boiler facilities is comprised of strategically located portable
dry chemical extinguishers
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4.8 Sample Plant
The sample plant building approximately 8000 square feet is located on the ore pad east of the
maintenance shop/warehouse building The sampling plant equipment has been removed from
the building and it is currently used as storage area for maintenance
4.8.1 Electrical
The electrical panel for this building is located on the east wall upstairs
4.8.2 Fire Protection System
There are no extinguishers or sprinkler systems in the sample plant
ORGANIZATION AND RESPONSIBILITIES
The organizational chart for an emergency situation is illustrated in Figure
5.1 Mill Manager/Incident Commander
The Incident Commander has the responsibility for
preparing an Emergency Plan
communicating the Plan
directing activities during emergencies and
reporting to local State and Federal authorities
The Incident Commander will stop routine radio usage upon learning of an emergency and set up
the base station in safe location for directing activities Radio usage will be limited to the
emergency The Incident Commander has the responsibility to contact all outside services
The Incident Commander has the responsibility to account for all employees at the Mill using
the assistance of supervisors and/or any International Uranium USA Corporation IUSA
personnel The Incident Commander has the responsibility for the news media and reports
directly to the President of IUSA
5.2 Mill General Superintendent
The Mill General Superintendent has the responsibility of directing outside emergency personnel
and has the responsibility for plant security and will report directly to the Incident Commander
The Mill General Superintendent will act as Incident Commander in the absence of the Mill
Manager
5.3 Radiation Safety Officer/Fire Chief
The Radiation Safety Officer will direct rescue operations and provide the necessary emergency
medical personnel and facilities to cope with the emergency Adequately trained fire crews and
operable emergency equipment will be maintained at all times
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INTERNATIONAL URANIUM USA CORPORATION
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As Fire Chief the Radiation Safety Officer has the responsibility to maintain trained fire crews
and operable equipment mobilize and direct the fire crews and equipment in fire emergency or
one containing the threat of fire and to assist in evacuation and rescue or recovery operations
In the absence of the Radiation Safety Officer the Mill Safety Coordinator will assume these
duties
5.4 Maintenance Supervisor
The Maintenance Supervisor will direct all personnel in evacuation and in activities to cope with
the emergency including isolation of utilities and providing technical advice as needed The
Maintenance Supervisor will be assisted by the Mill Safety Coordinator
5.5 Laboratory Supervisor
The Laboratory Supervisor has the responsibility to direct and account for all office personnel
including IUSA personnel and office visitors in evacuation and in activities to cope with the
emergency In case of mill tour the Supervisor accompanying the tour will be responsible for
evacuation of visitors
5.6 Shift Foremen
Shift Foremen are in charge until the Incident Commander arrives and are responsible for all
functions listed above Shift Foremen have the responsibility to account for all of their people in
addition to any visitors contractors etc in their areas and report to the Incident Commander or
in the absence of the Incident Commander to administer all of the above duties
5.7 Scale House Personnel
Scale house person on shift will be responsible to account for ore truck drivers and reagent truck
drivers
5.8 Emergency Response Teams
The response crew for each operating shift will normally consist of the following operators under
the direction of the shift foreman This organization may be changed for individual shifts subject
to the approval of the Fire Chief
5.8.1 Operational Mode
Leach Operator
CCD Operator
Solvent Extraction Operator
Mill Trainee
5.8.2 Non-Operational Mode
Shift Foreman
Operations Personnel
Maintenance Personnel
P\Admin\Master SOPs\Book 16_Emergency Response PJan\Emergency Response Plan Rev 09.29.O5.doc
INTERNATIONAL URANIUM USA CORPORATION
Rev No RI
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page 10 of 13
Figure
Emergency Response Organizational Structure
Incident Commander
Mitt Manager
Director of Security
Operations Superintendent
Fire Chief
Radiation Safety Officer
Shift Foremen Emeipency Response Teams Lab Supervisor
Operatidnal Mode Non-Operational Mode
Leach Operator CCD Operator Shift Foreman Operations Personnel
SX Operator Mill Trainee Maintenance Person net
SPECIFIC EMERGENCIES
The following details procedures to be followed during specific emergencies but are not limited
to the following
6.1 Fire
Should fire occur the procedure outlined in Appendix for reporting and responding to fires
will be followed Particular areas of concern include
Solvent Extraction Building
Propane Tanks
Lab or Lab Storage Area
6.2 Chemical or Gas Release
The procedures for response to chemical or gas release are outlined as Appendix
6.3 Earthquake
Although this is highly unlikely an earthquake could occur at the Mill severe earthquake
could cause buildings and other structures to collapse chemical and/or gas releases major fires
as well as general panic In the event of maj or earthquake the evacuation procedures outlined
in Appendix will be followed
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INTERNATIONAL URANIUM USA CORPORATION
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Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page 11 of 13
6.4 Terrorist/Bomb Threat
In the event that any person should receive threat of bomb the following evacuation
procedure should be followed
Notify any person of authority i.e Superintendent Foreman Radiation Safety Officer
who will immediately notify law enforcement authorities and evacuate the threatened
area
Evacuate all persons from the affected area and stop all radio transmissions
6.5 Tailings Dam Break and Major Floods
Flood water breaching tailings embanlcments presents one of the greatest dangers for the sudden
release of tailings solids and impounded water The tailings cells are designed with sufficient
freeboard three feet to withstand back-to-back 100-year storm events or 40%of the probable
maximum flood PMF followed by the 100-year storm event The flood design is equivalent to
15 inches of rainfall In addition the tailings dikes were designed in accordance with U.S NRC
regulations and allow sufficient margin of safety even in the event of an earthquake
The possibility of floods resulting from Westwater Creek Cottonwood Creek and Corral Creek
causing dam failure is extremely remote
The tailings cells and dikes are inspected on both daily and shift basis
Discharges from dike failure would extend three miles before leaving JUSAs property In the
event of dam failure large operating equipment will be mobilized to construct temporary
earthen dikes or bemis downgradient to the failed dike In addition the State of Utah
Department of Radiation Control Executive Secretary the Executive Secretary MSHA and
State of Utah Department of Natural Resources Division of Dam Safety shall be notified
In the event of seismic rupture of tailings slurry pipelines the released sluny will be contained
in the tailings cells regardless of the quantity released
EVACUATION PROCEDURE See Appendix
7.1 Notification
Employees will be notified to evacuate the area by dialing 184 on any area telephone and
announcing that the Mill should be evacuated This announcement will be repeated twice When
the paging system cycles through the evacuation siren continuous frequency will automatically
sound for approximately forty-five seconds and then automatically shut off allowing
communications by radio from that point If the 184 number is dialed accidentally the
evacuation alarm may be canceled by disconnecting the phone until the page cycle ends then re
dial 184 See Exhibits and
7.2 Assembly
When the evacuation alarm sounds or when personnel are verbally notified by radio or other
means all personnel will assemble at
The parking lot south of the office
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Date Sept 29 2005 WIIITE MESA MILL EMERGENCY RESPONSE PLAN Page 12 of 13
The scalehouse
North side of Tailings Cell or
North of the Mill
Assembly site will depend upon conditions i.e nature of the emergency wind conditions etc
The Fire Chief or Shift Foreman will specify the appropriate assembly site
7.3 Specific Procedure for Operations Personnel
See specific emergency shutdown procedure for Operations by area under the relevant
Operating Procedure for your area
All employees not mentioned under Operating Procedures are to immediately report to
the assembly area and congregate by crew so that all persons can be accounted for As
employees leave their work areas they must pass the word to evacuate to any persons
who may not be aware of the emergency
After the Mill has been determined to be safe for re-entry employees will be verbally
notified to return to their work stations
Off-Site Emergency Equipment/Personnel Release
Any emergency response equipment or personnel that enter the Restricted Area in response to an
incident will be scanned and decontaminated prior to leaving the site according to the procedures
included in PBL-9 End Dump Trailer Acceptance Handling and Release Any equipment will
be decontaminated according to the requirements found in Table of the Nuclear Regulatory
Commissions NRCs Policy and Guidance Directive FC-85-23 Guidelines for
Decontamination of Facilities and Equipment Prior to Release for Unrestricted Use or
Termination of Licenses for Byproduct Source or Special Nuclear Material issued May 1987
Injured personnel should be evaluated for radiation contamination if there was potential for
contamination at the earliest convenience Should it be necessary contaminated articles will be
gathered by the radiological staff after medical treatment has been rendered If the personnel
cannot be decontaminated notify the clinic/hospital personnel in advance
EMERGENCY EQUIPMENT
Emergency equipment for the Mill is provided as follows
9.1 Fire Hose
Fire hose cabinets are located at the following sites with minimum of 300 feet of 2-1/2 hose
two spanner wrenches spray nozzles and one hydrant wrench
South of SX
West of CCD
North of Mill Building
East of pulp storage tanks
Northwest of Maintenance Shop
West of Warehouse
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INTERNATIONAL URANIUM USA CORPORATION
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East of office building
9.2 Self Contained Breathing Apparatus
Two Self-Contained Breathing Apparatus
are located at each of the following locations
Hose station east of office building
Hose Station South of SX
North End SX Outside Wall
North end of Mill building outside wall
9.3 Spill Clean-up Equipment
Barrels of soda ash are located throughout the Mill to be used in case of chemical spill Soda
ash is also stored in bulk if needed There are also few drums of absorbent stored near the
laboratory The laboratory also contains acid spill kits and absorbent materials to be used in case
of spill
9.4 Fire Fighting PPE
Two complete sets of turnout gear for fire fighting and/or emergency extrication are located in
the Fire Hose Station located on the east side of the office building
9.5 Maintenance of Emergency Equipment
Fire extinguishers are inspected on an annual basis as well as the fire pump system The Mill
Safety Coordinator performs regular spot checks on the emergency equipment locations to ensure
that all of the equipment is in place
10 EMERGENCY TRANSPORTATION
One fully-equipped First Responder Unit Ambulance located west of the office building
Other motor pool vhicles on the property will be utilized as needed in emergency situations with
support as needed from the local Emergency Medical Services
11 EMERGENCY DRILLS AND TRAINING
Quarterly drills as required by MSHA are prepared by the Safety and Radiation Departments to
monitor performance of personnel responding to emergency situations Each drill will be
enacted upon one or more of the potential scenarios by this plan The drill and evacuation
activities are documented by the Mills Safety Coordinator and maintained within plant files
Management will review all drills at quarterly ALARA Committee Meetings
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc
EXIIIBIT
EMERGENCY NOTIFICATION LIST
ATTEND TO ANY INJURED PERSONS AND NOTIFY THE SUPERVISOR
Give artificial respiration if necessary
Control bleeding
Treat for shock
Immobilize fractures and stabilize for transportation
Scan the injured for excessive alpha prior to transporting if time allows
If alpha is excessive or there is no time to scan notify the clinic/hospital personnel and the
Radiation Safety Office
THE SUPERVISOR OR HIS DESIGNEE WILL NOTIFY THE FOLLOWING AS NEEDED
Blanding Clinic 678-2254 or 678-3434 930 400
San Juan Hospital Monticello ...678-2830 or 587-2116 364 1st
EMT and CPR TRAINED The following personnel should be contacted if they are on-site in the
event of an emergency to aid in the event of any injuries to personnel
David Turk EMT and CPR trained
Mike Spillman CPR trained
AMBULANCE SERVICE
Blanding Dial 911
If the Company Ambulance is used an attendant must ride with the injured in addition to the driver
except where the injured could normally be transported in car or pickup
OTHER EMERGENCY NUMBERS
Fire Department Dial 911 or 678-2313
County Sheriff Dial 911 or 587-2237
Highway Patrol Dial 911 or 587-2000
Blanding Police Dial 911 678-2916 or 678-2334
MANAGERS
The Supervisor will notify one of the following of all incidents
R.E Bartlett 435-678-2495
Turk 435-678-7802 or 435-459-1068
Spillman 435-678-2761
MEMBER OF MANAGEMENT WILL NOTIFY THE PROPER REGULATING AGENCIES
AS REQUIRED FOR EACH INCIDENT
State of Utah Department of Radiation Control 801-536-4250
MSHA Field Off.--80l-524-3450 Dist Off 303-231-5465
MSHA Arlington 800-746-1553
State Emergency Response Comm 801-538-3400
State of Utah Natural Resources Dam Safety 801-538-7200
National Response Center 800-424-8802
Utah Poison Control Center 800-456-7707
Notification of surrounding communities and or residences will be handled by the appropriate agencies as
required by EPCRA Emergency Planning and Community Right to Know Act
Revision Date January 16 2006 E-1
EXHIBIT
INTERNAL NOTIFICATIONS
Internal reporting requirements for Incidents Spills and Significant Events are as follows
Report Immediatejy
Event Criteria
Release of toxic or hazardous substances
Fire explosions or other accidents
Government investigations information requests or enforcement actions
Private actions or claims corporations or employees
Deviations from Corporate policies or government requirements by Management
Other significant events which have resulted or could result in
Death serious injury or adverse health effect employees or public
Property damage exceeding $1000000
Government investigation or enforcement action limiting operation or penalties
of $100000 or more
Significant criminal actions
Substantial media coverage
Unscheduled down time of more than 24 hours
Report at the Beginning of the Next Business Day
Tncident Criteria
Was reported to government agency as required by law
Worker IUSA or contractor recordable injury or illness associated with release
Community impact reported or awareness
Publicity resulted or is anticipated
Release of process material waste or product in excess of the Reportable
Quantities listed in Section 1.5 of the Spill Prevention Control and
Countermeasures Plan
The local manager in charge is to call Ron Hochstein or Dave Frydenlund
Name Title Office Phone Home Phone
Ron Hochstein President and COO 303-628-7798 office
604-931-6334 home
604-377-1167 cell
David Frydenlund V.P and General Counsel 303-389-4130 office
303-221-0098 home
303-808-6648 cell
Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 02.14.07 E-2
EXHIBIT
SITE LAYOUT MAP
P\Admin\Master SOPs\Book 16_Emergency Response PJan\Emergency Response Plan Rev 09.29.05.doc E-3
et
Ca Ci
LI -I Cl Cl Ci
EXHIBIT
MAIN SHUT-OFF VALVES
During an emergency this list should be used along with Site Layout Map Exhibit to locate
tanks and valves associated with these tanks
REAGENT SHUT-OFF VALVE LOCATIONS
Sulfuric Acid
Main located south side of acid tank
East acid pump discharge valve
West acid pump discharge valve
Main leach area located 25 feet west of Derrick screens next to walkway
1-1/2 Main SX area located south of Central Control room
Ammonia
Main east tank located on end at bottom
Main west tank located on end at bottom
Valve located on top of tank east tank
Valve located on top of tank west tank
Kerosene
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Pump discharge valve
Soda Ash
Main valve located at bottom of tank dry storage
Main valve located at bottom of tank on 30%dilution tank
Main valve locate at bottom of tank on dilution tank
Salt
Main valve located at bottom of tank
Caustic Soda
Main valve located at bottom of tank east and west between supports
P\Admin\Master SOPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc E-4
EXHJBIT
MAIN SHUT-OFF VALVES
Sodium Chlorate
31 Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Propane
Main located 15 feet east of tank
Main located on pipe off top of tank
Main located at bottom of tank also fill pipe
PLANT UTILITY SHUT-OFF VALVE LOCATIONS
Process Water
Main valve located on west side of water storage tank
Discharge valve off service water pump east
Discharge valve off service water pump west
Mill process water main located east wall by SAG mill
Fire Water
Main valve located west side of water storage tank
Emergency fire pump discharge valve to fire system
Emergency fire pump discharge valve to header west side of pump house
Main valve located south of Central Control room for SX and boilers
Potable Water
Main suction from potable water storage tank
Main discharge from potable water storage tank
Main located at east wall by SAG mill
Main located south of Central Control room for SX Maintenance shop and offices
Steam
Main discharge valve for Superior boiler located at top of boiler
Main steam valve located south side of boiler house
PfsAdmin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
EXHIBIT
MAIN SHUT-OFF VALVES
Plant Air
Main valve located at receiver tank in compressor room at boiler house
Main valve to mill building located south of Central Control room
PROCESS SHUT-OFF VALVE LOCATIONS
Pulp Storage
No valve located on west side of tank
No valve located on west side of tank
Preleach old No pulp storage valve located on west side of tank
Preleach Thickener
Main valve located underneath at center cone
Clarifier
Main valve located underneath at center cone
Main valve located underneath at center cone
CO Thickeners
Main valve located underneath at center cone of each thickener
PAdmin\Master 5OPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 0929.05 doe E-4
APPENDIX
EMERGENCY PROCEDURE RESPONSE TO FIRE
The fire will be reported by dialing 185 on any telephone in the area and announcing the
location of the fire over the paging system This announcement will be repeated twice
for total of three announcements When the paging system cycles through the fire siren
alternating frequency will automatically sound for approximately forty-five seconds
then automatically shut off allowing radio communications to resume
Mobilize the fire crew
Evacuate all personnel
Rescue any victims of the fire do this only with properly trained and equipped personnel
Isolate utility lines affected by the fire
Extinguish the fire and post fire watch for flare-ups
Report the fire to proper local State Corporate and Federal agencies
In cases where the fire is not extinguished within thirty minutes of discovery the area
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iliUnt uc Owl icaucu on aitcl cAungwnn1g atlu icit iutui ucu unui cica5cu oy ivionn
and JUSA management
Emergency off-site centers Blanding Fire House and Sheriffs office
Blanding Fire
350 West 200 South Blanding
Phone number is 911
Sheriffs Office
50 West 100 South Blanding
Phone number is 911 or 435 587-2237
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-I
APPENDIX
EMERGENCY PROCEDURE
RESPONSE TO CHEMICAL OR GAS RELEASE
chemical or gas release would most likely occur very suddenly The person who would first
witness chemical or gas release should immediately contact his supervisor who would initiate
the procedures outlined below
Activate evacuation alarm by using the dial 184 notification system Evacuate and
account for all personnel
Mobilize trained personnel and emergency equipment such as SCBAs first aid
equipment etc
Initiate rescue operations for any people who may be trapped by the release
Provide first aid and emergency medical care for any ill or injured persons
Initiate necessary steps to contain and/or neutralize the release such as spraying with
water fog turning off valves etc
Guard against possible fires by shutting off electrical circuits isolating gas lines and
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P\Admin\Master SOPs\Book 16_Emergency Response Plan \Emergency Response Plan Rev 09.29 05.doc A-I
APPENDIX
EMERGENCY EVACUATION PROCEDURE
Activate evacuation alarm by using the dial 184 notification system Evacuate and account
for all personnel
Personnel are to assemble in one of the following areas
The parking lot south of the office building
The scalehouse
The north side of Tailings Cell or
North of the Mill
Mobilize trained personnel and emergency equipment such as SCBAs first aid equipment
etc
Initiate rescue operations for any people who may be trapped
Provide first aid and emergency medical care for any ill or injured persons
Guard against possible fires by shutting off electrical circuits isolating gas lines and
eliminating ignition sources from the affected area
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-i
FIGURE
FIRE SYSTEM SCHEMATIC DRAWING
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-i
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STORM WATER
BEST MANGEMENT PRACTICES PLAN
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Blanding Utah
June 2008
Prepared by
Denison Mines USA Corp
1050 17th Street Suite 950
Denver CO 80265
TABLE OF CONTENTS
1.0 Purpose
2.0 Scope
3.0 Responsibility
4.0 Best Management Practices
4.1 General Management Practices Applicable to All Areas
4.2 Management Practices for Process and Laboratory Areas
4.3 Management Practices for Maintenance Activities
4.4 Management Practices for Ore Pad Tailings Area and heavy Equipment
Operations
Figures
Figure White Mesa Mill Site Map
Figure Mill Site Drainage Basins
Figure IIUSA Mill Management Organization Chart
Figure 1JSA Corporate Management Organization Chart
Tables
Table White Mesa Mill Management Personnel Responsible for Jmplementing
This BMPP
Appendices
Appendix White Mesa Mill Spill Prevention Control and Countermeasures Plan
Appendix White Mesa Mill Emergency Response Plan
Best Management Practices Plan
Revision 1.3 June 12 2008
1.0 INTRODUCTION/PURPOSE
Denison Mines USA Corp DUSA operates the White Mesa Uranium Mill the Mill in
Blanding Utah The Mill is net water consumer and is zero-discharge facility with respect to
water effluents That is no water leaves the Mill site because the Mill has
no outfalls to public stormwater systems
no surface runoff to public stormwater systems
no discharges to publicly owned treatment works POTW5 and
no discharges to surface water bodies
The State of Utah issued Groundwater Discharge Permit No UGW3 70004 to DUSA on March
2005 As part of compliance with the Permit DUSA is required to submit Stormwater Best
Management Practices Plan BMPP to the Executive Secretary of the Division of Radiation
Control Utah Department of Environmental Quality This BMPP presents operational and
management practices to minimize or prevent spills of chemicals or hazardous materials which
could result in contaminated surface water effluents potentially impacting surface waters or
ground waters through runoff or discharge connections to stormwater or surface water drainage
routes Although the Mill by design cannot directly impact stormwater surface water or
groundwater the Mill implements these practices in good faith effort to minimize all sources of
pollution at the site
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
2.0 SCOPE
This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in
process operations laboratory operations and maintenance activities and minimize spread of
particulates from stockpiles and tailings management areas at the Mill Storage of ores and
alternate feeds on the ore pad and containment of tailings in the Mill tailings impoundment
system are not considered spills for the purposes of this BMPP
The Mill site was constructed with an overall grade and diversion ditch system designed to
channel all surface runoff including precipitation equivalent to Probable Maximum
Precipitation/Probable Maximum Flood PMP/PMF storm event to the tailings management
system In addition Mill tailings all other process effluents all solid waste and debris except
used oil and recyclable materials and spilled materials that cannot be recovered for reuse are
transferred to one or more of the tailings cells in accordance with the Mills NRC license
conditions All of the process and laboratory building sinks sumps and floor drains are tied to
the transfer lines to the tailings impoundments site map of the Mill is provided in Figure
sketch of the site drainage basins is provided in Figure
As result unlike other industrial facilities whose spill management programs focus on
minimizing the introduction of chemical and solid waste and wastewater into the process sewers
and storm drains the Mill is permitted by NRC license to manage some spills via draining or
washdown to the process sewers and ultimately the tailings system However as good
environmental management practice the Mill attempts to minimize
the number and size of material spills and
the amount of unrecovered spilled material and washwater that enters the process sewers
after spill cleanup
Section 4.0 itemizes the practices in place at the Mill to meet these objectives
Requirements and methods for management recordkeeping and documentation of hazardous
material spills are addressed in the DUSA White Mesa Mill Spill Prevention Control and
Countermeasures SPCCPlan Revised February 2007 the Emergency Response Plan
ERP also revised in February 2007 and the housekeeping procedures incorporated in the
White Mesa Mill Standard Operating Procedures SOPs The SPCC plan and the ERP are
provided in their entirety in Appendices and respectively
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
3.0 RESPONSIBILITY
All Mill personnel are responsible for implementation of the practices in this BMPP DUSA
White Mesa Mill management is responsible for providing the facilities or equipment necessary
to implement the practices in this BMPP
The Mill Management Organization is presented in Figure The DUSA Corporate
Management Organization is presented in Figure
An updated spill prevention and control notification list is provided in Table
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.0 BEST MANAGEMENT PRACTICES
summary list and inventory of all liquid and solid materials managed at the Mill is provided in
Tables through
4.1 General Management Practices Applicable to All Areas
4.1.1 Keep Potential Pollutants from Contact with Soil and Surface Water
Store hazardous materials and other potential pollutants in appropriate containers
Label the containers
Keep the containers covered when not in use
4.1.2 Keep Potential Pollutants from Contact with Precipitation
Store bulk materials in covered tanks or drums
Store jars bottle or similar small containers in buildings or under covered areas
Replace or repair broken dumpsters and bins
Keep dumpster lids and large container covers closed when not in use to keep
precipitation out
4.1.3 Keep Paved Areas from Becoming Pollutant Sources
Sweep paved areas regularly and dispose of debris in the solid waste dumpsters or
tailings area as appropriate
4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the
Process and Reagent Storage Area
Diversion ditches drainage
channels and surface water control structures in and around
the Mill area will be inspected at least weekly in accordance with the regularly scheduled
inspections required by Groundwater Discharge Permit No UGW370004 and
Byproduct Materials License UT1900479 Areas requiring maintenance or repair such
as excessive vegetative growth channel erosion or pooling of surface water runoff will
be report to site management and maintenance departments for necessary action to repair
damage or perform reconstruction in order for the control feature to perform as intended
Status of maintenance or repairs will be documented during follow up inspections and
additional action taken if necessary
4.1.5 Recycle Fluids Whenever Possible
When possible select automotive fluids solvents and cleaners that can be recycled or
reclaimed
When possible select consumable materials from suppliers who will reclaim empty
containers
Keep spent fluids in properly labeled covered containers until they are picked up for
recycle or transfened to the tailings area for disposal
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.2 Management Practices for Process and Laboratory Areas
4.2.1 Clean Up Spills Properly
Clean up spills with dry cleanup methods absorbents sweeping collection drums
instead of water whenever possible
Clean spills of stored reagents or other chemicals immediately after discovery
Groundwater Discharge Permit No UGW370004 Section I.D.8.c
Recover and re-use spilled material whenever possible
Keep supplies of rags sorbent materials such as cat litter spill collection drums and
personnel protective equipment PPE near the areas where they may be needed for
spill response
If spills must be washed down use the minimum amount of water needed for effective
cleanup
4.2.2 Protect Materials Stored Outdoors
If drummed feeds or products must be stored outdoors store them in covered or diked
areas when possible
If drummed chemicals must be stored outdoors store them in covered or diked areas
when possible
Make sure drums and containers stored outdoors are in good condition and secured
against wind or leakage Place any damaged containers into an overpack drum or second
container
4.2.3 Water Management
When possible recycle and reuse water from flushing and pressure testing equipment
When possible wipe down the outsides of containers instead of rinsing them off in the
sink
When possible wipe down counters and work surfaces instead of hosing or rinsing them
off to sinks and drains
4.2.4 Materials Management
Purchase and inventory the smallest amount of laboratory reagent necessary
Do not stock more of reagent than will be used up before its expiration date
All new construction of reagent storage facilities will include secondary containment
which shall control and prevent any contact of spilled reagents or otherwise released
reagent or product with the ground surface Groundwater Discharge Permit No
UGW370004 Section I.D.3.e
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.3 Management Practices for Maintenance Activities
4.3.1 Keep Clean Dry Shop
Sweep or vacuum shop floors regularly
Designate specific areas indoors for parts cleaning and use cleaners and solvents only in
those areas
Clean up spills promptly Dont let minor spills spread
Keep supplies of rags collection containers and sorbent material near each work area
where they are needed
Store bulk fluids waste fluids and batteries in an area with secondary containment
double drum drip pan to capture leakage and contain spills
4.3.2 Manage Vehicle Fluids
Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as
possible Use drip pans or plastic tarps to prevent spillage and spread of fluids
Promptly contain and transfer drained fluids to appropriate storage area for reuse recycle
or disposal
Recycle automotive fluids if possible when their useful life is finished
4.3.3 Use Controls During Paint Removal
Use drop cloths and sheeting to prevent windbome contamination from paint chips and
sandblasting dust
Collect contain and transfer as soon as possible accumulated dusts and paint chips to
disposal location in the tailings area authorized to accept waste materials from
maintenance or construction activities
4.3.4 Use Controls During Paint Application and Cleanup
Mix and use the right amount of paint for the job Use up one container before opening
second one
Recycle or reuse leftover paint whenever possible
Never clean brushes or rinse or drain paint containers on the ground paved or unpaved
Clean brushes and containers only at sinks and stations that drain to the process sewer to
the tailings system
Paint out brushes to the extent possible before water washing water-based paint or
solvent rinsing oil-based paint
Filter and reuse thinners and solvent whenever possible Contain solids and unusable
excess liquids for transfer to the tailings area
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.4 Management Practices for Ore Pad Tailings Area and Heavy Equipment
Detailed instructions for ore unloading dust suppression and tailings management are provided
in the Mill SOPs
4.4.1 Wash Down Vehicles and Equipment in Proper Areas
Wash down trucks trailers and other heavy equipment only in areas designated for this
purpose such as washdown pad areas and the truck wash station
At the truck wash station make sure the water collection and recycling system is working
before turning on water sprays
4.4.2 Manage Stockpiles to Prevent Windborne Contamination
Water spray the ore pad and unpaved areas at appropriate frequency in accordance with
Mill SOPs
Water spray stockpiles as required by opacity standards or weather conditions
Dont over-water Keep surfaces moist but minimize runoff water
4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources
Schedule excavation grading and other earthmoving activities when extreme dryness and
high winds will not be factor to prevent the need for excessive dust suppression
Remove existing vegetation only when absolutely necessary
Seed or plant temporary vegetation for erosion control on slopes
Page7
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Home Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.l66
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Rome Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE
REAGENT YARD LIST
REAGEN1Hi .QUAN1rnLBS eNUMBEROF APACfl11
STORAGE-TANKS CAtiONS
ADOGEN 2382 6120
ADVANTAGE 1O1M 2475
AMERSITE
AMINE 2384 19440
AMMONIUM SULFATE BULK 54000
AMMONIUM SULFATE BAGS 4300
ANHYDROUS AMMONIA 107920 31409
CHEMFAC 100 12800
CLARIFLOC N-1O1P 3000
DECYLALCOHOL 45430
DIESEL FUEL 250
6000
FLOCCULENT M1O11N 30550
FLOCCULENT M1302C 3550
GRINDING BALLS 48290
ISODECANOL 45430
KEROSENE 1344 10152
MACKANATE 3150
MILLSPERSE 802 1410
NALCO 2458
NALCO 8815
PERCOL 351 1500
PERCOL 406 13950
PERCOL 745
POLOX 10360
POLYHALL YCF
PROPANE 30000
SALT BAGS 39280
SALT BULK
SODA ASH BAGS 39280
SODA ASH BULK 84100 16921
8530
SODIUM CHLORATE 101128 17700
10500
SODIUM HYDROXIDE 19904
SULFURIC ACID 4801440 1600000
269160
UNLEADED GASOLINE 3000
USED OIL 5000
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
Chemical in Lab RQ2 Quantity In Stock
Aluminum nitrate 2270 kg 1.8 kg
Ammonium bifluoride 45.4 kg 2.27 kg
Ammonium chloride 2270 kg 2.27 kg
Ammonium oxalate 2270 kg 6.8 kg
Ammonium thiocyanate 2270 kg 7.8 kg
Antimony potassium tartrate 45.4 kg 0.454 kg
n-Butyl acetate 2270 kg
Carbon tetrachloride 4.54 kg 1.0
Cyclohexane 454 kg 24
Ferric chloride 454 kg 6.810 kg
Ferrous ammonium sulfate 454 kg 0.57 kg
Potassium chromate 4.54 kg 0.114 kg
Sodium nitrite 45.4 kg 2.5 kg
Sodium phosphate tribasic 2270 kg 1.4 kg
Zinc acetate 454 kg 0.91 kg
Chemical in Volatiles and RQ2 Quantity In Stock
Flammables Lockers ABC
Chloroform 4.54 kg
Formaldehyde 45.4 kg of 37%solution
Nitrobenzene 454 kg 12
Toluene 454 kg 12L
Chemical in Acid Shed RQ2 Quantity In Stock
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
fftRQ7 QJA1.JN
Acetic Acid Glacial 1000 lbs gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 lbs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs kg 11 Ibs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal 5kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARDIBULK CHEMICALS LIST1
REAGENT RQ QUANTITY IN
REAGENT YARD
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfloc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution Control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous substances Designated Pursuant to section 311 of the Clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT QUANTITY IN
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
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Mill Site Drainage Basins
Figure
White Mesa Mill
Mill Management Organization Chart
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APPENDICES
APPENDIX
WHITE MESA MTLL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
FOR CHEMICALS AND PETROLEUM PRODUCTS
for
White Mesa Uranium Mill
6425 South Highway 191
Box 809
Blanding Utah 84511
February 2007
Prepared by
Denison Mines USA Corp
1050 7th Street Suite 950
Denver Colorado 80265
TABLE OF CONTENTS
SECTION PAGE
1.1 Objective
1.2 Responsibilities
1.3 Drainage Basins Pathways and Diversions
1.4 Description of Basins
1.4.1 Basin Al
.4.2 Basin A2
1.4.3 Basin BI
1.4.4 Basin B2
1.4.5 Basin B3
1.4.6 Basin
1.4.7 Basin
1.4.8 Basin
1.5 Potential Chemical Spill Sources And Spill Containment
1.5.1 Reagent Tanks
1.5.2 Ammonia
1.5.3 Ammonium Meta Vanadate
1.5.4 Caustic Storage Sodium Hydroxide
1.5.5 Sodium Carbonate
1.5.6 Sodium Chlorate
1.5.7 Sulfuric Acid
1.5.8 Vanadium Pentoxide
1.5.9 Kerosene Organic
1.6.0 Used/Waste Oil
SECTION PAGE
1.6.1 Propane
1.7 Potential Petroleum Sources And Containment
1.7.1 Petroleum Storage Tanks
1.7.1.1 Diesel
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.2 Unleaded Gasoline
1.7.2.3 Pump Station
1.7.2.4 Truck Unloading
1.8 Spill Discovery And Remedial Action
1.9 Spill Incident Notifications
1.9.1 External Notification
1.9.2 Internal Notification 11
1.10 Records And Reports 12
1.11 Personnel Training And Spill Prevention Procedures 12
1.11.1 Training Records 12
1.11.2 Monitoring Reports 13
1.12 Revision 13
1.13 Summary 13
1.14 Mill Manager Approval 14
1.15 Certification by Registered Professional Engineer 14
LIST OF TABLES
Table 1.0 Mill Organization Chart
Table 2.0 Reagent Tank List
Table 3.0 Laboratory Chemical Inventory List
Table 4.0 Reagent Yard/Small Quantity Chemicals List
Table 5.0 Reagent Yard/Bulk Chemicals List
Table 6.0 Petroleum Products and Solvents List
LIST OF FIGURES
Figure Mill Site Layout
Figure Mill Site Drainage Basins
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS
1.1 OBJECTIVE
The objective of the Spill Prevention Control and Countermeasures SPCC
Plan is to serve as site-specific guideline for the prevention of and response to
chemical and petroleum spills and as guidance document for compliance with
Groundwater Discharge Permit No UGW370004 The plan outlines spill
potentials containment areas and drainage characteristics of the White Mesa
Mill site The plan addresses chemical spill prevention spill potentials spill
discovery and spill notification procedures The Oil Pollution Prevention Sections
of the Clean Water Act 40 CFR 112 to 117 also referred to as the Spill
Prevention Control and Countermeasures SPCC rules establish
requirements that apply to facilities which could reasonably be expected to
discharge oil in quantities that may be harmful as described in that Act into or
upon the navigable waters of the United States or that may affect natural
resources of the United States Section 112 states that the Act is not applicable
to facilities that are not subject to the authority of the Environmental
Protection Agency EPA for one of the following reasons
Due to its location the facility could not reasonably be expected to
discharge oil into navigable waters of or impact natural resources of the
U.S or
The facility is subject to authority of the Department of Transportation as
defined in Memorandum of Understanding MOU between the
Secretary of Transportation and the EPA Administrator or
The facility does not exceed either the underground or the above ground
storage capacity 42000 gallons and 1320 gallons respectively
prescribed in the rules
The Mill could not reasonably be expected as described in the SPCC regulation
to discharge oil into the navigable waters or impact natural resources of the
U.S The Mill site was constructed with an overall grade and diversion ditch
system designed to channel the non-recovered portion of any material spill to the
tailings management system Hence it is not reasonable to expect that surface
spills will ever reach navigable waters or natural resources of the U.S or Utah
Therefore the SPCC reporting requirements in the Clean Water Act are not
applicable to the Mill However as good environmental management practice
the Mill has implemented the spill management program described in this
document which is consistent with the intent of the Clean Water Act to the
extent practicable Although the Mill by design cannot directly impact navigable
waters of the U.S and as result spills that may occur but are retained within
the site would not be reportable the Mill implements these practices in good
faith effort to minimize all potential sources of pollution at the site
Storage of ores and alternate feeds on the ore pad and containment of tailings
in the Mill tailings impoundment system are not considered spills for the
purposes of this SPCC
Ammonia is the only chemical that has the potential to leave the site and would
do so as vapor
Figure Site Layout Map shows map of the mill site including the locations of
the chemical tanks on-site Figure shows the basins and drainage ditch areas
for the mill site Table 1.0 is an organization chart for Mill operations Table 2.0
lists the reagent tanks and their respective capacities Table 3.0 lists the
laboratory chemicals their amounts and their reportable quantities Table 4.0
lists the operations chemicals Table 5.0 lists the chemicals in the reagent yard
their amounts and their reportable quantities Table 6.0 lists the petroleum
products and solvents on site
1.2 RESPONSIBILITIES
Person in charge of facility responsible for spill prevention
Mr Richard Bartlett Interim Mill Manager
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 459-2495 home
Person in charge of follow-up spill record keeping and/or reporting
Mr David Turk Department Head Health Safety and Environmental
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 678-7802 home
Refer to Section 1.9 Spill Incident Notification for list of company personnel
to be notified in case of spill In addition an organizational chart is provided
in Table 1.0
1.3 DRAINAGE BASINS PATHWAYS AND DIVERSIONS
The main drainage pathways are illustrated in Figure The map shows
drainage basin boundaries flow paths constructed diversion ditches tailings
cells the spillway between Cell and dikes berms and other relevant
features The White Mesa Mill is zero discharge facility for process liquid
wastes The mill area has been designed to ensure that all spills or leaks
from tanks will drain toward the lined tailings cells
The tailings cells in turn are operated with sufficient freeboard minimum of
three feet to withstand 100%of the PMP Probable Maximum Precipitation
This allows for maximum of 10 inches of rain at any given time
1.4 DESCRIPTION OF BASINS
Precipitation and unexpected spills on the mill property are contained within
their respective drainage basins Runoff would ultimately drain into one of
the three lined tailings cells
1.4.1 Basin Al
Basin Al is north of Cell 1-I and Diversion Ditch No The basin
contains 23 acres all of which drain into Westwater Creek This area is
not affected by mill operations
1.4.2 Basin A2
Basin A2 contains all of Cell 1-I including an area south of the Diversion
Ditch No The basin covers 84 acres Any runoff from this basin
would be contained within Cell 1-I
1.4.3 Basin BI
Basin Bl is north of the mill property and is not affected by mill
operations The basin contains 45.4 tributary acres Runoff from this
basin drains into flood retention area by flowing through Diversion Ditch
No Diversion Ditch No drains into Westwater Creek
1.4.4 Basin B2
Basin B2 is northeast of the mill and contains only 2.6 acres Runoff from
this basin would drain into Diversion Ditch No Diversion Ditch No
ultimately drains into Diversion Ditch No This basin is not affected by
mill operations
1.4.5 Basin B3
Basin B3 contains most of the mill area buildings ore stockpiles process
storage tanks retention ponds spill containment structures pipelines
and roadways The normal direction of flow in this basin is from the
northwest to the southwest Any runoff from this basin would drain into
Cell 1-I The basin contains 64 acres This basin has sufficient
freeboard to withstand 100%of the PMP Probable Maximum
Precipitation This allows 10 inches of rain for any given storm event
1.4.6 Basin
Basin contains all of Cell The basin consists of 80.7 acres This
basin contains earth stockpiles and the heavy equipment shop The
direction of flow in this basin is to the southwest All runoff in this basin
would be channeled along the southern edge of the basin Runoff would
then flow into Cell via the spillway from Cell to Cell
1.4.7 Basin
Basin contains all of Cell This basin consists of 78.3 acres including
portion of the slopes of the topsoil stockpile and random stockpile The
basin contains all flows including those caused by the PMF
1.4.8 Basin
Basin contains Cell 4A and consists of 43.3 acres All anticipated flows
including those caused by the PMF will be contained within the basin and
will flow directly into Cell 4A
1.5 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL
CONTAINMENT
This section details potential sources of chemical spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States Reportable
Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act
It is not expected that any spill would reach navigable waters of the United States
However if spill of volume listed below occurs and remains on the mill site which is
the more likely scenario then management is to be notified so that proper internal
evaluations of the spill are made
1.5.1 Reagent Tanks Tank list included in Table 2.0
1.5.2 Ammonia
The ammonia storage tanks consist of two tanks with capacity of
31409 gallons each The tanks are located southeast of the Mill building
Daily monitoring of the tanks for leaks and routine integrity inspections will be
conducted to minimize the hazard associated with ammonia The reportable
quantity for an ammonia spill is gallons
Ammonia spills should be treated as gaseous Ammonia vapors will be
monitored closely to minimize the hazard associated with inhalation If
vapors are detected efforts will be made to stop or repair the leak
expeditiously Ammonia is the only chemical as vapor that has the
potential to leave the site
1.5.3 Ammonia Meta Vanadate
Ammonia meta vanadate is present in the SX building as the process
solutions move through the circuit to produce the vanadium end product
But the primary focus will be on the transportation of this chemical The
reportable quantity for an ammonia meta vanadate spill is 1000 pounds
1.5.4 Caustic Storage Sodium Hydroxide
The caustic storage tank is located on splash pad on the northwest corner
of the SX building The tank has capacity of 19904 gallons The tank
supports are mounted on concrete curbed catchment pad that directs spills
into the sand filter sump in the northwest corner of the SX building The
reportable quantity for sodium hydroxide spill is 85 gallons
1.5.5 Sodium Carbonate Soda Ash
The soda ash solution tank has capacity of 16921 gallons and is located in
the northeast corner of the SX building The smaller soda ash shift tank has
capacity of 8530 gallons and is located in the SX building Spills will be
diverted into the boiler area and would ultimately drain into Cell I-I There is
no reportable quantity associated with sodium carbonate spill
1.5.6 Sodium Chlorate
Sodium chlorate tanks consist of two fiberglass tanks located within dike
east of the SX building The larger tank is used for dilution purposes and has
maximum capacity of 17700 gallons The smaller tank serves as
storage tank and has capacity of 10500 gallons Daily monitoring of the
tanks for leaks and integrity inspections will be conducted to minimize the
hazard associated with sodium chlorate
Sodium chlorate that has dried and solidified becomes even more of safety
hazard due to its extremely flammable nature The reportable quantity for
sodium chlorate spill is 400 gallons
1.5.7 Sulfuric Acid
The sulfuric acid storage tanks consist of one large tank with the capacity of
16000000 gallons and two smaller tanks with capacities of 269160 gallons
each
The large tank is located in the northwest corner of mill area basin B3 and is
primarily used for acid storage and unloading The tank support for the large
tank is on mound above depression which would contain significant
spill All flows resulting would be channeled to Cell 1-I The tank is equipped
with high level audible alarm which sounds prior to tank overflows
concrete spill catchment with sump in the back provides added
containment around the base of the tank However the catchment basin
would not be able to handle major tank failure such as tank rupture The
resulting overflow would flow towards Cell 1-I
The two smaller storage tanks are located within an equal volume spill
containment dike east of the mill building The tanks are not presently in
use but are equipped with high level audible alarms
The reportable quantity for sulfuric acid spill is 65 gallons 1000 pounds
1.5.8 Vanadium Pentoxide
Vanadium pentoxide is produced when vanadium is processed through the
drying and fusing circuits and is not present in the vanadium circuit until after
the deammoniator Efforts will be made to minimize leaks or line breaks that
may occur in processes in the circuit that contain vanadium pentoxide
Special care will be taken in the transportation of this chemical The
reportable quantity for vanadium pentoxide spill is 1000 pounds
1.5.9 Kerosene Organic
The kerosene storage area is located in the central mill yard and has
combined capacity of 10152 gallons in three tanks Any overflow from these
three tanks would flow around the south side of the SX building and then into
Cell 1-I These tanks have drain valves which remain locked unless
personnel are supervising draining operations The reportable quantity for
kerosene spill is 100 gallons
1.6.0 Used Waste Oil
Used Waste oil for parts washing is located north of the maintenance shop
in tank and has capacity of 5000 gallons The tank is contained within
concrete containment system Ultimate disposal of the used oil is to an EPA
permitted oil recycler Any oil escaping the concrete containment system will
be cleaned up Soil contaminated with used oil will be excavated and
disposed of in Cell
1.6.1 Propane
The propane tank is located in the northwest corner of the mill yard and has
capacity of 30000 gallons Daily monitoring of the tank for leaks and
integrity inspections will be conducted to minimize potential hazards
associated with propane leaks Propane leaks will be reported immediately
There is no reportable quantity associated with propane spill
1.7 POTENTIAL PETROLEUM SPILL SOURCES AND
CONTAINMENT
This section details potential sources of petroleum spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States It is not
expected that any spill would reach navigable waters of the United States However if
spill of volume listed below occurs and remains on the mill site which is the more
likely scenario then management is to be notified so that proper internal evaluations of
the spill are made
1.7.1 Petroleum Tanks
1.7.1.1 Diesel
Two diesel storage tanks are located north of the mill building The tanks
have capacities of 250 gallons each One of the diesel tanks is for the
emergency generator The other tank is located in the pumphouse on an
elevated stand Spillage from either tank would ultimately flow into Cell 1-I
The reportable quantity for diesel spill is 100 gallons
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.1 Diesel
The diesel tank is located on the east boundary of Basin B3 and has
capacity of 6000 gallons The tank is contained within concrete catchment
pad The reportable quantity for diesel spill is 100 gallons
1.7.2.2 Unleaded Gasoline
The unleaded gasoline tank is located next to the diesel tank The unleaded
gasoline tank has capacity of 3000 gallons and is contained within the
same containment system as the diesel tank The reportable quantity for an
unleaded gasoline spill is 100 gallons
1.7.2.3 Pump Station
Both the diesel and the unleaded gasoline tanks will be used for refueling
company vehicles used around the mill site The pump station is equipped
with an emergency shut-off device in case of overflow during fueling In
addition the station is also equipped with piston leak detector and
emergency vent Check valves are present along
with tank monitor
console with leak detection system The catchment is able to handle
complete failure of one tank However if both tanks failed the concrete
catchment pad would not be able to contain the spill In this case
temporary berm would need to be constructed Absorbent diapers or floor
sweep would be used in an effort to limit and contain the spill The soil would
be cleaned up and placed in the authorized disposal area in Cell
1.7 2.4 Truck Unloading
In the event of truck accident resulting in an overturned vehicle in the mill
area proper reporting and containment procedures will be followed when
warranted such as when oil or diesel fuel is spilled Proper clean-up
procedures will be followed to minimize or limit the spill The spill may be
temporarily bermed or localized with absorbent compounds Any soils
contaminated with diesel fuel or oil will be cleaned up and placed in the
authorized disposal area in Cell
1.8 SPILL DISCOVERY AND REMEDIAL ACTION
Once chemical or petroleum spill has been detected it is important to take
measures to limit additional spillage and contain the spill that has already
occurred Chemical or petroleum spills will be handled as follows
The Shift Foreman will direct efforts to shut down systems if
possible to limit further release
The Shift Foreman will also secure help if operators are requiring
additional assistance to contain the spill
The Shift Foreman is also obligated to initiate reporting procedures
Once control measures have begun and personal danger is
minimized the Shift Foreman will notify the Production
Superintendent Maintenance Superintendent or Mill Manager
The Production or Maintenance Superintendent will notify the Mill
Manager who in turn will notify the Environmental Health and Safety
Manager
The Mill Manager will assess the spill and related damage and direct
remedial actions The corrective actions may include repairs clean
up disposal and company notifications Government notifications
may be necessary in some cases
If major spill continues uncontrolled these alternatives will be considered
Construct soil dikes or pit using heavy equipment
Construct diversion channel into an existing pond
Start pumping the spill into an existing tank or pond
Plan further clean-up and decontamination measures
1.9 SPILL INCIDENT NOTIFICATION
1.9.1 External Notification
As stated in Section 1.1 spills are not expected to reach navigable waters of
the United States If spill of reportable quantity occurs then mill and
corporate management must be notified and they will evaluate whether or not
the following agencies must be notified
EPA National Response Center 1-800-424-8802
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah 801/538-7200
Water Quality Division 801/538-6146
In case of tailings dam failure contact the following agencies
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah Natural Resources 801/538-7200
1.9.2 Internal Notification
Internal reporting requirements for incidents spills and significant spills are
as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions and accidents
Government investigations information requests or enforcement
actions
Private actions or claims corporate or employee
Deviations from corporate policies or government requirements by
management
Which have or could result in the following
Death serious injury or adverse health effects
Property damage exceeding $1000000
10
Government investigation or enforcement action which limits
operations or assesses penalties of $100000 or more
Publicity resulted or anticipated
Substantial media coverage
Report At The Beginning Of The Next Day
Event Criteria
Was reported to government agency as required by law
Worker employee or contractor recordable injury or illness associated
with release
Community impact-reported or awareness
Publicity resulted or anticipated
Release exceeding the reportable quantities listed in Section 1.5 for
each specific process material waste or by-product
In the event of spill of reportable quantity the Mill Manager is required to
call the Corporate Environmental Manager or the President and Chief
Executive Officer The individual first discovering the spill will report it to the
Shift Foreman Production Superintendent or Maintenance Superintendent
who will in turn ensure that the Mill Manager is notified The Environmental
Health and Safety Manager will also be contacted by the Mill Manager
Name Title Home Phone
Mill Personnel
Richard Bartlett Interim Mill Manager 435 678-2495
Wade Hancock Maintenance Foreman 435 678-2753
David Turk Environmental Health and
Safety Manager 435 678-7802
N/A Production Superintendent
N/A Maintenance Foreman
Scot Christensen Mill Shift Foreman 435 678-2015
Corporate Personnel
Ronald Hochstein President and Chief Operating Officer 604 377-1167
David Frydenlund Vice President and General Counsel 303 221-0098
In the event the next person in the chain-of-command cannot be reached
then proceed up the chain-of-command to the next level Table 1.0 shows the
organizational chart for the mill site
11
1.10 RECORDS AND REPORTS
The following reports and records are to be maintained in Central Files by the
Environmental Health and Safety Manager for inspection and review for
minimum of three years
Record of site monitoring inspections
Daily Tailings Inspection Data
Weekly Tailings Inspection and Survey
Monthly Tailings Inspection Pipeline thickness
Quarterly Tailings Inspection
Tank to soil potential measurements
Annual bulk oil and fuel tank visual inspections
Tank and pipeline thickness tests
Quarterly and annual PCB transformer inspections if transformer
contains PCBs
Tank supports and foundation inspections
Spill Incident Reports
Latest revision of SPCC plan
1.11 PERSONNEL TRAINING AND SPILL PREVENTION
PROCEDURES
All new employees are instructed on spills at the time they are employed and
trained They are briefed on chemical and petroleum spill prevention and
control They are informed that leaks in piping valves and sudden
discharges from tanks should be reported immediately Abnormal flows from
ditches or impoundments are of immediate concern In addition safety
meeting is presented annually by the Environmental Health and Safety
Manager to review the SPCC plan
1.11.1 Training Records
Employee training records on chemical and petroleum spill prevention are
maintained in the general safety training files
1.11.2 Monitoring Reports
Shift logs shall provide checklist for inspection items
12
1.12 REVISION
This procedure is to be reviewed by the mill staff and registered
professional engineer at least once very th ree years and updated when
circumstances warrant revision
1.13 Summary
Below is table listing the specific reportable quantities associated with the
major chemical and petroleum products on-site
CHEMICAL REPORTABLE
QUANTITY RQ
AMMONIA 100 POUNDS
AMV 1000 POUNDS
SODIUM
HYDROXIDE
1000 POUNDS
SODA ASH No Reportable
Quantity
SODIUM
CHLORATE
400 GALLONS
SULFURIC ACID 1000 POUNDS
VANADIUM
PENTOXI DE
1000 POUNDS
KEROSENE 100 GALLONS
OIL No Reportable
Quantity
PROPANE No Reportable
Quantity
DIESEL
UNLEADED
FUEL
100 GALLONS
13
1.14 MILL MANAGER APPROVAL
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with the Standard Operating Procedures
currently in effect
Richard Bartlett
Interim Mill Manager
1.15 CERTIFICATION BY
REGISTERED PROFESSIONAL ENGINEER
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with good engineering practices
Harold Roberts
Registered Professional Engineer
State of Utah No 165838
14
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Rome Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.166
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Rome Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE 2.0
REAGENT TANK LIST
QUANTITY REAGENT CAPACITY GAL
DIESEL 250
KEROSENE 10152
USED/WASTE OIL 5000
DIESEL 6000
UNLEADED 3000
PROPANE 30000
AMMONIA 31409
SODIUM HYDROXIDE 19904
SODA ASH SOLUTION 16921
SODA ASH SHIFT 8530
SODIUM CHLORATE 17700
SODIUM CHLORATE 10500
SULFURIC ACID 1600000
SULFURIC ACID 269160
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
bTtr\t_-
Aluminum nitrate 2270 kg 1.6 kg
Ammonium bifluoride 45.4 kg 2.27 kg
Ammonium chloride 2270 kg 2.27 kg
Ammonium oxalate 2270 kg 6.8 kg
Ammonium thiocyanate 2270 kg 7.8 kg
Antimony potassium tartrate 45.4 kg 0.454 kg
n-Butyl acetate 2270 kg
Carbon tetrachloride 4.54 kg 1.0
Cyclohexane 454 kg 24
Ferric chloride 454 kg 6.810 kg
Ferrous ammonium sulfate 454 kg 0.57 kg
Potassium chromate 4.54 kg 0.114 kg
Sodium nitrite 45.4 kg 2.5 kg
Sodium phosphate tribasic 2270 kg 1.4 kg
Zinc acetate 454 kg 0.91 kg
ChethiŁa11oIatiIei4and/1 RQLCi
cct Cr
Chloroform 4.54 kg
Formaldehyde 45.4 kg IL of 37%solution
Nitrobenzene 454 kg 12
Toluene 454 kg 12
-j
1ttti
.c-tt
7Uaflfl$SStc1c
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
CHEMICAU C941y4--C1z _________
Acetic Acid Glacial 1000 lbs
COMPOUND
gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 Ibs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs 5kg IlIbs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
REAGENT QUANTITYIN
REAGENT YARD
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfloc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT -.-QUANTITYINI
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
GR
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L
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DE
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T
A
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N
A
1
I
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N
PA
D
DIE
S
E
L
SA
M
P
L
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PL
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o
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Figure
White Mesa Mill
Mill Site Drainage Basins
APPENDIX
WHITE MESA MILL
EMERGENCY RESPONSE PLAN
EMERGENCY RESPONSE PLAN
REVISION 1.1
Denison Mthes USA Corp
t1TL--aa...r aimYVILLICIVICScLIVIIII
landing Utah
April14 1986
REVISED
February 16 2007
Distribution List
Ron Hochstein
Rich Bartlett
David Turk
Michael Spillman
Mill Shift Foremen
Blanding Fire Department
San Juan County EMS Coordinator
State of Utah Department of Radiation Control
Revision Date Januaiy 162006
TABLE OF CONTENTS
Page
Number
1.0 Introduction
2.0 White Mesa Mill Background
3.0 Plan Objectives
4.0 Description of Facilities
4.1 Fire Water Supply and Alarm Systems
4.2 Office Building and Laboratory
4.3 Solvent Extraction Building
4.4 Mill Building
4.5 Maintenance Shop/Warehouse/Change Room Building
4.6 Reagent and Fuel Storage
4.7 Boiler House
4.8 Sample Plant
5.0 Organization and Responsibilities
5.1 Mill Manager/Incident Commander
5.2 Operations Superintendent
5.3 Radiation Safety Officer/Fire Chief
5.4 Maintenance Supervisor
5.5 Laboratory Supervisor
5.6 Shift Foremen
5.7 Scale House Personnel
5.8 Emergency Response Teams
6.0 Specific Emergencies 10
6.1 Fire 10
6.2 Chemical or Gas Release 10
6.3 Earthquake 10
6.4 Terrorist/Bomb Threat 10
6.5 Tailings Dam Break and Major Floods 10
7.0 Evacuation Procedure 11
7.1 Notification II
7.2 Assembly 11
7.3 Specific Procedures for Operations Personnel II
8.0 Off-Site Emergency Equipment/Personnel Release 11
9.0 Emergency Equipment 12
9.1 Fire Hose 12
9.2 Self Contained Breathing Apparatus
12
9.3 Spill Clean-up Equipment 12
9.4 Fire Fighting PPE 12
10.0 Emergency Transportation 13
11.0 Emergency Evacuation Drills 13
EXHIBITS
Emergency Notification List E-
Internal Notifications E-2
Site Layout Map E-3
Main Shut-off Valves E-4
APPENDICES
Emergency Procedure Response to Fire A-I
Emergency Procedure Response to Chemical or Gas Release A-2
Emergency Evacuation Procedure A-3
FIGURES
Fire System Schematic F-I
ii
INTERNATIONAL URANIUM USA CORPORATION
Rev No R-1
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
INTRODUCTION
This Emergency Response Plan is written not only to comply with Federal State and local
regulations but even more importantly to reduce the risk to our employees and that of the
community in regards to Health Safety and Environmental Emergencies
This plan includes the following
evaluation of the potential risks for fire explosions gas releases chemical spills and
floods including tailings dam failure
specific emergency programs for each potential event
definition of administrative response actions and
definition of the emergency response contacts both internal and external
The White Mesa Mill the Mill operates under the following regulatory agencies
Utah State Department of Environmental Quality Division of Radiation Control
Mine Safety and Health Administration
Environmental Protection Agency
Utah State Department of Environmental Quality Division of Air Quality and
Utah State Division of Natural Resources Bureau of Dam Safety
WIIITE MESA MILL OVERVIEW
The Mill processes conventional uranium or uranium/vanadium ores to recover uranium and
vanadium In addition to the processing of conventional ores the Mill also processes alternate
feed materials using similar process steps and chemicals The conventional ore is stored on the
Ore Pad shown in Exhibit Alternate feed materials are also stored on the Ore Pad and may
be stored in bulk form lined burrito bags liners or drums The descriptions of each alternate
feed material are maintained by the Mills Radiation Safety Officer
The Mill utilizes semi-autogenous grind circuit followed by hot sulfuric acid leach and
solvent extraction process to extract uranium and vanadium from ores using large amounts of
sulfuric acid sodium chlorate kerosene amines ammonia and caustic soda in the process The
reagent storage tank locations are described in further detail in Section 4.6
Emissions from the Mill process are in the form of air emissions from exhaust stacks and
solid/liquid tailings which are stored in the Mills tailings cells located west/southwest of the
main Mill building The major exhaust stack parameters are shown in the following table
Description
Height
ft from surface
Diameter
inches
Estimated Flow Rate
cfm
Leach Exhaust -400 36 13700
Yellow Cake Drying
stacks
85 18 4000 per stack
Vanadium Roasting
Fusion
85 38 4100
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There are also smaller exhaust stacks associated with the Laboratory in the Mill Administration
building and the boiler exhaust stack
The Mills tailings cells are comprised of four below grade engineered cells Cell 1-I and
4A Liquids are stored in Cell 1-I and Cell the active tailings cell The liquid in the tailings
cells is very acidic In addition to the tailings cells there is also an emergency lined catchment
basin west of the Mill building Solutions in this basin or the tailings cells should not be used to
fight fires in the Mill facility
The products of the Mill include ammonium metavanadate AIvIV vanadium pregnant liquor
VPL vanadium pentoxide 1205 and yellowcake or uranium concentrate U308 The V2O5
and U308 products are packaged in steel drums for shipment The AMY is packaged in either
steel drums or super-saks while the VPL is sold in liquid form in bulk
Master files containing Material Safety Data Sheets for all materials in use at the Mill are
maintained at the Safety Office Mill Maintenance Office Mill Laboratory and Mill Central
Control Room Copies are also on file at the Blanding Clinic Doctors Offices Blanding Fire
House and Office of the San Juan County Emergency Medical Coordinator
The nearest residence to the Mill is approximately one mile to the north of the Mill the next is
residence approximately two miles north of the Mill followed by the community of White Mesa
about 3.5 miles to the south The City of Blanding is located approximately miles to the
northeast
The Mill site is near Utah State Highway 191 and can be accessed by paved access road from
the highway to the Mill facilities
PLAN OBJECTIVES
The primary objectives of this plan are
To save lives prevent injuries prevent panic and minimize property/environmental
damage to the lowest possible level
To evacuate and account for all people in the area including visitors truck drivers
contractors etc
To provide assembly areas that are as safe as possible and which can be reached without
traveling through hazardous area Assembly areas will be properly manned to deal with
sick or injured persons and provisions will be made to evacuate those persons to proper
shelter
To make adequately trained personnel available to cope with rescue and recovery
operations as directed by the Incident Commander
DESCRIPTION OF FACILITIES
The Mill facilities are shown on the Site Layout Map included as Exhibit
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4.1 Fire Water Supply and Alarm Systems
4.1.1 Fire Water Supply
The fire water supply facilities include
400000 gallon Storage Tank of which 250000 gallons are reserved for fire emergencies
Centrifugal diesel driven pump rated at 2000 gpm at 100 psi This pump starts
automatically when the pressure in the fire main drops below 100 psi See Figure Fire
System Schematic
When more water is needed for an emergency an additional source is the Recapture Reservoir
supply pipeline which can be utilized in emergencies at rate of about 1200 gpm
4.1.2 Alarm System
The alarm systems include the following
public address system
hand held radios
siren
4.2 Office Building and Laboratory
4.2.1 Office Building
The office building approximately 10000 square feet contains the administration offices
radiation health and safety offices and the Mill laboratory The central file vault and the main
computer system are also in this building The ambulance is kept on the west side of the office
building near the safety office entrance
4.2.2 Laboratory
The laboratory facilities contain the following
three flammable cabinets keys required
chemical storage room south of main lab
six fume hoods hoods 12 and are in the center of the laboratory and hoods and
are along the west wall Hoods and are no longer in service Hoods and are on
the west side and are on the east side of the center cluster of hoods with being in
front Only hoods and may be used for perchloric acid
outside laboratory chemical storage north of office building key required
perchloric acid storage vault located underground west of office building key required
wide variety of chemicals in small quantities are located in the laboratory These chemicals
range from acids to bases along with flammable metal compounds and peroxide forming
compounds Oxidizers and organic chemicals which have strong potential of producing
harmful vapors if the containers are damaged to the point that the chemicals are exposed are
stored in storage room in the laboratory There are no acids stored in this storage room The
acids including but not limited to sulfuric nitric acetic perchloric phosphoric and hydrochloric
acids are stored in the main laboratory area in 2.5 liter or 500-mi bottles MSDS books for all
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chemicals in the laboratory are located in the Laboratory Safety Department Mill Maintenance
office and Mill Central Control room
4.2.3 Electrical
Electrical transformers and electrical switches are located in the laboratory at the east end of the
chemical storage room
4.2.4 Fire Protection System
The fire protection systems in the office building and laboratory include
fire hose station located on the east end of the office building The station includes two
sets of turnout gear two SCBA units and Incident Commander materials
automatic wet sprinkler system which is actuated at 212
portable dry chemical extinguishers strategically located throughout the building
4.3 Solvent Extraction Building
The solvent extraction SX building approximately 21000 square feet houses the uranium and
vanadium solvent extraction circuits and the ELUEX circuit The SX circuits may contain up to
200000 gallons kerosene 757000 liters which has flash point of 185
Associated equipment in the SX building includes temporary boiler located at the southwest
end of the SX building which maintains the temperature for the fire system
Chemicals which may be encountered in the SX building include
Kerosene
Caustic Soda
Anhydrous Ammonia
Sulfuric Acid
Salt Brine
Soda Ash
Ammonium Sulfate
Amines
Alcohol
Sodium Chlorate
Sodium Vanadate
Propane
The VPL product is stored in the SX building
4.3.1 Electrical
All electrical switches are located outside in the MCC room north of the SX building The main
control panel for all of the equipment is located in the Central Control Room in the main Mill
building
4.3.2 Fire Protection System
The SX building fire protection systems include
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wet AFFF foam sprinkler system with heat actuated sprinkler heads that release at
12F
portable dry chemical extinguishers strategically located throughout the building
For fire hydrant and hose cabinet locations in the SX building refer to the Fire System Schematic
included as Figure in this Plan
4.4 Mill Building
The mill building approximately 22000 square feet contains process equipment related to
grind leach counter current decantation precipitation drying and packaging of uranium and
vanadium products
Chemicals which may be encountered in the mill building include
Caustic Soda
Aithydrous Ammonia
Sulfuric Acid
Soda Ash
Ammonium Sulfate
Sodium Chlorate
Sodium Vanadate
Propane
The finished products which are contained in the mill building include AMY V205 and U308 or
yellowcake
4.4.1 Electrical
The main electrical switch gear is located west of the SAG mill on the ground floor in the north
west corner of the mill building Circuit control panels are located in the SAG mill control room
the central control room the vanadium roaster control room and the AMY area
4.4.2 Fire Protection System
The main mill building fire protection systems include
portable dry chemical extinguishers strategically located throughout the building
water hoses throughout the building
For fire hydrant and hose cabinet locations in the Mill building refer to the Fire System
Schematic included as Figure of this Plan
4.5 Maintenance Shop/Warehouse/Change Room Building
This building approximately 20000 square feet contains the main maintenance shop area
located on the north end of the building the main warehouse located on the south end of the
building and the personnel change rooms and lunch/training room located on the extreme south
end of the building on the ground and second floors
Within the maintenance shop area are the following work area and specialty shops
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the main maintenance shop area contains welding and cuffing equipment lathes presses
and drill presses
carpenter shop which contains various saws and planes Fiberglass work is also done
within this shop area and it is located at the northwest end of the maintenance shop area
an electrical shop which is located south of the carpenter shop
heavy equipment maintenance shop area is located at the north end of the maintenance
shop in the center of the building
rubber room for rubber lining of equipment is located east of the equipment shop area
the maintenance shop office instrument shop and tool room are located at the south end
of the maintenance shop area
The warehouse area contains primarily dry good storage for repair parts and consumables for the
operation of the Mill There is an electrical water heater for the change room which is located in
the warehouse area at the south end
Within the warehouse and maintenance shops there are some oils and chemicals stored in the
following locations
small quantities of flammable material such as starting fluid and spray paint are kept in
the warehouse
drums of new oil and anti-freeze are stored along the east wall of the equipment
maintenance area and on the east side of the warehouse on oil storage racks
used oil is stored in tank located northeast of the equipment shop The tank has
capacity of approximately 5800 gallons
in the main maintenance shop area and the rubber room there are flammable storage
cabinets and east of the warehouse there is trailer which is used to store flammable
items such as rubber cements paints and fiberglass resins
compressed gas cylinder storage both empty and full is located outside east of the
maintenance shop
4.5.1 Electrical
The main electrical circuit breaker for the maintenance shop and warehouse building is located
on the east wall inside the Maintenance shop Auxiliary electrical panels for the change room
and warehouse are located in the southwest corner of the warehouse area
4.5.2 Fire Protection System
The fire protection system within the maintenance shop/warehouse/change room building
includes
wet automatic sprinider system that releases at 212
portable dry chemical extinguishers strategically located throughout the maintenance
area warehouse area and the change room and lunch room
For fire hydrant and hose cabinet locations refer to the Fire System Schematic Figure
4.6 Reagent and Fuel Storage
The following lists the reagents and fuel stored at the Mill site
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sulfuric acid tank located northwest of the mill building which has capacity of
approximately 1.4 million gallons
storage tank for propane is located on the north edge of the mill site northwest of the
mill building It has storage capacity of 30000 gallons
four sodium chlorate tanks located east of SX building north of the office building and
east of the pulp storage tanks The two tanks east of the SX building are for sodium
chlorate storage and the other two tanks are for dilution of the sodium chlorate
two anhydrous ammonia tanks located east of the SX building with capacity of 31409
gallons each
three kerosene tanks located east of the SX building with capacity of 10152 gallons
each
one caustic soda tank north of the SX building with capacity of 19904 gallons
three soda ash tanks which are located east of the SX building One tank is the dry soda
ash tank with capacity of 70256 gallons Two of the tanks are soda ash dilution tanks
with capacities of 16921 gallons each
diesel fuel and gasoline are stored in two tanks located on the eastern side of the ore pad
The gasoline storage capacity is 3200 gallons while diesel storage capacity is 8000
gallons
Other reagents are stored in steel barrels or super sacs in reagent yard located east of the office
building Typical reagents which are stored in this yard include
polymers and flocculants
boiler feed water chemicals
methanol
tributyl phosphate
dirty soda ash and ammonium sulfate
SX amines and emulsion breakers
decyl alcohol
minimal amounts of acid in barrels
used oil in drums and overpacks
4.7 Boiler Facilities
The main building approximately 12400 square feet is located on the west side of the Mill site
and contains air compressors and water treatment facilities To the north of the main building is
building which houses propane-fired boiler The vanadium oxidation tank oxidation
thickener and pH adjustment tank are located south of the boiler house facilities
4.7.1 Electrical
The main electrical panel for the boiler house is located outside of the building on the south
wall
4.7.2 Fire Protection System
The fire protection system for the boiler facilities is comprised of strategically located portable
dry chemical extinguishers
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4.8 Sample Plant
The sample plant building approximately 8000 square feet is located on the ore pad east of the
maintenance shop/warehouse building The sampling plant equipment has been removed from
the building and it is cunently used as storage area for maintenance
4.8.1 Electrical
The electrical panel for this building is located on the east wall upstairs
4.8.2 Fire Protection System
There are no extinguishers or sprinider systems in the sample plant
ORGANIZATION AND RESPONSIBILITIES
The organizational chart for an emergency situation is illustrated in Figure
5.1 Mill Manager/Incident Commander
The Incident Conunander has the responsibility for
preparing an Emergency Plan
communicating the Plan
directing activities during emergencies and
reporting to local State and Federal authorities
The Incident Commander will stop routine radio usage upon learning of an emergency and set up
the base station in safe location for directing activities Radio usage will be limited to the
emergency The Incident Commander has the responsibility to contact all outside services
The Incident Commander has the responsibility to account for all employees at the Mill using
the assistance of supervisors and/or any International Uranium USA Corporation IUSA
personnel The Incident Commander has the responsibility for the news media and reports
directly to the President of IUSA
5.2 Mill General Superintendent
The Mill General Superintendent has the responsibility of directing outside emergency personnel
and has the responsibility for plant security and will report directly to the Incident Commander
The Mill General Superintendent will act as Incident Commander in the absence of the Mill
Manager
5.3 Radiation Safety Officer/Fire Chief
The Radiation Safety Officer will direct rescue operations and provide the necessary emergency
medical personnel and facilities to cope with the emergency Adequately trained fire crews and
operable emergency equipment will be maintained at all times
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INTERNATIONAL URANIUM USA CORPORATION
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As Fire Chief the Radiation Safety Officer has the responsibility to maintain trained fire crews
and operable equipment mobilize and direct the fire crews and equipment in fire emergency or
one containing the threat of fire and to assist in evacuation and rescue or recovery operations
In the absence of the Radiation Safety Officer the Mill Safety Coordinator will assume these
duties
5.4 Maintenance Supervisor
The Maintenance Supervisor will direct all personnel in evacuation and in activities to cope with
the emergency including isolation of utilities and providing technical advice as needed The
Maintenance Supervisor will be assisted by the Mill Safety Coordinator
5.5 Laboratory Supervisor
The Laboratory Supervisor has the responsibility to direct and account for all office personnel
including IUSA personnel and office visitors in evacuation and in activities to cope with the
emergency In case of mill tour the Supervisor accompanying the tour will be responsible for
evacuation of visitors
5.6 Shift Foremen
Shift Foremen are in charge until the Incident Commander arrives and are responsible for all
functions listed above Shift Foremen have the responsibility to account for all of their people in
addition to any visitors contractors etc in their areas and report to the Incident Commander or
in the absence of the Incident Commander to administer all of the above duties
5.7 Scale House Personnel
Scale house person on shift will be responsible to account for ore truck drivers and reagent truck
drivers
5.8 Emergency Response Teams
The response crew for each operating shift will normally consist of the following operators under
the direction of the shift foreman This organization may be changed for individual shifts subject
to the approval of the Fire Chief
5.8.1 Operational Mode
Leach Operator
CCD Operator
Solvent Extraction Operator
Mill Trainee
5.8.2 Non-Operational Mode
Shift Foreman
Operations Personnel
Maintenance Personnel
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Rev No R-1
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page 10 of 13
Figure
Emergency Response Organizational Structure
Incident Commander
Mitt Manager
Director of Security
Operations Supedntendent
Fire Chief
Radiation Safety Officer
Shift Foremen Emergency Response Teams Lab Supervisor
Operational Mode Non-Operational Mode
Leach Operator CCD Operator Shift Foreman Operations Personnel
SX Operator Mill Trainee Maintenance Personnel
SPECIFIC EMERGENCIES
The following details procedures to be followed during specific emergencies but are not limited
to the following
6.1 Fire
Should fire occur the procedure outlined in Appendix for reporting and responding to fires
will be followed Particular areas of concern include
Solvent Extraction Building
Propane Tanks
Lab or Lab Storage Area
6.2 Chemical or Gas Release
The procedures for response to chemical or gas release are outlined as Appendix
6.3 Earthquake
Although this is highly unlikely an earthquake could occur at the Mill severe earthquake
could cause buildings and other structures to collapse chemical and/or gas releases major fires
as well as general panic In the event of major earthquake the evacuation procedures outlined
in Appendix will be followed
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INTERNATIONAL URANIUM USA CORPORATION
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6.4 Terrorist/Bomb Threat
In the event that any person should receive threat of bomb the following evacuation
procedure should be followed
Notify any person of authority i.e Superintendent Foreman Radiation Safety Officer
who will immediately notify law enforcement authorities and evacuate the threatened
area
Evacuate all persons from the affected area and stop all radio transmissions
6.5 Tailings Dam Break and Major Floods
Flood water breaching tailings embankments presents one of the greatest dangers for the sudden
release of tailings solids and impounded water The tailings cells are designed with sufficient
freeboard three feet to withstand back-to-back 100-year storm events or 40%of the probable
maximum flood PMF followed by the 100-year storm event The flood design is equivalent to
15 inches of rainfall In addition the tailings dikes were designed in accordance with U.S NRC
regulations and allow sufficient margin of safety even in the event of an earthquake
The possibility of floods resulting from Westwater Creek Cottonwood Creek and Corral Creek
causing dam failure is extremely remote
The tailings cells and dikes are inspected on both daily and shift basis
Discharges from dike failure would extend three miles before leaving IUSAs property In the
event of dam failure large operating equipment will be mobilized to construct temporary
earthen dikes or berms downgradient to the failed dike In addition the State of Utah
Department of Radiation Control Executive Secretary the Executive Secretary MSIIA and
State of Utah Department of Natural Resources Division of Dam Safety shall be notified
In the event of seismic rupture of tailings slurry pipelines the released slurry will be contained
in the tailings cells regardless of the quantity released
EVACUATION PROCEDURE See Appendix
7.1 Notification
Employees will be notified to evacuate the area by dialing 184 on any area telephone and
announcing that the Mill should be evacuated This announcement will be repeated twice When
the paging system cycles through the evacuation siren continuous frequency will automatically
sound for approximately forty-five seconds and then automatically shut off allowing
communications by radio from that point If the 184 number is dialed accidentally the
evacuation alarm may be canceled by disconnecting the phone until the page cycle ends then re
dial 184 See Exhibits and
7.2 Assembly
When the evacuation alarm sounds or when personnel are verbally notified by radio or other
means all personnel will assemble at
The parking lot south of the office
PAdmin\Master SOPs\Book 16_Emergency Response Plan \Ernergency Response Plan Rev 09.29.05.doc 11
INTERNATIONAL URANIUM USA CORPORATION
Rev No R-l
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The scalehouse
North side of Tailings Cell or
North of the Mill
Assembly site will depend upon conditions i.e nature of the emergency wind conditions etc
The Fire Chief or Shift Foreman will specify the appropriate assembly site
7.3 Specific Procedure for Operations Personnel
See specific emergency shutdown procedure for Operations by area under the relevant
Operating Procedure for your area
All employees not mentioned under Operating Procedures are to immediately report to
the assembly area and congregate by crew so that all persons can be accounted for As
employees leave their work areas they must pass the word to evacuate to any persons
who may not be aware of the emergency
After the Mill has been detennined to be safe for re-entry employees will be verbally
notified to return to their work stations
Off-Site Emergency Equipment/Personnel Release
Any emergency response equipment or personnel that enter the Restricted Area in response to an
incident will be scanned and decontaminated prior to leaving the site according to the procedures
included in PBL-9 End Dump Trailer Acceptance ilandling and Release Any equipment will
be decontaminated according to the requirements found in Table of the Nuclear Regulatory
Commissions NRCs Policy and Guidance Directive FC-85-23 Guidelines for
Decontamination of Facilities and Equipment Prior to Release for Unrestricted Use or
Termination of Licenses for Byproduct Source or Special Nuclear Material issued May 1987
Injured personnel should be evaluated for radiation contamination if there was potential for
contamination at the earliest convenience Should it be necessary contaminated articles will be
gathered by the radiological staff after medical treatment has been rendered If the personnel
cannot be decontaminated notify the clinic/hospital personnel in advance
EMERGENCY EQUIPMENT
Emergency equipment for the Mill is provided as follows
9.1 Fire Hose
Fire hose cabinets are located at the following sites with minimum of 300 feet of 2-1/2 hose
two spanner wrenches spray nozzles and one hydrant wrench
South of SX
West of CCD
North of Mill Building
East of pulp storage tanks
Northwest of Maintenance Shop
West of Warehouse
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East of office building
9.2 Self Contained Breathing Apparatus
Two Self-Contained Breathing Apparatus
are located at each of the following locations
Hose station east of office building
Hose Station South of SX
North End SX Outside Wall
North end of Mill building outside wall
9.3 Spill Clean-up Equipment
Barrels of soda ash are located throughout the Mill to be used in case of chemical spill Soda
ash is also stored in bulk if needed There are also few drums of absorbent stored near the
laboratory The laboratory also contains acid spill kits and absorbent materials to be used in case
of spill
9.4 Fire Fighting PPE
Two complete sets of turnout gear for fire fighting and/or emergency extrication are located in
the Fire Hose Station located on the east side of the office building
9.5 Maintenance of Emergency Equipment
Fire extinguishers are inspected on an annual basis as well as the fire pump system The Mill
Safety Coordinator performs regular spot checks on the emergency equipment locations to ensure
that all of the equipment is in place
10 EMERGENCY TRANSPORTATION
One filly-equipped First Responder Unit Ambulance located west of the office building
Other motor pool vehicles on the property will be utilized as needed in emergency situations with
support as needed from the local Emergency Medical Services
11 EMERGENCY DRILLS AND TRAINING
Quarterly drills as required by MSHA are prepared by the Safety and Radiation Departments to
monitor performance of personnel responding to emergency situations Each drill will be
enacted upon one or more of the potential scenarios by this plan The drill and evacuation
activities are documented by the Mills Safety Coordinator and maintained within plant files
Management will review all drills at quarterly ALARA Committee Meetings
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc 13
EXHIBIT
EMERGENCY NOTIFICATION LIST
ATTEND TO ANY INJURED PERSONS AND NOTIFY THE SUPERVISOR
Give artificial respiration if necessary
Control bleeding
Treat for shock
Immobilize fractures and stabilize for transportation
Scan the injured for excessive alpha prior to transporting if time allows
If alpha is excessive or there is no time to scan notify the clinic/hospital personnel and the
Radiation Safety Office
THE SUPERVISOR OR HIS DESIGNEE WILL NOTIFY THE FOLLOWING AS NEEDED
Blanding Clinic 678-2254 or 678-3434 930 400
San Juan Hospital Monticello ...678-2830 or 587-2116 364 1st
EMT and CPR TRAINED The following personnel should be contacted if they are on-site in the
event of an emergency to aid in the event of any injuries to personnel
David Turk EMT and CPR trained
Mike Spillman CPR trained
AMBULANCE SERVICE
Blanding Dial 911
If the Company Ambulance is used an attendant must ride with the injured in addition to the driver
except where the injured could normally be transported in car or pickup
OTHER EMERGENCY NUMBERS
Fire Department Dial 911 or 678-2313
County Sheriff Dial 911 or 587-2237
Highway Patrol Dial 911 or 587-2000
Blanding Police Dial 911 678-2916 or 678-2334
MANAGERS
The Supervisor will notify one of the following of all incidents
R.E Bartlett 435-678-2495
Turk 435-678-7802 or 435-459-1068
Spillman 435-678-2761
MEMBER OF MANAGEMENT WILL NOTIFY THE PROPER REGULATING AGENCIES
AS REQUIRED FOR EACH INCIDENT
State of Utah Department of Radiation Control 801-536-4250
MSHA Field Off.--801-524-3450 Dist Off 303-231-5465
MSHA Arlington 800-746-1553
State Emergency Response Comm 801-538-3400
State of Utah Natural Resources Dam Safety 801-538-7200
National Response Center 800-424-8802
Utah Poison Control Center 800-456-7707
Notification of surrounding communities and or residences will be handled by the appropriate agencies as
required by EPCRA Emergency Planning and Community Right to Know Act
Revision Date January 16 2006 Ed
EXHIBIT
INTERNAL NOTIFICATIONS
Internal reporting requirements for Incidents Spills and Significant Events are as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions or other accidents
Government investigations information requests or enforcement actions
Private actions or claims corporations or employees
Deviations from Corporate policies or government requirements by Management
Other significant events which have resulted or could result in
Death serious injury or adverse health effect employees or public
Property damage exceeding $1000000
Government investigation or enforcement action limiting operation or penalties
of $100000 or more
Significant criminal actions
Substantial media coverage
Unscheduled down time of more than 24 hours
Report at the Beginning of the Next Business Day
Incident Criteria
Was reported to government agency as required by law
Worker IIJSA or contractor recordable injury or illness associated with release
Community impact reported or awareness
Publicity resulted or is anticipated
Release of process material waste or product in excess of the Reportable
Quantities listed in Section 1.5 of the Spill Prevention Control and
Countermeasures Plan
The local manager in charge is to call Ron Hochstein or Dave Frydenlund
Name Title Office Phone Home Phone
Ron Hochstein President and COO 303-628-7798 office
604-931-6334 home
604-377-1167 cell
David Frydenlund V.P and General Counsel 303-389-4130 office
303-221-0098 home
303-808-6648 cell
Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 02.14.07 E-2
EXHIBIT
SITE LAYOUT MAP
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-3
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EXIIIBIT
MAIN SHUT-OFF VALVES
During an emergency this list should be used along with Site Layout Map Exhibit to locate
tanks and valves associated with these tanks
REAGENT SHUT-OFF VALVE LOCATIONS
Sulfuric Acid
Main located south side of acid tank
East acid pump discharge valve
West acid pump discharge valve
Main leach area located 25 feet west of Denick screens next to walkway
1-1/2 Main SX area located south of Central Control room
Ammonia
Main east tank located on end at bottom
Main west tank located on end at bottom
Valve located on top of tank east tank
Valve located on top of tank west tank
Kerosene
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Pump discharge valve
Soda Ash
Main valve located at bottom of tank dry storage
Main valve located at bottom of tank on 30%dilution tank
Main valve locate at bottom of tank on dilution tank
Salt
Main valve located at bottom of tank
Caustic Soda
Main valve located at bottom of tank east and west between supports
PAAdmin\Master SOPs\Book 16_Emergency Response PlarAEmergency Response Plan Rev 09.29.05.doc E-4
EXHIBIT
MAIN SHUT-OFF VALVES
Sodium Chlorate
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Propane
Main located 15 feet east of tank
Main located on pipe off top of tank
Main located at bottom of tank also fill pipe
PLANT UTILITY SHUT-OFF VALVE LOCATIONS
Process Water
Main valve located on west side of water storage tank
Discharge valve off service water pump east
Discharge valve off service water pump west
Mill process water main located east wall by SAG mill
Fire Water
Main valve located west side of water storage tank
Emergency fire pump discharge valve to fire system
Emergency fire pump discharge valve to header west side of pump house
Main valve located south of Central Control room for SX and boilers
Potable Water
Main suction from potable water storage tank
Main discharge from potable water storage tank
Main located at east wall by SAG mill
Main located south of Central Control room for SX Maintenance shop and offices
Steam
Main discharge valve for Superior boiler located at top of boiler
Main steam valve located south side of boiler house
P\AcImin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
EXHIBIT
MAIN SHUT-OFF VALVES
Plant Air
Main valve located at receiver tank in compressor room at boiler house
Main valve to mill building located south of Central Control room
PROCESS SHUT-OFF VALVE LOCATIONS
Pulp Storage
No valve located on west side of tank
No valve located on west side of tank
Preleach old No pulp storage valve located on west side of tank
Preleach Thickener
Main valve located underneath at center cone
Clarifier
Main valve located underneath at center cone
Main valve located underneath at center cone
CO Thickeners
Main valve located underneath at center cone of each thickener
PAdminMaster 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
APPENDIX
EMERGENCY PROCEDURE RESPONSE TO FIRE
The fire will be reported by dialing 185 on any telephone in the area and announcing the
location of the fife over the paging system This announcement will be repeated twice
for total of three announcements When the paging system cycles through the fire siren
alternating frequency will automatically sound for approximately forty-five seconds
then automatically shut off allowing radio communications to resume
Mobilize the fire crew
Evacuate all personnel
Rescue any victims of the fire do this only with properly trained and equipped personnel
Isolate utility lines affected by the fire
Extinguish the fire and post fife watch for flare-ups
Report the fire to proper local State Corporate and Federal agencies
In cases where the fire is not extinguished within thirty minutes of discovery the area
must be barricaded off after extinguishing and left undisturbed until released by MSHA
and IUSA management
Emergency off-site centers Blanding Fire House and Sheriffs office
landing Fire
350 West 200 South Blanding
Phone number is 911
Sheriffs Office
50 West 100 South Blanding
Phone number is 911 or 435 587-2237
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-I
APPENDIX
EMERGENCY PROCEDURE
RESPONSE TO CHEMICAL OR GAS RELEASE
chemical or gas release would most likely occur very suddenly The person who would first
witness chemical or gas release should immediately contact his supervisor who would initiate
the procedures outlined below
Activate evacuation alarm by using the dial 184 notification system Evacuate and
account for all personnel
Mobilize trained personnel and emergency equipment such as SCBAs first aid
equipment etc
Initiate rescue operations for any people who may be trapped by the release
Provide first aid and emergency medical care for any ill or injured persons
Initiate necessary steps to contain and/or neutralize the release such as spraying with
water fog turning off valves etc
Guard against possible fires by shutting off electrical circuits isolating gas lines and
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P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29 05.doc A-I
APPENDIX
EMERGENCY EVACUATION PROCEDURE
Activate evacuation alarm by using the dial 184 notification system Evacuate and account
for all personnel
Personnel are to assemble in one of the following areas
The parking lot south of the office building
The scalehouse
The north side of Tailings Cell or
North of the Mill
Mobilize trained personnel and emergency equipment such as SCBAs first aid equipment
etc
Initiate rescue operations for any people who may be trapped
Provide first aid and emergency medical care for any ill or injured persons
Guard against possible fires by shutting off electrical circuits isolating gas lines and
eliminating ignition sources from the affected area
P\Admin\Master 5OPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc A-i
FIGURE
FIRE SYSTEM SCHEMATIC DRAWING
P\Admin\Master SOPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc A-I
44
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STORM WATER
BEST MANGEMENT PRACTICES PLAN
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Blanding Utah
June 2008
Prepared by
Denison Mines USA Corp
1050 17th Street Suite 950
Denver CO 80265
TABLE OF CONTENTS
1.0 Purpose
2.0 Scope
3.0 Responsibility
4.0 Best Management Practices
4.1 General Management Practices Applicable to All Areas
4.2 Management Practices for Process and Laboratory Areas
4.3 Management Practices for Maintenance Activities
4.4 Management Practices for Ore Pad Tailings Area and heavy Equipment
Operations
Figures
Figure White Mesa Mill Site Map
Figure Mill Site Drainage Basins
Figure JUSA Mill Management Organization Chart
Figure IUSA Corporate Management Organization Chart
Tables
Table White Mesa Mill Management Personnel Responsible for Implementing
This BMPP
Appendices
Appendix White Mesa Mill Spill Prevention Control and Countermeasures Plan
Appendix White Mesa Mill Emergency Response Plan
Best Management Practices Plan
Revision 1.3 June 12 2008
1.0 INTRODUCTION/PURPOSE
Denison Mines USA Corp DUSA operates the White Mesa Uranium Mill the Mill in
Blanding Utah The Mill is net water consumer and is zero-discharge facility with respect to
water effluents That is no water leaves the Mill site because the Mill has
no outfalls to public stormwater systems
no surface runoff to public stormwater systems
no discharges to publicly owned treatment works POTWs and
no discharges to surface water bodies
The State of Utah issued Groundwater Discharge Permit No UGW3 70004 to DUSA on March
2005 As part of compliance with the Permit DUSA is required to submit Stormwater Best
Management Practices Plan BMPP to the Executive Secretary of the Division of Radiation
Control Utah Department of Environmental Quality This BMPP presents operational and
management practices to minimize or prevent spills of chemicals or hazardous materials which
could result in contaminated surface water effluents potentially impacting surface waters or
ground waters through runoff or discharge connections to stormwater or surface water drainage
routes Although the Mill by design cannot directly impact stormwater surface water or
groundwater the Mill implements these practices in good faith effort to minimize all sources of
pollution at the site
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
2.0 SCOPE
This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in
process operations laboratory operations and maintenance activities and minimize spread of
particulates from stockpiles and tailings management areas at the Mill Storage of ores and
alternate feeds on the ore pad and containment of tailings in the Mill tailings impoundment
system are not considered spills for the purposes of this BMPP
The Mill site was constructed with an overall grade and diversion ditch system designed to
channel all surface runoff including precipitation equivalent to Probable Maximum
Precipitation/Probable Maximum Flood PMP/PMF storm event to the tailings management
system In addition Mill tailings all other process effluents all solid waste and debris except
used oil and recyclable materials and spilled materials that cannot be recovered for reuse are
transferred to one or more of the tailings cells in accordance with the Mills NRC license
conditions All of the process and laboratory building sinks sumps and floor drains are tied to
the transfer lines to the tailings impoundments site map of the Mill is provided in Figure
sketch of the site drainage basins is provided in Figure
As result unlike other industrial facilities whose spill management programs focus on
minimizing the introduction of chemical and solid waste and wastewater into the process sewers
and storm drains the Mill is permitted by NRC license to manage some spills via draining or
washdown to the process sewers and ultimately the tailings system However as good
environmental management practice the Mill attempts to minimize
the number and size of material spills and
the amount of unrecovered spilled material and washwater that enters the process sewers
after spill cleanup
Section 4.0 itemizes the practices in place at the Mill to meet these objectives
Requirements and methods for management recordkeeping and documentation of hazardous
material spills are addressed in the DUSA White Mesa Mill Spill Prevention Control and
Countermeasures SPCCPlan Revised February 2007 the Emergency Response Plan
ERP also revised in February 2007 and the housekeeping procedures incorporated in the
White Mesa Mill Standard Operating Procedures SOPs The SPCC plan and the ERP are
provided in their entirety in Appendices and respectively
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
3.0 RESPONSIBILITY
All Mill personnel are responsible for implementation of the practices in this BMPP DUSA
White Mesa Mill management is responsible for providing the facilities or equipment necessary
to implement the practices in this BMPP
The Mill Management Organization is presented in Figure The DUSA Corporate
Management Organization is presented in Figure
An updated spill prevention and control notification list is provided in Table
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.0 BEST MANAGEMENT PRACTICES
summary list and inventory of all liquid and solid materials managed at the Mill is provided in
Tables through
4.1 General Management Practices Applicable to All Areas
4.1.1 Keep Potential Pollutants from Contact with Soil and Surface Water
Store hazardous materials and other potential pollutants in appropriate containers
Label the containers
Keep the containers covered when not in use
4.1.2 Keep Potential Pollutants from Contact with Precipitation
Store bulk materials in covered tanks or drums
Store jars bottle or similar small containers in buildings or under covered areas
Replace or repair broken dumpsters and bins
Keep dumpster lids and large container covers closed when not in use to keep
precipitation out
4.1.3 Keep Paved Areas from Becoming Pollutant Sources
Sweep paved areas regularly and dispose of debris in the solid waste dumpsters or
tailings area as appropriate
4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the
Process and Reagent Storage Area
Diversion ditches drainage channels and surface water control structures in and around
the Mill area will be inspected at least weekly in accordance with the regularly scheduled
inspections required by Groundwater Discharge Permit No UGW370004 and
Byproduct Materials License UT1900479 Areas requiring maintenance or repair such
as excessive vegetative growth channel erosion or pooling of surface water runoff will
be report to site management and maintenance departments for necessary action to repair
damage or perform reconstruction in order for the control feature to perform as intended
Status of maintenance or repairs will be documented during follow up inspections and
additional action taken if necessary
4.1.5 Recycle Fluids Whenever Possible
When possible select automotive fluids solvents and cleaners that can be recycled or
reclaimed
When possible select consumable materials from suppliers who will reclaim empty
containers
Keep spent fluids in properly labeled covered containers until they are picked up for
recycle or transferred to the tailings area for disposal
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.2 Management Practices for Process and Laboratory Areas
4.2.1 Clean Up Spills Properly
Clean up spills with dry cleanup methods absorbents sweeping collection drums
instead of water whenever possible
Clean spills of stored reagents or other chemicals immediately after discovery
Groundwater Discharge Permit No UGW370004 Section I.D.8.c
Recover and re-use spilled material whenever possible
Keep supplies of rags sorbent materials such as cat litter spill collection drums and
personnel protective equipment PPE near the areas where they may be needed for
spill response
If spills must be washed down use the minimum amount of water needed for effective
cleanup
4.2.2 Protect Materials Stored Outdoors
If drummed feeds or products must be stored outdoors store them in covered or diked
areas when possible
If drummed chemicals must be stored outdoors store them in covered or diked areas
when possible
Make sure drums and containers stored outdoors are in good condition and secured
against wind or leakage Place any damaged containers into an overpack drum or second
container
4.2.3 Water Management
When possible recycle and reuse water from flushing and pressure testing equipment
When possible wipe down the outsides of containers instead of rinsing them off in the
sink
When possible wipe down counters and work surfaces instead of hosing or rinsing them
off to sinks and drains
4.2.4 Materials Management
Purchase and inventory the smallest amount of laboratory reagent necessary
Do not stock more of reagent than will be used up before its expiration date
All new construction of reagent storage facilities will include secondary containment
which shall control and prevent any contact of spilled reagents or otherwise released
reagent or product with the ground surface Groundwater Discharge Permit No
UGW370004 Section I.D.3.e
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.3 Management Practices for Maintenance Activities
4.3.1 Keep Clean Dry Shop
Sweep or vacuum shop floors regularly
Designate specific areas indoors for parts cleaning and use cleaners and solvents only in
those areas
Clean up spills promptly Dont let minor spills spread
Keep supplies of rags collection containers and sorbent material near each work area
where they are needed
Store bulk fluids waste fluids and batteries in an area with secondary containment
double drum drip pan to capture leakage and contain spills
4.3.2 Manage Vehicle Fluids
Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as
possible Use drip pans or plastic tarps to prevent spillage and spread of fluids
Promptly contain and transfer drained fluids to appropriate storage area for reuse recycle
or disposal
Recycle automotive fluids if possible when their useful life is finished
4.3.3 Use Controls During Paint Removal
Use drop cloths and sheeting to prevent windborne contamination from paint chips and
sandblasting dust
Collect contain and transfer as soon as possible accumulated dusts and paint chips to
disposal location in the tailings area authorized to accept waste materials from
maintenance or construction activities
4.3.4 Use Controls During Paint Application and Cleanup
Mix and use the right amount of paint for the job Use up one container before opening
second one
Recycle or reuse leftover paint whenever possible
Never clean brushes or rinse or drain paint containers on the ground paved or unpaved
Clean brushes and containers only at sinks and stations that drain to the process sewer to
the tailings system
Paint out brushes to the extent possible before water washing water-based paint or
solvent rinsing oil-based paint
Filter and reuse thinners and solvent whenever possible Contain solids and unusable
excess liquids for transfer to the tailings area
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.4 Management Practices for Ore Pad Tailings Area and Heavy Equipment
Detailed instructions for ore unloading dust suppression and tailings management are provided
in the Mill SOPs
4.4.1 Wash Down Vehicles and Equipment in Proper Areas
Wash down trucks trailers and other heavy equipment only in areas designated for this
purpose such as washdown pad areas and the truck wash station
At the truck wash station make sure the water collection and recycling system is working
before turning on water sprays
4.4.2 Manage Stockpiles to Prevent Windborne Contamination
Water spray the ore pad and unpaved areas at appropriate frequency in accordance with
Mill SOPs
Water spray stockpiles as required by opacity standards or weather conditions
Dont over-water Keep surfaces moist but minimize runoff water
4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources
Schedule excavation grading and other earthrnoving activities when extreme dryness and
high winds will not be factor to prevent the need for excessive dust suppression
Remove existing vegetation only when absolutely necessary
Seed or plant temporary vegetation for erosion control on slopes
Page
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Rome Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.l66
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Home Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Fryderihmd Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE
REAGENT YARD LIST
ADOGEN 2382
ADVANTAGE 1O1M
AMERS1TE
AMINE 2384
AMMONIUM SULFATE BULK
AMMONIUM SULFATE BAGS
ANHYDROUS AMMONIA
CHEMFAC 100
CLARIFLOC N-1O1P
DECYLALCOHOL
DIESEL FUEL
FLOCCULENT M1O11N
FLOCCULENT M1302C
GRINDING BALLS
ISODECANOL
KEROSENE
MACKANATE
MILLSPERSE 802
NALCO 2458
NALCO 8815
PERCOL 351
PERCOL 406
PERCOL 745
POLOX
POLYHALL YCF
PROPANE
SALT BAGS
SALT BULK
SODA ASH BAGS
SODA ASH BULK
SODIUM CHLORATE
SODIUM HYDROXIDE
SULFURIC ACID
UNLEADED GASOLINE
USED OIL
6120
2475
19440
54000
4300
107920
12800
3000
45430
30550
3550
48290
45430
1344
3150
1410
1500
13950
10360
39280
39280
84100
101128
4801440
16921
8530
17700
10500
19904
1600000
269160
3000
5000
REAGENT ..2Hy QUANTT\ttBSY NUMBEROFcTh
STORAGE TANKS
pAc1T.
cAaoNs
31409
250
6000
10152
30000
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
Chemical in Lab RQ2 Quantity In Stock
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
6.8 kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
Chemical in Volatiles and RQ2 Quantity In Stock
Flammables Lockers ABC
Chloroform 4.54 kg
Formaldehyde 45.4 kg cl of 37%solution
Nitrobenzene 454 kg 12
Toluene 454kg 12L
Chemical in Acid Shed RQ2 Quantity In Stock
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
IcHEMItAt tYQ tQijAN7jTht1NN
CiRAtE
1kStP
Acetic Acid Glacial 1000 lbs
toMpooNæ
gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 Ibs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs kg 11 Ibs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal 5kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
REAGENT RQ2 QUANTITY IN
REAGENT YARD
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfloc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous substances Designated Pursuant to section 311 of the clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT RQ QUANTITY IN
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
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Mill Site Drainage Basins
Figure
White Mesa Mill
Mill Management Organization Chart
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APPENDICES
APPENDIX
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
FOR CHEMICALS AND PETROLEUM PRODUCTS
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box809
Bland ing Utah 84511
February 2007
Prepared by
Denison Mines USA Corp
1050 Street Suite 950
Denver Colorado 80265
TABLE OF CONTENTS
SECTION PAGE
1.1 Objective
1.2 Responsibilities
1.3 Drainage Basins Pathways and Diversions
1.4 Description of Basins
1.4.1 Basin Al
.4.2 Basin A2
1.4.3 Basin Bl
1.4.4 Basin B2
1.4.5 Basin B3
1.4.6 Basin
1.4.7 Basin
1.4.8 Basin
1.5 Potential Chemical Spill Sources And Spill Containment
1.5.1 ReagentTanks
1.5.2 Ammonia
1.5.3 Ammonium Meta Vanadate
1.5.4 Caustic Storage Sodium Hydroxide
1.5.5 Sodium Carbonate
1.5.6 Sodium Chlorate
1.5.7 Sulfuric Acid
1.5.8 Vanadium Pentoxide
1.5.9 Kerosene Organic
1.6.0 Used/Waste Oil
SECTION PAGE
1.6.1 Propane
1.7 Potential Petroleum Sources And Containment
1.7.1 Petroleum Storage Tanks
1.7.1.1 Diesel
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.2 Unleaded Gasoline
1.7.2.3 Pump Station
1.7.2.4 Truck Unloading
1.8 Spill Discovery And Remedial Action
1.9 Spill Incident Notifications
1.9.1 External Notification
1.9.2 Internal Notification 11
1.10 Records And Reports 12
1.11 Personnel Training And Spill Prevention Procedures 12
1.11.1 Training Records 12
1.11.2 Monitoring Reports 13
1.12 Revision 13
1.13 Summary 13
1.14 Mill Manager Approval 14
1.15 Certification by Registered Professional Engineer 14
LIST OF TABLES
Table 1.0 Mill Organization Chart
Table 2.0 Reagent Tank List
Table 3.0 Laboratory Chemical Inventory List
Table 4.0 Reagent Yard/Small Quantity Chemicals List
Table 5.0 Reagent Yard/Bulk Chemicals List
Table 6.0 Petroleum Products and Solvents List
LIST OF FIGURES
Figure Mill Site Layout
Figure Mill Site Drainage Basins
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS
1.1 OBJECTIVE
The objective of the Spill Prevention Control and Countermeasures SPCC
Plan is to serve as site-specific guideline for the prevention of and response to
chemical and petroleum spills and as guidance document for compliance with
Groundwater Discharge Permit No UGW370004 The plan outlines spill
potentials containment areas and drainage characteristics of the White Mesa
Mill site The plan addresses chemical spill prevention spill potentials spill
discovery and spill notification procedures The Oil Pollution Prevention Sections
of the Clean Water Act 40 CFR 112 to 117 also referred to as the Spill
Prevention Control and Countermeasures SPCC rules establish
requirements that apply to facilities which could reasonably be expected to
discharge oil in quantities that may be harmful as described in that Act into or
upon the navigable waters of the United States or that may affect natural
resources of the United States Section 112 states that the Act is not applicable
to facilities that are not subject to the authority of the Environmental
Protection Agency EPA for one of the following reasons
Due to its location the facility could not reasonably be expected to
discharge oil into navigable waters of or impact natural resources of the
U.S or
The facility is subject to authority of the Department of Transportation as
defined in Memorandum of Understanding MOU between the
Secretary of Transportation and the EPA Administrator or
The facility does not exceed either the underground or the above ground
storage capacity 42000 gallons and 1320 gallons respectively
prescribed in the rules
The Mill could not reasonably be expected as described in the SPCC regulation
to discharge oil into the navigable waters or impact natural resources of the
U.S The Mill site was constructed with an overall grade and diversion ditch
system designed to channel the non-recovered portion of any material spill to the
tailings management system Hence it is not reasonable to expect that surface
spills will ever reach navigable waters or natural resources of the U.S or Utah
Therefore the SPCC reporting requirements in the Clean Water Act are not
applicable to the Mill However as good environmental management practice
the Mill has implemented the spill management program described in this
document which is consistent with the intent of the Clean Water Act to the
extent practicable Although the Mill by design cannot directly impact navigable
waters of the U.S and as result spills that may occur but are retained within
the site would not be reportable the Mill implements these practices in good
faith effort to minimize all potential sources of pollution at the site
Storage of ores and alternate feeds on the ore pad and containment of tailings
in the Mill tailings impoundment system are not considered spills for the
purposes of this SPCC
Ammonia is the only chemical that has the potential to leave the site and would
do so as vapor
Figure Site Layout Map shows map of the mill site including the locations of
the chemical tanks on-site Figure shows the basins and drainage ditch areas
for the mill site Table 1.0 is an organization chart for Mill operations Table 2.0
lists the reagent tanks and their respective capacities Table 3.0 lists the
laboratory chemicals their amounts and their reportable quantities Table 4.0
lists the operations chemicals Table 5.0 lists the chemicals in the reagent yard
their amounts and their reportable quantities Table 6.0 lists the petroleum
products and solvents on site
1.2 RESPONSIBILITIES
Person in charge of facility responsible for spill prevention
Mr Richard Bartlett Interim Mill Manager
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 459-2495 home
Person in charge of follow-up spill record keeping and/or reporting
Mr David Turk Department Head Health Safety and Environmental
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 678-7802 home
Refer to Section 1.9 Spill Incident Notification for list of company personnel
to be notified in case of spill In addition an organizational chart is provided
in Table 1.0
1.3 DRAINAGE BASINS PATHWAYS AND DIVERSIONS
The main drainage pathways are illustrated in Figure The map shows
drainage basin boundaries flow paths constructed diversion ditches tailings
cells the spillway between Cell and dikes berms and other relevant
features The White Mesa Mill is zero discharge facility for process liquid
wastes The mill area has been designed to ensure that all spills or leaks
from tanks will drain toward the lined tailings cells
The tailings cells in turn are operated with sufficient freeboard minimum of
three feet to withstand 100%of the PMP Probable Maximum Precipitation
This allows for maximum of 10 inches of rain at any given time
1.4 DESCRIPTION OF BASINS
Precipitation and unexpected spills on the mill property are contained within
their respective drainage basins Runoff would ultimately drain into one of
the three lined tailings cells
1.4.1 Basin Al
Basin Al is north of Cell I-I and Diversion Ditch No The basin
contains 23 acres all of which drain into Westwater Creek This area is
not affected by mill operations
1.4.2 BasinA2
Basin A2 contains all of Cell 1-I including an area south of the Diversion
Ditch No The basin covers 84 acres Any runoff from this basin
would be contained within Cell 1-I
1.4.3 Basin BI
Basin B1 is north of the mill property and is not affected by mill
operations The basin contains 45.4 tributary acres Runoff from this
basin drains into flood retention area by flowing through Diversion Ditch
No Diversion Ditch No drains into Westwater Creek
1.4.4 Basin B2
Basin B2 is northeast of the mill and contains only 2.6 acres Runoff from
this basin would drain into Diversion Ditch No Diversion Ditch No
ultimately drains into Diversion Ditch No This basin is not affected by
mill operations
1.4.5 Basin B3
Basin B3 contains most of the mill area buildings ore stockpiles process
storage tanks retention ponds spill containment structures pipelines
and roadways The normal direction of flow in this basin is from the
northwest to the southwest Any runoff from this basin would drain into
Cell 1-I The basin contains 64 acres This basin has sufficient
freeboard to withstand 100%of the PMP Probable Maximum
Precipitation This allows 10 inches of rain for any given storm event
1.4.6 Basin
Basin contains all of Cell The basin consists of 80.7 acres This
basin contains earth stockpiles and the heavy equipment shop The
direction of flow in this basin is to the southwest All runoff in this basin
would be channeled along the southern edge of the basin Runoff would
then flow into Cell via the spillway from Cell to Cell
1.4.7 Basin
Basin contains all of Cell This basin consists of 78.3 acres including
portion of the slopes of the topsoil stockpile and random stockpile The
basin contains all flows including those caused by the PMF
1.4.8 Basin
Basin contains Cell 4A and consists of 43.3 acres All anticipated flows
including those caused by the PMF will be contained within the basin and
will flow directly into Cell 4A
1.5 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL
CONTAINMENT
This section details potential sources of chemical spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States Reportable
Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act
It is not expected that any spill would reach navigable waters of the United States
However if spill of volume listed below occurs and remains on the mill site which is
the more likely scenario then management is to be notified so that proper internal
evaluations of the spill are made
1.5.1 Reagent Tanks Tank list included in Table 2.0
1.5.2 Ammonia
The ammonia storage tanks consist of two tanks with capacity of
31409 gallons each The tanks are located southeast of the Mill building
Daily monitoring of the tanks for leaks and routine integrity inspections will be
conducted to minimize the hazard associated with ammonia The reportable
quantity for an ammonia spill is gallons
Ammonia spills should be treated as gaseous Ammonia vapors will be
monitored closely to minimize the hazard associated with inhalation If
vapors are detected efforts will be made to stop or repair the leak
expeditiously Ammonia is the only chemical as vapor that has the
potential to leave the site
1.5.3 Ammonia Meta Vanadate
Ammonia meta vanadate is present in the SX building as the process
solutions move through the circuit to produce the vanadium end product
But the primary focus will be on the transportation of this chemical The
reportable quantity for an ammonia meta vanadate spill is 1000 pounds
1.5.4 Caustic Storage Sodium Hydroxide
The caustic storage tank is located on splash pad on the northwest corner
of the SX building The tank has capacity of 19904 gallons The tank
supports are mounted on concrete curbed catchment pad that directs spills
into the sand filter sump in the northwest corner of the SX building The
reportable quantity for sodium hydroxide spill is 85 gallons
1.5.5 Sodium Carbonate Soda Ash
The soda ash solution tank has capacity of 16921 gallons and is located in
the northeast corner of the SX building The smaller soda ash shift tank has
capacity of 8530 gallons and is located in the SX building Spills will be
diverted into the boiler area and would ultimately drain into Cell 1-I There is
no reportable quantity associated with sodium carbonate spill
1.5.6 Sodium Chlorate
Sodium chlorate tanks consist of two fiberglass tanks located within dike
east of the SX building The larger tank is used for dilution purposes and has
maximum capacity of 17700 gallons The smaller tank serves as
storage tank and has capacity of 10500 gallons Daily monitoring of the
tanks for leaks and integrity inspections will be conducted to minimize the
hazard associated with sodium chlorate
Sodium chlorate that has dried and solidified becomes even more of safety
hazard due to its extremely flammable nature The reportable quantity for
sodium chlorate spill is 400 gallons
1.5.7 Sulfuric Acid
The sulfuric acid storage tanks consist of one large tank with the capacity of
16000000 gallons and two smaller tanks with capacities of 269160 gallons
each
The large tank is located in the northwest corner of mill area basin B3 and is
primarily used for acid storage and unloading The tank support for the large
tank is on mound above depression which would contain significant
spill All flows resulting would be channeled to Cell 1-I The tank is equipped
with high level audible alarm which sounds prior to tank overflows
concrete spill catchment with sump in the back provides added
containment around the base of the tank However the catchment basin
would not be able to handle major tank failure such as tank rupture The
resulting overflow would flow towards Cell 1-I
The two smaller storage tanks are located within an equal volume spill
containment dike east of the mill building The tanks are not presently in
use but are equipped with high level audible alarms
The reportable quantity for sulfuric acid spill is 65 gallons 1000 pounds
1.5.8 Vanadium Pentoxide
Vanadium pentoxide is produced when vanadium is processed through the
drying and fusing circuits and is not present in the vanadium circuit until after
the deammoniator Efforts will be made to minimize leaks or line breaks that
may occur in processes in the circuit that contain vanadium pentoxide
Special care will be taken in the transportation of this chemical The
reportable quantity for vanadium pentoxide spill is 1000 pounds
1.5.9 Kerosene Organic
The kerosene storage area is located in the central mill yard and has
combined capacity of 10152 gallons in three tanks Any overflow from these
three tanks would flow around the south side of the SX building and then into
Cell 1-I These tanks have drain valves which remain locked unless
personnel are supervising draining operations The reportable quantity for
kerosene spill is 100 gallons
1.6.0 Used Waste Oil
Used Waste oil for parts washing is located north of the maintenance shop
in tank and has capacity of 5000 gallons The tank is contained within
concrete containment system Ultimate disposal of the used oil is to an EPA
permitted oil recycler Any oil escaping the concrete containment system will
be cleaned up Soil contaminated with used oil will be excavated and
disposed of in Cell
1.6.1 Propane
The propane tank is located in the northwest corner of the mill yard and has
capacity of 30000 gallons Daily monitoring of the tank for leaks and
integrity inspections will be conducted to minimize potential hazards
associated with propane leaks Propane leaks will be reported immediately
There is no reportable quantity associated with propane spill
1.7 POTENTIAL PETROLEUM SPILL SOURCES AND
CONTAINMENT
This section details potential sources of petroleum spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States It is not
expected that any spill would reach navigable waters of the United States However if
spill of volume listed below occurs and remains on the mill site which is the more
likely scenario then management is to be notified so that proper internal evaluations of
the spill are made
1.7.1 Petroleum Tanks
1.7.1.1 Diesel
Two diesel storage tanks are located north of the mill building The tanks
have capacities of 250 gallons each One of the diesel tanks is for the
emergency generator The other tank is located in the pumphouse on an
elevated stand Spillage from either tank would ultimately flow into Cell 1-I
The reportable quantity for diesel spill is 100 gallons
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.1 Diesel
The diesel tank is located on the east boundary of Basin B3 and has
capacity of 6000 gallons The tank is contained within concrete catchment
pad The reportable quantity for diesel spill is 100 gallons
1.7.2.2 Unleaded Gasoline
The unleaded gasoline tank is located next to the diesel tank The unleaded
gasoline tank has capacity of 3000 gallons and is contained within the
same containment system as the diesel tank The reportable quantity for an
unleaded gasoline spill is 100 gallons
1.7.2.3 Pump Station
Both the diesel and the unleaded gasoline tanks will be used for refueling
company vehicles used around the mill site The pump station is equipped
with an emergency shut-off device in case of overflow during fueling In
addition the station is also equipped with piston leak detector and
emergency vent Check valves are present along
with tank monitor
console with leak detection system The catchment is able to handle
complete failure of one tank However if both tanks failed the concrete
catchment pad would not be able to contain the spill In this case
temporary berm would need to be constructed Absorbent diapers or floor
sweep would be used in an effort to limit and contain the spill The soil would
be cleaned up and placed in the authorized disposal area in Cell
1.7 2.4 Truck Unloading
In the event of truck accident resulting in an overturned vehicle in the mill
area proper reporting and containment procedures will be followed when
warranted such as when oil or diesel fuel is spilled Proper clean-up
procedures will be followed to minimize or limit the spill The spill may be
temporarily bermed or localized with absorbent compounds Any soils
contaminated with diesel fuel or oil will be cleaned up and placed in the
authorized disposal area in Cell
1.8 SPILL DISCOVERY AND REMEDIAL ACTION
Once chemical or petroleum spill has been detected it is important to take
measures to limit additional spillage and contain the spill that has already
occurred Chemical or petroleum spills will be handled as follows
The Shift Foreman will direct efforts to shut down systems if
possible to limit further release
The Shift Foreman will also secure help if operators are requiring
additional assistance to contain the spill
The Shift Foreman is also obligated to initiate reporting procedures
Once control measures have begun and personal danger is
minimized the Shift Foreman will notify the Production
Superintendent Maintenance Superintendent or Mill Manager
The Production or Maintenance Superintendent will notify the Mill
Manager who in turn will notify the Environmental Health and Safety
Manager
The Mill Manager will assess the spill and related damage and direct
remedial actions The corrective actions may include repairs clean
up disposal and company notifications Government notifications
may be necessary in some cases
If major spill continues uncontrolled these alternatives will be considered
Construct soil dikes or pit using heavy equipment
Construct diversion channel into an existing pond
Start pumping the spill into an existing tank or pond
Plan further clean-up and decontamination measures
1.9 SPILL INCIDENT NOTIFICATION
1.9.1 External Notification
As stated in Section 1.1 spills are not expected to reach navigable waters of
the United States If spill of reportable quantity occurs then mill and
corporate management must be notified and they will evaluate whether or not
the following agencies must be notified
EPA National Response Center 1-800-424-8802
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah 801/538-7200
Water Quality Division 801/538-6146
In case of tailings dam failure contact the following agencies
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah Natural Resources 801/538-7200
1.9.2 Internal Notification
Internal reporting requirements for incidents spills and significant spills are
as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions and accidents
Government investigations information requests or enforcement
actions
Private actions or claims corporate or employee
Deviations from corporate policies or government requirements by
management
Which have or could result in the following
Death serious injury or adverse health effects
Property damage exceeding $1000000
10
Government investigation or enforcement action which limits
operations or assesses penalties of $100000 or more
Publicity resulted or anticipated
Substantial media coverage
Report At The Beginning Of The Next Day
Event Criteria
Was reported to government agency as required by law
Worker employee or contractor recordable injury or illness associated
with release
Community impact-reported or awareness
Publicity resulted or anticipated
Release exceeding the reportable quantities listed in Section 1.5 for
each specific process material waste or by-product
In the event of spill of reportable quantity the Mill Manager is required to
call the Corporate Environmental Manager or the President and Chief
Executive Officer The individual first discovering the spill will report it to the
Shift Foreman Production Superintendent or Maintenance Superintendent
who will in turn ensure that the Mill Manager is notified The Environmental
Health and Safety Manager will also be contacted by the Mill Manager
Name Title Home Phone
Mill Personnel
Richard Bartlett Interim Mill Manager 435 678-2495
Wade Hancock Maintenance Foreman 435 678-2753
David Turk Environmental Health and
Safety Manager 435 678-7802
N/A Production Superintendent
N/A Maintenance Foreman
Scot Christensen Mill Shift Foreman 435 678-2015
Corporate Personnel
Ronald Hochstein President and Chief Operating Officer 604 377-1167
David Frydenlund Vice President and General Counsel 303 221-0098
In the event the next person in the chain-of-command cannot be reached
then proceed up the chain-of-command to the next level Table 1.0 shows the
organizational chart for the mill site
11
1.10 RECORDS AND REPORTS
The following reports and records are to be maintained in Central Files by the
Environmental Health and Safety Manager for inspection and review for
minimum of three years
Record of site monitoring inspections
Daily Tailings Inspection Data
Weekly Tailings Inspection and Survey
Monthly Tailings Inspection Pipeline thickness
Quarterly Tailings Inspection
Tank to soil potential measurements
Annual bulk oil and fuel tank visual inspections
Tank and pipeline thickness tests
Quarterly and annual PCB transformer inspections if transformer
contains PCBs
Tank supports and foundation inspections
Spill Incident Reports
Latest revision of SPCC plan
1.11 PERSONNEL TRAINING AND SPILL PREVENTION
PROCEDURES
All new employees are instructed on spills at the time they are employed and
trained They are briefed on chemical and petroleum spill prevention and
control They are informed that leaks in piping valves and sudden
discharges from tanks should be reported immediately Abnormal flows from
ditches or impoundments are of immediate concern In addition safety
meeting is presented annually by the Environmental Health and Safety
Manager to review the SPCC plan
1.11.1 Training Records
Employee training records on chemical and petroleum spill prevention are
maintained in the general safety training files
1.11.2 Monitoring Reports
Shift logs shall provide checklist for inspection items
12
1.12 REVISION
This procedure is to be reviewed by the mill staff and registered
professional engineer at least onc eve ry th ree years and updated when
circumstances warrant revision
1.13 Summary
Below is table listing the specific reportable quantities associated with the
major chemical and petroleum products on-site
CHEMICAL REPORTABLE
QUANTITY RQ
AMMONIA 100 POUNDS
AMV 1000 POUNDS
SODIUM 1000 POUNDS
HYDROXIDE
SODA ASH No Reportable
Quantity
SODIUM 400 GALLONS
CHLORATE
SULFURIC ACID 1000 POUNDS
VANADIUM 1000 POUNDS
PENTOXIDE
KEROSENE 100 GALLONS
OIL No Reportable
Quantity
PROPANE No Reportable
Quantity
DIESEL 100 GALLONS
UNLEADED
FUEL
13
1.14 MILL MANAGER APPROVAL
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with the Standard Operating Procedures
currently in effect
%dcar
Richard Bartlett
Interim Mill Manager
1.15 CERTIFICATION BY
REGISTERED PROFESSIONAL ENGINEER
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with good engineering practices
Registered Professional Engineer
State of Utah No 165838
Harold Roberts
14
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Home Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.166
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Home Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE 2.0
REAGENT TANK LIST
QUANTITY REAGENT cAPACITYGAt
DIESEL 250
KEROSENE 10152
USED/WASTE OIL 5000
DIESEL 6000
UNLEADED 3000
PROPANE 30000
AMMONIA 31409
SODIUM HYDROXIDE 19904
SODA ASH SOLUTION 16921
SODA ASH SHIFT 8530
SODIUM CHLORATE 17700
SODIUM CHLORATE 10500
SULFURIC ACID 1600000
SULFURIC ACID 269160
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
_-__
fiQj
---
ÆntiiIAStbk
---s-b
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
6.8 kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
GhiºatVoiMiIand
FIfl3iæTib1e ScSABt t1t1
Chloroform
-p1
4.54 kg
Formaldehyde 45.4 kg IL of 37%solution
Nitrobenzene 454 kg 12
Toluene 454 kg 12
CheiWuinAidShØd-I
--
Oiiaht1tWJitStoÆk
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
cH EMiCAt .RQ eQUANTJ 1WŁ1NIZ2t
Acetic Acid Glacial
4c
000 lbs
tOMPOUNU
gal
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 Ibs
Chlorine 10 lbs lbs
Ferrous Sulfate Heptahydrate 1000 lbs kg 11 Ibs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
REAGENT RQ2 QUANTITY IN
REAGENT YARD
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfloc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT QUANTJTY IN
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
GR
I
Z
Z
L
Y
DE
C
O
N
T
A
M
I
N
A
T
I
O
N
PA
D
DIE
S
E
L
SA
M
P
L
E
P
L
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Lj
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10
SC
f
t
L
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IN
FT
Figure
White Mesa Mill
Mill Site Drainage Basins
APPENDIX
WHITE MESA MILL
EMERGENCY RESPONSE PLAN
EMERGENCY RESPONSE PLAN
REVISION 1.1
Denison Mines USA Corp
na.i--aL--isii
VYIIIIC IVlCSct 1SC
landing Utah
April14 1986
REVISED
February 16 2007
Distribution List
Ron Hochstein
Rich Bartlett
David Turk
Michael Spillman
Miii Shifi Foremen
Blanding Fire Department
San Juan County EMS Coordinator
State of Utah Department of Radiation Control
Revision Date January 16 2006
TABLE OF CONTENTS
Page
Number
1.0 Introduction
2.0 White Mesa Mill Background
3.0 Plan Objectives
4.0 Description of Facilities
4.1 Fire Water Supply and Alarm Systems
4.2 Office Building and Laboratory
4.3 Solvent Extraction Building
4.4 Mill Building
4.5 Maintenance Shop/Warehouse/Change Room Building
4.6 Reagent and Fuel Storage
4.7 Boiler House
4.8 Sample Plant
5.0 Organization and Responsibilities
5.1 Mill Manager/Incident Commander
5.2 Operations Superintendent
5.3 Radiation Safety Officer/F ire Chief
5.4 Maintenance Supervisor
5.5 Laboratory Supervisor
5.6 Shift Foremen
5.7 Scale House Personnel
5.8 Emergency Response Teams
6.0 Specific Emergencies 10
6.1 Fire 10
6.2 Chemical or Gas Release 10
6.3 Earthquake 10
6.4 Terrorist/Bomb Threat 10
6.5 Tailings Dam Break and Major Floods 10
7.0 Evacuation Procedure 11
7.1 Notification 11
7.2 Assembly 11
7.3 Specific Procedures for Operations Personnel 11
8.0 Off-Site Emergency Equipment/Personnel Release 11
9.0 Emergency Equipment 12
9.1 Fire Hose 12
9.2 Self Contained Breathing Apparatus 12
9.3 Spill Clean-up Equipment 12
9.4 Fire Fighting PPE 12
10.0 Emergency Transportation 13
11.0 Emergency Evacuation Drills 13
EXHIBITS
Emergency Notification List E-
Internal Notifications E-2
Site Layout Map E-3
Main Shut-off Valves E-4
APPENDICES
Emergency Procedure Response to Fire A-I
Emergency Procedure Response to Chemical or Gas Release A-2
Emergency Evacuation Procedure A-3
FIGURES
Fire System Schematic F-I
ii
INTERNATIONAL URANIUM USA CORPORATION
Rev No R-1
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
INTRODUCTION
This Emergency Response Plan is written not only to comply with Federal State and local
regulations but even more importantly to reduce the risk to our employees and that of the
community in regards to Health Safety and Environmental Emergencies
This plan includes the following
evaluation of the potential risks for fire explosions gas releases chemical spills and
floods including tailings dam failure
specific emergency programs for each potential event
definition of administrative response actions and
definition of the emergency response contacts both internal and external
The White Mesa Mill the Mill operates under the following regulatory agencies
Utah State Department of Environmental Quality Division of Radiation Control
Mine Safety and Health Administration
Environmental Protection Agency
Utah State Department of Environmental Quality Division of Air Quality and
Utah State Division of Natural Resources Bureau of Dam Safety
WHITE MESA MILL OVERVIEW
The Mill processes conventional uranium or uranium/vanadium ores to recover uranium and
vanadium In addition to the processing of conventional ores the Mill also processes alternate
feed materials using similar process steps and chemicals The conventional ore is stored on the
Ore Pad shown in Exhibit Alternate feed materials are also stored on the Ore Pad and may
be stored in bulk form lined burrito bags liners or drums The descriptions of each alternate
feed material are maintained by the Mills Radiation Safety Officer
The Mill utilizes semi-autogenous grind circuit followed by hot sulfuric acid leach and
solvent extraction process to extract uranium and vanadium from ores using large amounts of
sulfuric acid sodium chlorate kerosene amines ammonia and caustic soda in the process The
reagent storage tank locations are described in further detail in Section 4.6
Emissions from the Mill process are in the form of air emissions from exhaust stacks and
solid/liquid tailings which are stored in the Mills tailings cells located west/southwest of the
main Mill building The major exhaust stack parameters are shown in the following table
Description
Height
ft from surface
Diameter
inches
Estimated Flow Rate
cfm
Leach Exhaust -l00 36 13700
Yellow Cake Drying
stacks
-85 18 4000 per stack
Vanadium Roasting
Fusion
85 38 4100
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INTERNATIONAL URANIUM USA CORPORATION
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Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
There are also smaller exhaust stacks associated with the Laboratory in the Mill Administration
building and the boiler exhaust stack
The Mills tailings cells are comprised of four below grade engineered cells Cell 1-I and
4A Liquids are stored in Cell 1-I and Cell the active tailings cell The liquid in the tailings
cells is very acidic In addition to the tailings cells there is also an emergency lined catchment
basin west of the Mill building Solutions in this basin or the tailings cells should not be used to
fight fires in the Mill facility
The products of the Mill include ammonium metavanadate AMy vanadium pregnant liquor
VPL vanadium pentoxide V205 and yellowcake or uranium concentrate lJO The V205
and 11308 products are packaged in steel drums for shipment The AMV is packaged in either
steel drums or super-saks while the VPL is sold in liquid form in bulk
Master files containing Material Safety Data Sheets for all materials in use at the Mill are
maintained at the Safety Office Mill Maintenance Office Mill Laboratory and Mill Central
Control Room Copies are also on file at the Blanding Clinic Doctors Offices Blanding Fire
House and Office of the San Juan County Emergency Medical Coordinator
The nearest residence to the Mill is approximately one mile to the north of the Mill the next is
residence approximately two miles north of the Mill followed by the community of White Mesa
about 3.5 miles to the south The City of Blanding is located approximately miles to the
northeast
The Mill site is near Utah State Highway 191 and can be accessed by paved access road from
the highway to the Mill facilities
PLAN OBJECTIVES
The primary objectives of this plan are
To save lives prevent injuries prevent panic and minimize property/environmental
damage to the lowest possible level
To evacuate and account for all people in the area including visitors truck drivers
contractors etc
To provide assembly areas that are as safe as possible and which can be reached without
traveling through hazardous area Assembly areas will be properly manned to deal with
sick or injured persons and provisions will be made to evacuate those persons to proper
shelter
To make adequately trained personnel available to cope with rescue and recovery
operations as directed by the Incident Commander
DESCRIPTION OF FACILITIES
The Mill facilities are shown on the Site Layout Map included as Exhibit
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4.1 Fire Water Supply and Alarm Systems
4.1.1 Fire Water Supply
The fire water supply facilities include
400000 gallon Storage Tank of which 250000 gallons are reserved for fire emergencies
Centrifugal diesel driven pump rated at 2000 gpm at 100 psi This pump starts
automatically when the pressure in the fire main drops below 100 psi See Figure Fire
System Schematic
When more water is needed for an emergency an additional source is the Recapture Reservoir
supply pipeline which can be utilized in emergencies at rate of about 1200 gpm
4.1.2 Alarm System
The alarm systems include the following
public address system
hand held radios
siren
4.2 Office Building and Laboratory
4.2.1 Office Building
The office building approximately 10000 square feet contains the administration offices
radiation health and safety offices and the Mill laboratory The central file vault and the main
computer system are also in this building The ambulance is kept on the west side of the office
building near the safety office entrance
4.2.2 Laboratory
The laboratory facilities contain the following
three flammable cabinets keys required
chemical storage room south of main lab
six fume hoods hoods 12 and are in the center of the laboratory and hoods and
are along the west wall Hoods and are no longer in service Hoods and are on
the west side and are on the east side of the center cluster of hoods with being in
front Only hoods and may be used for perchloric acid
outside laboratory chemical storage north of office building key required
perchloric acid storage vault located underground west of office building key required
wide variety of chemicals in small quantities are located in the laboratory These chemicals
range from acids to bases along with flammable metal compounds and peroxide forming
compounds Oxidizers and organic chemicals which have strong potential of producing
harmful vapors if the containers are damaged to the point that the chemicals are exposed are
stored in storage room in the laboratory There are no acids stored in this storage room The
acids including but not limited to sulfuric nitric acetic perchloric phosphoric and hydrochloric
acids are stored in the main laboratory area in 2.5 liter or 500-mi bottles MSDS books for all
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chemicals in the laboratory are located in the Laboratory Safety Department Mill Maintenance
office and Mill Central Control room
4.2.3 Electrical
Electrical transformers and electrical switches are located in the laboratory at the east end of the
chemical storage room
4.2.4 Fire Protection System
The fire protection systems in the office building and laboratory include
fire hose station located on the east end of the office building The station includes two
sets of turnout gear two SCBA units and Incident Commander materials
automatic wet sprinkler system which is actuated at 212
portable dry chemical extinguishers strategically located throughout the building
4.3 Solvent Extraction Building
The solvent extraction SX building approximately 21000 square feet houses the uranium and
vanadium solvent extraction circuits and the ELUEX circuit The SX circuits may contain up to
200000 gallons kerosene 757000 liters which has flash point of 185
Associated equipment in the SX building includes temporary boiler located at the southwest
end of the SX building which maintains the temperature for the fire system
Chemicals which may be encountered in the SX building include
Kerosene
Caustic Soda
Anhydrous Ammonia
Sulthric Acid
Salt Brine
Soda Ash
Ammonium Sulfate
Amines
Alcohol
Sodium Chlorate
Sodium Vanadate
Propane
The VPL product is stored in the SX building
4.3.1 Electrical
All electrical switches are located outside in the MCC room north of the SX building The main
control panel for all of the equipment is located in the Central Control Room in the main Mill
building
4.3.2 Fire Protection System
The SX building fire protection systems include
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wet AFFF foam sprinkler system with heat actuated sprinider heads that release at
212F
portable dry chemical extinguishers strategically located throughout the building
For fire hydrant and hose cabinet locations in the SX building refer to the Fire System Schematic
included as Figure in this Plan
4.4 Mill Building
The mill building approximately 22000 square feet contains process equipment related to
grind leach counter current decantation precipitation drying and packaging of uranium and
vanadium products
Chemicals which may be encountered in the mill building include
Caustic Soda
Anhydrous Ammonia
Sulfuric Acid
SodaAsh
Ammonium Sulfate
Sodium Chlorate
Sodium Vanadate
Propane
The finished products which are contained in the mill building include AMY V2O5 and U308 or
yellowcake
4.4.1 Electrical
The main electrical switch gear is located west of the SAG mill on the ground floor in the north
west corner of the mill building Circuit control panels are located in the SAG mill control room
the central control room the vanadium roaster control room and the AMV area
4.4.2 Fire Protection System
The main mill building fire protection systems include
portable dry chemical extinguishers strategically located throughout the building
water hoses throughout the building
For fire hydrant and hose cabinet locations in the Mill building refer to the Fire System
Schematic included as Figure of this Plan
4.5 Maintenance Shop/Warehouse/Change Room Building
This building approximately 20000 square feet contains the main maintenance shop area
located on the north end of the building the main warehouse located on the south end of the
building and the personnel change rooms and lunchltraining room located on the extreme south
end of the building on the ground and second floors
Within the maintenance shop area are the following work area and specialty shops
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the main maintenance shop area contains welding and cutting equipment lathes presses
and drill presses
carpenter shop which contains various saws and planes Fiberglass work is also done
within this shop area and it is located at the northwest end of the maintenance shop area
an electrical shop which is located south of the carpenter shop
heavy equipment maintenance shop area is located at the north end of the maintenance
shop in the center of the building
rubber room for rubber lining of equipment is located east of the equipment shop area
the maintenance shop office instrument shop and tool room are located at the south end
of the maintenance shop area
The warehouse area contains primarily dry good storage for repair parts and consumables for the
operation of the Mill There is an electrical water heater for the change room which is located in
the warehouse area at the south end
Within the warehouse and maintenance shops there are some oils and chemicals stored in the
following locations
small quantities of flammable material such as starting fluid and spray paint are kept in
the warehouse
drums of new oil and anti-freeze are stored along the east wall of the equipment
maintenance area and on the east side of the warehouse on oil storage racks
used oil is stored in tank located northeast of the equipment shop The tank has
capacity of approximately 5800 gallons
in the main maintenance shop area and the rubber room there are flammable storage
cabinets and east of the warehouse there is trailer which is used to store flammable
items such as rubber cements paints and fiberglass resins
compressed gas cylinder storage both empty and full is located outside east of the
maintenance shop
4.5.1 Electrical
The main electrical circuit breaker for the maintenance shop and warehouse building is located
on the east wall inside the Maintenance shop Auxiliary electrical panels for the change room
and warehouse are located in the southwest corner of the warehouse area
4.5.2 Fire Protection System
The fire protection system within the maintenance shop/warehouse/change room building
includes
wet automatic sprinkler system that releases at 212
portable dry chemical extinguishers strategically located throughout the maintenance
area warehouse area and the change room and lunch room
For fire hydrant and hose cabinet locations refer to the Fire System Schematic Figure
4.6 Reagent and Fuel Storage
The following lists the reagents and fuel stored at the Mill site
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sulfuric acid tank located northwest of the mill building which has capacity of
approximately 1.4 million gallons
storage tank for propane is located on the north edge of the mill site northwest of the
mill building It has storage capacity of 30000 gallons
four sodium chlorate tanks located east of SX building north of the office building and
east of the pulp storage tanks The two tanks east of the SX building are for sodium
chlorate storage and the other two tanks are for dilution of the sodium chlorate
two anhydrous ammonia tanks located east of the SX building with capacity of 31409
gallons each
three kerosene tanks located east of the SX building with capacity of 10152 gallons
each
one caustic soda tank north of the SX building with capacity of 19904 gallons
three soda ash tanks which are located east of the SX building One tank is the dry soda
ash tank with capacity of 70256 gallons Two of the tanks are soda ash dilution tanks
with capacities of 16921 gallons each
diesel fuel and gasoline are stored in two tanks located on the eastern side of the ore pad
The gasoline storage capacity is 3200 gallons while diesel storage capacity is 8000
gallons
Other reagents are stored in steel barrels or super sacs in reagent yard located east of the office
building Typical reagents which are stored in this yard include
polymers and flocculants
boiler feed water chemicals
methanol
tributyl phosphate
dirty soda ash and ammonium sulfate
SX amines and emulsion breakers
decyl alcohol
minimal amounts of acid in barrels
used oil in drums and overpacks
4.7 Boiler Facilities
The main building approximately 12400 square feet is located on the west side of the Mill site
and contains air compressors and water treatment facilities To the north of the main building is
building which houses propane-fired boiler The vanadium oxidation tank oxidation
thickener and pH adjustment tank are located south of the boiler house facilities
4.7.1 Electrical
The main electrical panel for the boiler house is located outside of the building on the south
wall
4.7.2 Fire Protection System
The fire protection system for the boiler facilities is comprised of strategically located portable
dry chemical extinguishers
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4.8 Sample Plant
The sample plant building approximately 8000 square feet is located on the ore pad east of the
maintenance shop/warehouse building The sampling plant equipment has been removed from
the building and it is currently used as storage area for maintenance
4.8.1 Electrical
The electrical panel for this building is located on the east wall upstairs
4.8.2 Fire Protection System
There are no extinguishers or sprinkler systems in the sample plant
ORGANIZATION AND RESPONSIBILITIES
The organizational chart for an emergency situation is illustrated in Figure
5.1 Mill Manager/Incident Commander
The Incident Commander has the responsibility for
preparing an Emergency Plan
communicating the Plan
directing activities during emergencies and
reporting to local State and Federal authorities
The Incident Commander will stop routine radio usage upon learning of an emergency and set up
the base station in safe location for directing activities Radio usage will be limited to the
emergency The Incident Commander has the responsibility to contact all outside services
The Incident Commander has the responsibility to account for all employees at the Mill using
the assistance of supervisors and/or any International Uranium USA Corporation IUSA
personnel The Incident Commander has the responsibility for the news media and reports
directly to the President of IUSA
5.2 Mill General Superintendent
The Mill General Superintendent has the responsibility of directing outside emergency personnel
and has the responsibility for plant security and will report directly to the Incident Commander
The Mill General Superintendent will act as Incident Commander in the absence of the Mill
Manager
5.3 Radiation Safety Officer/Fire Chief
The Radiation Safety Officer will direct rescue operations and provide the necessary emergency
medical personnel and facilities to cope with the emergency Adequately trained fire crews and
operable emergency equipment will be maintained at all times
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As Fire Chief the Radiation Safety Officer has the responsibility to maintain trained fire crews
and operable equipment mobilize and direct the fire crews and equipment in fire emergency or
one containing the threat of fire and to assist in evacuation and rescue or recovery operations
In the absence of the Radiation Safety Officer the Mill Safety Coordinator will assume these
duties
5.4 Maintenance Supervisor
The Maintenance Supervisor will direct all personnel in evacuation and in activities to cope with
the emergency including isolation of utilities and providing technical advice as needed The
Maintenance Supervisor will be assisted by the Mill Safety Coordinator
5.5 Laboratory Supervisor
The Laboratory Supervisor has the responsibility to direct and account for all office personnel
including IUSA personnel and office visitors in evacuation and in activities to cope with the
emergency In case of mill tour the Supervisor accompanying the tour will be responsible for
evacuation of visitors
5.6 Shift Foremen
Shift Foremen are in charge until the Incident Commander arrives and are responsible for all
functions listed above Shift Foremen have the responsibility to account for all of their people in
addition to any visitors contractors etc in their areas and report to the Incident Commander or
in the absence of the Incident Commander to administer all of the above duties
5.7 Scale House Personnel
Scale house person on shift will be responsible to account for ore truck drivers and reagent truck
drivers
5.8 Emergency Response Teams
The response crew for each operating shift will normally consist of the following operators under
the direction of the shift foreman This organization may be changed for individual shifts subject
to the approval of the Fire Chief
5.8.1 Operational Mode
Leach Operator
CCD Operator
Solvent Extraction Operator
Mill Trainee
5.8.2 Non-Operational Mode
Shift Foreman
Operations Personnel
Maintenance Personnel
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Figure
Emergency Response Organizational Structure
Incident Commander
Mitt Manager
Director of Secuhty
Operations Supehntendent
Fire Chief
Radiation Safety Officer
Shift Foremen Emergency Response Teams Lab Supervisor
Operatidnal Mode Non-Operational Mode
Leach Operator CCD Operator Shift Fomman Operations Personnel
SX Operator Mill Trainee Maintenance Personnel
SPECIFIC EMERGENCIES
The following details procedures to be followed during specific emergencies but are not limited
to the following
6.1 Fire
Should fire occur the procedure outlined in Appendix for reporting and responding to fires
will be followed Particular areas of concern include
Solvent Extraction Building
Propane Tanks
Lab or Lab Storage Area
6.2 Chemical or Gas Release
The procedures for response to chemical or gas release are outlined as Appendix
6.3 Earthquake
Although this is highly unlikely an earthquake could occur at the Mill severe earthquake
could cause buildings and other structures to collapse chemical and/or gas releases major fires
as well as general panic In the event of major earthquake the evacuation procedures outlined
in Appendix will be followed
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6.4 Terrorist/Bomb Threat
In the event that any person should receive threat of bomb the following evacuation
procedure should be followed
Notify any person of authority i.e Superintendent Foreman Radiation Safety Officer
who will immediately notify law enforcement authorities and evacuate the threatened
area
Evacuate all persons from the affected area and stop all radio transmissions
6.5 Tailings Dam Break and Major Floods
Flood water breaching tailings embankments presents one of the greatest dangers for the sudden
release of tailings solids and impounded water The tailings cells are designed with sufficient
freeboard three feet to withstand back-to-back 00-year storm events or 40%of the probable
maximum flood PMF followed by the 100-year storm event The flood design is equivalent to
15 inches of rainfall In addition the tailings dikes were designed in accordance with U.S NRC
regulations and allow sufficient margin of safety even in the event of an earthquake
The possibility of floods resulting from Westwater Creek Cottonwood Creek and Corral Creek
causing dam failure is extremely remote
The tailings cells and dikes are inspected on both daily and shift basis
Discharges from dike failure would extend three miles before leaving IUSAs property In the
event of dam failure large operating equipment will be mobilized to construct temporary
earthen dikes or berms downgradient to the failed dike In addition the State of Utah
Department of Radiation Control Executive Secretary the Executive Secretary MSHA and
State of Utah Department of Natural Resources Division of Dam Safety shall be notified
In the event of seismic rupture of tailings slurry pipelines the released slurry will be contained
in the tailings cells regardless of the quantity released
EVACUATION PROCEDURE See Appendix
7.1 Notification
Employees will be notified to evacuate the area by dialing 184 on any area telephone and
announcing that the Mill should be evacuated This announcement will be repeated twice When
the paging system cycles through the evacuation siren continuous frequency will automatically
sound for approximately forty-five seconds and then automatically shut off allowing
communications by radio from that point If the 184 number is dialed accidentally the
evacuation alarm may be canceled by disconnecting the phone until the page cycle ends then re
dial 184 See Exhibits and
7.2 Assembly
When the evacuation alarm sounds or when personnel are verbally notified by radio or other
means all personnel will assemble at
The parking lot south of the office
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The scalehouse
North side of Tailings Cell or
North of the Mill
Assembly site will depend upon conditions i.e nature of the emergency wind conditions etc
The Fire Chief or Shift Foreman will specify the appropriate assembly site
7.3 Specific Procedure for Operations Personnel
See specific emergency shutdown procedure for Operations by area under the relevant
Operating Procedure for your area
All employees not mentioned under Operating Procedures are to immediately report to
the assembly area and congregate by crew so that all persons can be accounted for As
employees leave their work areas they must pass the word to evacuate to any persons
who may not be aware of the emergency
After the Mill has been detennined to be safe for re-entry employees will be verbally
notified to return to their work stations
Off-Site Emergency Equipment/Personnel Release
Any emergency response equipment or personnel that enter the Restricted Area in response to an
incident will be scanned and decontaminated prior to leaving the site according to the procedures
included in PBL-9 End Dump Trailer Acceptance Handling and Release Any equipment will
be decontaminated according to the requirements found in Table of the Nuclear Regulatory
Commissions NRCs Policy and Guidance Directive FC-85-23 Guidelines for
Decontamination of Facilities and Equipment Prior to Release for Unrestricted Use or
Termination of Licenses for Byproduct Source or Special Nuclear Material issued May 1987
Injured personnel should be evaluated for radiation contamination if there was potential for
contamination at the earliest convenience Should it be necessary contaminated articles will be
gathered by the radiological staff after medical treatment has been rendered If the personnel
cannot be decontaminated notify the clinic/hospital personnel in advance
EMERGENCY EQUIPMENT
Emergency equipment for the Mill is provided as follows
9.1 Fire Hose
Fire hose cabinets are located at the following sites with minimum of 300 feet of 2-1/2 hose
two spanner wrenches spray nozzles and one hydrant wrench
South of SX
West of CCD
North of Mill Building
East of pulp storage tanks
Northwest of Maintenance Shop
West of Warehouse
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East of office building
9.2 Self Contained Breathing Apparatus
Two Self-Contained Breathing Apparatus
are located at each of the following locations
Hose station east of office building
Hose Station South of SX
North End SX Outside Wall
North end of Mill building outside wall
9.3 Spill Clean-up Equipment
Barrels of soda ash are located throughout the Mill to be used in case of chemical spill Soda
ash is also stored in bulk if needed There are also few drums of absorbent stored near the
laboratory The laboratory also contains acid spill kits and absorbent materials to be used in case
of spill
9.4 Fire Fighting PPE
Two complete sets of turnout gear for fire fighting and/or emergency extrication are located in
the Fire Hose Station located on the east side of the office building
9.5 Maintenance of Emergency Equipment
Fire extinguishers are inspected on an annual basis as well as the fire pump system The Mill
Safety Coordinator performs regular spot checks on the emergency equipment locations to ensure
that all of the equipment is in place
10 EMERGENCY TRANSPORTATION
One fully-equipped First Responder Unit Ambulance located west of the office building
Other motor pool vehicles on the property will be utilized as needed in emergency situations with
support as needed from the local Emergency Medical Services
11 EMERGENCY DRILLS AND TRAINING
Quarterly drills as required by MSHA are prepared by the Safety and Radiation Departments to
monitor performance of personnel responding to emergency situations Each drill will be
enacted upon one or more of the potential scenarios by this plan The drill and evacuation
activities are documented by the Mills Safety Coordinator and maintained within plant files
Management will review all drills at quarterly ALARA Committee Meetings
P\Admin\Master SOPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc 13
EXHIBIT
EMERGENCY NOTIFICATION LIST
ATTEND TO ANY INJURED PERSONS AND NOTIFY THE SUPERVISOR
Give artificial respiration if necessary
Control bleeding
Treat for shock
Immobilize fractures and stabilize for transportation
Scan the injured for excessive alpha prior to transporting if time allows
If alpha is excessive or there is no time to scan notify the clinic/hospital personnel and the
Radiation Safety Office
TIlE SUPERVISOR OR HIS DESIGNEE WILL NOTIFY THE FOLLOWING AS NEEDED
Blanding Clinic 678-2254 or 678-3434 930 400
San Juan Hospital Monticello ...678-2830 or 587-2116 364 1st
EMT and CPR TRAINED The following personnel should be contacted if they are on-site in the
event of an emergency to aid in the event of any injuries to personnel
David Turk EMT and CPR trained
Mike Spiliman CPR trained
AMBULANCE SERVICE
Blanding Dial 911
If the Company Ambulance is used an attendant must ride with the injured in addition to the driver
except where the injured could normally be transported in car or pickup
OTHER EMERGENCY NUMBERS
Fire Department Dial 911 or 678-2313
County Sheriff Dial 911 or 587-2237
Highway Patrol Dial 911 or 587-2000
Blanding Police Dial 911 678-2916 or 678-2334
MANAGERS
The Supervisor will notify one of the following of all incidents
R.E Bartlett 435-678-2495
Turk 435-678-7802 or 435-459-1068
Spiliman 435-678-2761
MEMBER OF MANAGEMENT WILL NOTIFY THE PROPER REGULATING AGENCIES
AS REQUIRED FOR EACH INCIDENT
State of Utah Department of Radiation Control 801-536-4250
MSHA Field Off.--801-524-3450 Dist Off 303-231-5465
MSHA Arlington 800-746-1553
State Emergency Response Comm 801-538-3400
State of Utah Natural Resources Dam Safety 801-538-7200
National Response Center 800-424-8802
Utah Poison Control Center 800-456-7707
Notification of surrounding communities and or residences will be handled by the appropriate agencies as
required by EPCRA Emergency Planning and Community Right to Know Act
Revision Date Januaiy 16 2006 Ed
EXHIBIT
INTERNAL NOTIFICATIONS
Internal reporting requirements for Incidents Spills and Significant Events are as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions or other accidents
Government investigations information requests or enforcement actions
Private actions or claims corporations or employees
Deviations from Corporate policies or government requirements by Management
Other significant events which have resulted or could result in
Death serious injury or adverse health effect employees or public
Property damage exceeding $1000000
Government investigation or enforcement action limiting operation or penalties
of $100000 or more
Significant criminal actions
Substantial media coverage
Unscheduled down time of more than 24 hours
Renort at the Beginning of the Next Business Day
Incident Criteria
Was reported to government agency as required by law
Worker uSA or contractor recordable injury or illness associated with release
Community impact reported or awareness
Publicity resulted or is anticipated
Release of process material waste or product in excess of the Reportable
Quantities listed in Section 1.5 of the Spill Prevention Control and
Countermeasures Plan
The local manager in charge is to call Ron Hochstein or Dave Frydenlund
Name Title Office Phone Home Phone
Ron Hochstein President and COO 303-628-7798 office
604-931-6334 home
604-377-1167 cell
David Frydenlund V.P and General Counsel 303-389-4130 office
303-221-0098 home
303-808-6648 cell
Master SOPs\Book 16_Emergency Response PlarAEmergcncy Response Plan Rev 002.14.07 E-2
EXHIBIT
SITE LAYOUT MAP
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-3
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EXHIBIT
MAIN SHUT-OFF VALVES
During an emergency this list should be used along with Site Layout Map Exhibit to locate
tanks and valves associated with these tanks
REAGENT SHUT-OFF VALVE LOCATIONS
Sulfuric Acid
Main located south side of acid tank
East acid pump discharge valve
West acid pump discharge valve
Main leach area located 25 feet west of Derrick screens next to walkway
1-1/2 Main SX area located south of Central Control room
Ammonia
Main east tank located on end at bottom
Main west tank located on end at bottom
Valve located on top of tank east tank
Valve located on top of tank west tank
Kerosene
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Pump discharge valve
Soda Ash
Main valve located at bottom of tank dry storage
Main valve located at bottom of tank on 30%dilution tank
Main valve locate at bottom of tank on dilution tank
Salt
Main valve located at bottom of tank
Caustic Soda
Main valve located at bottom of tank east and west between supports
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
EXIIIBIT
MAIN SHUT-OFF VALVES
Sodium Chlorate
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Propane
Main located 15 feet east of tank
Main located on pipe off top of tank
Main located at bottom of tank also fill pipe
PLANT UTILITY SHUT-OFF VALVE LOCATIONS
Process Water
Main valve located on west side of water storage tank
Discharge valve off service water pump east
Discharge valve off service water pump west
Mill process water main located east wall by SAG mill
Fire Water
Main valve located west side of water storage tank
Emergency fire pump discharge valve to fire system
Emergency fire pump discharge valve to header west side of pump house
Main valve located south of Central Control room for SX and boilers
Potable Water
Main suction from potable water storage tank
Main discharge from potable water storage tank
Main located at east wall by SAG mill
Main located south of Central Control room for SX Maintenance shop and offices
Steam
Main discharge valve for Superior boiler located at top of boiler
Main steam valve located south side of boiler house
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
EXHIBIT
MAIN SHUT-OFF VALVES
Plant Air
Main valve located at receiver tank in compressor room at boiler house
Main valve to mill building located south of Central Control room
PROCESS SHUT-OFF VALVE LOCATIONS
Pulp Storage
No valve located on west side of tank
No valve located on west side of tank
Preleach old No pulp storage valve located on west side of tank
Preleach Thickener
Main valve located underneath at center cone
Clarifier
Main valve located underneath at center cone
Main valve located underneath at center cone
CCD Thickeners
Main valve located underneath at center cone of each thickener
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc E-4
APPENDIX
EMERGENCY PROCEDURE RESPONSE TO FIRE
The fire will be reported by dialing 185 on any telephone in the area and announcing the
location of the fire over the paging system This announcement will be repeated twice
for total of three announcements When the paging system cycles through the fire siren
alternating frequency will automatically sound for approximately forty-five seconds
then automatically shut off allowing radio communications to resume
Mobilize the fire crew
Evacuate all personnel
Rescue any victims of the fire do this only with properly trained and equipped personnel
Isolate utility lines affected by the fire
Extinguish the fire and post fire watch for flare-ups
Report the fire to proper local State Corporate and Federal agencies
In cases where the fire is not extinguished within thirty minutes of discovery the area
t...-..4 1-.-...-.a IAOTIA
lflUnL tic tuuiicaucu Un aiLc1 cAwlgunrnJlg CUJU ICIL WIUILU1UCU wan icxca5cu vy nuorln
and IUSA management
Emergency off-site centers Blanding Fire House and Sheriffs office
Blanding Fire
350 West 200 South Blanding
Phone number is 911
Sheriffs Office
50 West 100 South Blanding
Phone number is 911 or 435 587-2237
P\Admin\Master 5OPs\Book 6_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc A-I
APPENDIX
EMERGENCY PROCEDURE
RESPONSE TO CHEMICAL OR GAS RELEASE
chemical or gas release would most likely occur very suddenly The person who would first
witness chemical or gas release should immediately contact his supervisor who would initiate
the procedures outlined below
Activate evacuation alarm by using the dial 184 notification system Evacuate mul
account for all personnel
Mobilize trained personnel and emergency equipment such as SCBAs first aid
equipment etc
Initiate rescue operations for any people who may be trapped by the release
Provide first aid and emergency medical care for any ill or injured persons
Initiate necessary steps to contain and/or neutralize the release such as spraying with
water fog turning off valves etc
Guard against possible fires by shutting off electrical circuits isolating gas lines and
alrnn0tn nntnn on.rna frnrn 4ha oPfansA 0mbOJt41%.IUI1 L1I%ass%.JL%.tt Wta
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.054oc A-I
APPENDIX
EMERGENCY EVACUATION PROCEDURE
Activate evacuation alann by using the dial 184 notification system Evacuate and account
for all personnel
Personnel are to assemble in one of the following areas
The parking lot south of the office building
The scalehouse
The north side of Tailings Cell or
North of the Mill
Mobilize trained personnel and emergency equipment such as SCBAs first aid equipment
etc
Initiate rescue operations for any people who may be trapped
Provide first aid and emergency medical care for any ill or injured persons
Guard against possible fires by shutting off electrical circuits isolating gas lines and
eliminating ignition sources frbm the affected area
P\Mmin\Master 5OPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc A-I
FIGURE
FIRE SYSTEM SCHEMATIC DRAWING
PfAdmin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-I
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STORM WATER
BEST MANGEMENT PRACTICES PLAN
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Blanding Utah
June 2008
Prepared by
Denison Mines USA Corp
1050 17th Street Suite 950
Denver CO 80265
TABLE OF CONTENTS
1.0 Purpose
2.0 Scope
3.0 Responsibility
4.0 Best Management Practices
4.1 General Management Practices Applicable to All Areas
4.2 Management Practices for Process and Laboratory Areas
4.3 Management Practices for Maintenance Activities
4.4 Management Practices for Ore Pad Tailings Area and heavy Equipment
Operations
Figures
Figure White Mesa Mill Site Map
Figure Mill Site Drainage Basins
Figure JUSA Mill Management Organization Chart
Figure IIJSA Corporate Management Orgathzation Chart
Tables
Table White Mesa Mill Management Personnel Responsible for Implementing
This BMPP
Appendices
Appendix White Mesa Mill Spill Prevention Control and Countermeasures Plan
Appendix White Mesa Mill Emergency Response Plan
Best Management Practices Plan
Revision 1.3 June 12 2008
1.0 INTRODUCTION/PURPOSE
Denison Mines USA Corp DUSA operates the White Mesa Uranium Mill the Mill in
Blanding Utah The Mill is net water consumer and is zero-discharge facility with respect to
water effluents That is no water leaves the Mill site because the Mill has
no outfalls to public stormwater systems
no surface runoff to public stormwater systems
no discharges to publicly owned treatment works POTW5 and
no discharges to surface water bodies
The State of Utah issued Groundwater Discharge Permit No UGW3 70004 to DUSA on March
2005 As part of compliance with the Permit DUSA is required to submit Stormwater Best
Management Practices Plan BMPP to the Executive Secretary of the Division of Radiation
Control Utah Department of Environmental Quality This BMPP presents operational and
management practices to minimize or prevent spills of chemicals or hazardous materials which
could result in contaminated surface water effluents potentially impacting surface waters or
ground waters through runoff or discharge connections to stormwater or surface water drainage
routes Although the Mill by design cannot directly impact stormwater surface water or
groundwater the Mill implements these practices in good faith effort to minimize all sources of
pollution at the site
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
2.0 SCOPE
This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in
process operations laboratory operations and maintenance activities and minimize spread of
particulates from stockpiles and tailings management areas at the Mill Storage of ores and
alternate feeds on the ore pad and containment of tailings in the Mill tailings impoundment
system are not considered spills for the purposes of this BMPP
The Mill site was constructed with an overall grade and diversion ditch system designed to
channel all surface runoff including precipitation equivalent to Probable Maximum
PrecipitationlProbable Maximum Flood PMP/PMF storm event to the tailings management
system In addition Mill tailings all other process effluents all solid waste and debris except
used oil and recyclable materials and spilled materials that cannot be recovered for reuse are
transferred to one or more of the tailings cells in accordance with the Mills NRC license
conditions All of the process and laboratory building sinks sumps and floor drains are tied to
the transfer lines to the tailings impoundments site map of the Mill is provided in Figure
sketch of the site drainage basins is provided in Figure
As result unlike other industrial facilities whose spill management programs focus on
minimizing the introduction of chemical and solid waste and wastewater into the process sewers
and storm drains the Mill is permitted by NRC license to manage some spills via draining or
washdown to the process sewers and ultimately the tailings system However as good
environmental management practice the Mill attempts to minimize
the number and size of material spills and
the amount of unrecovered spilled material and washwater that enters the process sewers
after spill cleanup
Section 4.0 itemizes the practices in place at the Mill to meet these objectives
Requirements and methods for management recordkeeping and documentation of hazardous
material spills are addressed in the DUSA White Mesa Mill Spill Prevention Control and
Countermeasures SPCCPlan Revised February 2007 the Emergency Response Plan
ERP also revised in February 2007 and the housekeeping procedures incorporated in the
White Mesa Mill Standard Operating Procedures SOPs The SPCC plan and the ERP are
provided in their entirety in Appendices and respectively
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
3.0 RESPONSIBILITY
All Mill personnel are responsible for implementation of the practices in this BMPP DUSA
White Mesa Mill management is responsible for providing the facilities or equipment necessary
to implement the practices in this BMPP
The Mill Management Organization is presented in Figure The DUSA Corporate
Management Organization is presented in Figure
An updated spill prevention and control notification list is provided in Table
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.0 BEST MANAGEMENT PRACTICES
summary list and inventory of all liquid and solid materials managed at the Mill is provided in
Tables through
4.1 General Management Practices Applicable to All Areas
4.1.1 Keep Potential Pollutants from Contact with Soil and Surface Water
Store hazardous materials and other potential pollutants in appropriate containers
Label the containers
Keep the containers covered when not in use
4.1.2 Keep Potential Pollutants from Contact with Precipitation
Store bulk materials in covered tanks or drums
Store jars bottle or similar small containers in buildings or under covered areas
Replace or repair broken dumpsters and bins
Keep dumpster lids and large container covers closed when not in use to keep
precipitation out
4.1.3 Keep Paved Areas from Becoming Pollutant Sources
Sweep paved areas regulariy and dispose of debris in the solid waste dumpsters or
tailings area as appropriate
4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the
Process and Reagent Storage Area
Diversion ditches drainage
channels and surface water control structures in and around
the Mill area will be inspected at least weekly in accordance with the regularly scheduled
inspections required by Groundwater Discharge Permit No UGW370004 and
Byproduct Materials License UT1900479 Areas requiring maintenance or repair such
as excessive vegetative growth channel erosion or pooling of surface water runoff will
be report to site management and maintenance departments for necessary action to repair
damage or perform reconstruction in order for the control feature to perform as intended
Status of maintenance or repairs will be documented during follow up inspections and
additional action taken if necessary
4.1.5 Recycle Fluids Whenever Possible
When possible select automotive fluids solvents and cleaners that can be recycled or
reclaimed
When possible select consumable materials from suppliers who will reclaim empty
containers
Keep spent fluids in properly labeled covered containers until they are picked up for
recycle or transferred to the tailings area for disposal
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.2 Management Practices for Process and Laboratory Areas
4.2.1 Clean Up Spills Properly
Clean up spills with dry cleanup methods absorbents sweeping collection drums
instead of water whenever possible
Clean spills of stored reagents or other chemicals immediately after discovery
Groundwater Discharge Permit No UGW370004 Section I.D.8.c
Recover and re-use spilled material whenever possible
Keep supplies of rags sorbent materials such as cat litter spill collection drums and
personnel protective equipment PPE near the areas where they may be needed for
spill response
If spills must be washed down use the minimum amount of water needed for effective
cleanup
4.2.2 Protect Materials Stored Outdoors
If drummed feeds or products must be stored outdoors store them in covered or diked
areas when possible
If drummed chemicals must be stored outdoors store them in covered or diked areas
when possible
Make sure drums and containers stored outdoors are in good condition and secured
against wind or leakage Place any damaged containers into an overpack drum or second
container
4.2.3 Water Management
When possible recycle and reuse water from flushing and pressure testing equipment
When possible wipe down the outsides of containers instead of rinsing them off in the
sink
When possible wipe down counters and work surfaces instead of hosing or rinsing them
off to sinks and drains
4.2.4 Materials Management
Purchase and inventory the smallest amount of laboratory reagent necessary
Do not stock more of reagent than will be used up before its expiration date
All new construction of reagent storage facilities will include secondary containment
which shall control and prevent any contact of spilled reagents or otherwise released
reagent or product with the ground surface Groundwater Discharge Permit No
UGW370004 Section I.D.3.e
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.3 Management Practices for Maintenance Activities
4.3.1 Keep Clean Dry Shop
Sweep or vacuum shop floors regularly
Designate specific areas indoors for parts cleaning and use cleaners and solvents only in
those areas
Clean up spills promptly Dont let minor spills spread
Keep supplies of rags collection containers and sorbent material near each work area
where they are needed
Store bulk fluids waste fluids and batteries in an area with secondary containment
double drum drip pan to capture leakage and contain spills
4.3.2 Manage Vehicle Fluids
Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as
possible Use drip pans or plastic tarps to prevent spillage and spread of fluids
Promptly contain and transfer drained fluids to appropriate storage area for reuse recycle
or disposal
Recycle automotive fluids if possible when their useful life is finished
4.3.3 Use Controls During Paint Removal
Use drop cloths and sheeting to prevent windbome contamination from paint chips and
sandblasting dust
Collect contain and transfer as soon as possible accumulated dusts and paint chips to
disposal location in the tailings area authorized to accept waste materials from
maintenance or construction activities
4.3.4 Use Controls During Paint Application and Cleanup
Mix and use the right amount of paint for the job Use up one container before opening
second one
Recycle or reuse leftover paint whenever possible
Never clean brushes or rinse or drain paint containers on the ground paved or unpaved
Clean brushes and containers only at sinks and stations that drain to the process sewer to
the tailings system
Paint out brushes to the extent possible before water washing water-based paint or
solvent rinsing oil-based paint
Filter and reuse thinners and solvent whenever possible Contain solids and unusable
excess liquids for transfer to the tailings area
Page
Best Management Practices Plan
Revision 1.3 June 12 2008
4.4 Management Practices for Ore Pad Tailings Area and Heavy Equipment
Detailed instructions for ore unloading dust suppression and tailings management are provided
in the Mill SOPs
4.4.1 Wash Down Vehicles and Equipment in Proper Areas
Wash down trucks trailers and other heavy equipment only in areas designated for this
purpose such as washdown pad areas and the truck wash station
At the truck wash station make sure the water collection and recycling system is working
before turning on water sprays
4.4.2 Manage Stockpiles to Prevent Windborne Contamination
Water spray the ore pad and unpaved areas at appropriate frequency in accordance with
Mill SOPs
Water spray stockpiles as required by opacity standards or weather conditions
Dont over-water Keep surfaces moist but minimize runoff water
4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources
Schedule excavation grading and other earthmoving activities when extreme dryness and
high winds will not be factor to prevent the need for excessive dust suppression
Remove existing vegetation only when absolutely necessary
Seed or plant temporary vegetation for erosion control on slopes
Page
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Home Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.l66
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Home Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE
REAGENT YARD LIST
REAGEN1/L t-UAt4mitBS
2-
UMBERO
STORAGETANKS
-PAC WL
4GALWNSV
ADOGEN 2382 6120
ADVANTAGE 1O1M 2475
AMERSJTE2
AMINE 2384 19440
AMMONIUM SULFATE BULK 54000
AMMONIUM SULFATE BAGS 4300
ANHYDROUS AMMONIA 107920 31409
CHEMFAC 100 12800
CLARIFLOC N-1O1P 3000
DECYLALCOHOL 45430
DIESEL FUEL 250
6000
FLOCCULENTM1O11N 30550
FLOCCULENT M1302C 3550
GRINDING BALLS 48290
ISODECANOL 45430
KEROSENE 1344 10152
MACKANATE 3150
MILLSPERSE 802 1410
NALCO 2458
NALCO 8815
PERCOL 351 1500
PERCOL 406 13950
PERCOL 745
POLOX 10360
POLYHALL YCF
PROPANE 30000
SALT BAGS 39280
SALT BULK
SODA ASH BAGS 39280
SODA ASH BULK 84100 16921
8530
SODIUM CHLORATE 101128 17700
10500
SODIUM HYDROXIDE 19904
SULFURIC ACID 4801440 1600000
269160
UNLEADED GASOLINE 3000
USED OIL 5000
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
Chemical in Lab RQ2 Quantity In Stock
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
6M kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
Chemical in Volatiles and RQ2 Quantity In Stock
Flammables Lockers AIBC
Chloroform 4.54 kg
Formaldehyde 45.4 kg of 37%solution
Nitrobenzene 454 kg 12
Toluene 454 kg 12L
Chemical in Acid Shed RQ2 Quantity In Stock
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARD/SMALL QUANTITY CHEMICALS LIST1
ay
1000 lbs
ftM POiJtPt
gal
1000 lbs 5L
100 lbs lbs
10 lbs kg 4.4 Ibs
10 lbs lbs
Heptahydrate 1000 lbs kg 11 Ibs
5000 lbs 60 gal of 40%
solution
1000 lbs 10
0.1 32 gal 5kg 11 Ibs
5.5%100 lbs kg 11 Ibs of
5.5%solution
lb lbs
100 lb
100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Part 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
TABLE 5.0
REAGENT YARDIBULK CHEMICALS LIST1
Sulfuric Acid
Floc 301
Hyperfloc 102
Ammonia East Tank
Ammonia West Tank
Kerosene
Salt Bags
Ammonium Hydrogendifluoride
Soda Ash Dense Bag
Phosphoric Acid
Polyox
Millsperse
Nalco TX760
Nalco 7200
Tributyl phosphate
Distillates
Diesel
Gasoline
Alamine 336 drums
Floc 109
Floc 208
Floc 904
Hyperfioc 624
Salt Bulk solids
Salt Bulk solutions
Caustic Soda
Ammonium Sulfate
Sodium Chlorate
Alamine 335 Bulk
Alamine 310 Bulk
Isodecanol
Vanadium Pentoxide3
Yellowcake3
Ammonia Meta Vanadate
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the clean Water Act
REAGENT RQ2 QUANTITY IN
REAGENT YARD
1000 lbs
None
None
100 lbs
100 lbs
100 gal
None
None
None
5000 lbs
None
None
None
None
None
None
100 gal
100 gal
None
None
None
None
None
None
None
1000 lbs
None
None
None
None
None
1000 lbs
None
1000 lbs
9000000 lbs
1200 lbs
1500 lbs
lbs
105000 lbs
500 gal
2000 lbs
20450 lbs
lbs
6300 lbs
490 lbs
1410 lbs
barrels
1590 lbs
9450 lbs
100 gal
Approx 3300 gal
Approx 6000 gal
lbs
lbs
lbs
lbs
lbs
lbs
lbs
lbs
lbs
20000 lbs
lbs
lbs
lbs
30000 lbs
100000 lbs
lbs
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
PRODUCT QUANTITY
WAREHOUSE
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
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Mill Site Layout
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White Mesa Mill
Mill Site Drainage Basins
Figure
White Mesa Mill
Mill Management Organization Chart
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Corporate Management Organization Chart
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APPENDICES
APPENDIX
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN
FOR CHEMICALS AND PETROLEUM PRODUCTS
for
White Mesa Uranium Mill
6425 South Highway 191
P.O Box 809
Blanding Utah 84511
February 2007
Prepared by
Denison Mines USA Corp
1050 7th Street Suite 950
Denver Colorado 80265
TABLE OF CONTENTS
SECTION PAGE
1.1 Objective
1.2 Responsibilities
1.3 Drainage Basins Pathways and Diversions
1.4 Description of Basins
1.4.1 Basin Al
1.42 Basin A2
1.4.3 Basin BI
1.4.4 Basin B2
1.4.5 Basin B3
1.4.6 Basin
1.4.7 Basin
1.4.8 Basin
1.5 Potential Chemical Spill Sources And Spill Containment
1.5.1 ReagentTanks
1.5.2 Ammonia
1.5.3 Ammonium Meta Vanadate
1.5.4 Caustic Storage Sodium Hydroxide
1.5.5 Sodium Carbonate
1.5.6 Sodium Chlorate
1.5.7 Sulfuric Acid
1.5.8 Vanadium Pentoxide
1.5.9 Kerosene Organic
1.6.0 Used/Waste Oil
SECTION PAGE
1.6.1 Propane
1.7 Potential Petroleum Sources And Containment
1.7.1 Petroleum Storage Tanks
1.7.1.1 Diesel
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.2 Unleaded Gasoline
1.7.2.3 Pump Station
11.2.4 Truck Unloading
1.8 Spill Discovery And Remedial Action
1.9 Spill Incident Notifications
1.9.1 External Notification
1.9.2 Internal Notification 11
1.10 Records And Reports 12
1.11 Personnel Training And Spill Prevention Procedures 12
1.11.1 Training Records 12
1.11.2 Monitoring Reports 13
1.12 Revision 13
1.13 Summary 13
1.14 Mill Manager Approval 14
1.15 Certification by Registered Professional Engineer 14
LIST OF TABLES
Table 1.0 Mill Organization Chart
Table 2.0 Reagent Tank List
Table 3.0 Laboratory Chemical Inventory List
Table 4.0 Reagent Yard/Small Quantity Chemicals List
Table 5.0 Reagent Yard/Bulk Chemicals List
Table 6.0 Petroleum Products and Solvents List
LIST OF FIGURES
Figure Miii Site Layout
Figure Mill Site Drainage Basins
WHITE MESA MILL
SPILL PREVENTION CONTROL AND COUNTERMEASURES
PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS
1.1 OBJECTIVE
The objective of the Spilt Prevention Control and Countermeasures SPCC
Plan is to serve as site-specific guideline for the prevention of and response to
chemicat and petroteum spilts and as guidance document for compliance with
Groundwater Discharge Permit No UGW370004 The ptan outlines spill
potentials containment areas and drainage characteristics of the White Mesa
Mill site The plan addresses chemical spill prevention spitt potentials spill
discovery and spilt notification procedures The Oil Pollution Prevention Sections
of the Clean Water Act 40 CFR 112 to 117 atso referred to as the Spitl
Prevention Control and Countermeasures SPCC rutes estabtish
requirements that appty to facilities which coutd reasonabty be expected to
discharge oit in quantities that may be harmful as described in that Act into or
upon the navigabte waters of the United States or that may affect natural
resources of the United States Section 112 states that the Act is not appticable
to facilities that are not subject to the authority of the Environmental
Protection Agency EPA for one of the fottowing reasons
Due to its tocation the facitity coutd not reasonably be expected to
discharge oit into navigabte waters of or impact naturat resources of the
U.S or
The facility is subject to authority of the Department of Transportation as
defined in Memorandum of Understanding MOU between the
Secretary of Transportation and the EPA Administrator or
The facility does not exceed either the underground or the above ground
storage capacity 42000 gatlons and 1320 gatlons respectively
prescribed in the rutes
The Milt could not reasonabty be expected as described in the SPCC regutation
to discharge oil into the navigable waters or impact naturat resources of the
U.S The Mitt site was constructed with an overalt grade and diversion ditch
system designed to channel the non-recovered portion of any material spill to the
tailings management system Hence it is not reasonabte to expect that surface
spills will ever reach navigable waters or naturat resources of the U.S or Utah
Therefore the SPCC reporting requirements in the Clean Water Act are not
appticable to the Milt However as good environmental management practice
the Mitt has implemented the spitl management program described in this
document which is consistent with the intent of the Clean Water Act to the
extent practicable Although the Mill by design cannot directly impact navigable
waters of the U.S and as result spills that may occur but are retained within
the site would not be reportable the Mill implements these practices in good
faith effort to minimize all potential sources of pollution at the site
Storage of ores and alternate feeds on the ore pad and containment of tailings
in the Mill tailings impoundment system are not considered spills for the
purposes of this SPCC
Ammonia is the only chemical that has the potential to leave the site and would
do so as vapor
Figure Site Layout Map shows map of the mill site including the locations of
the chemical tanks on-site Figure shows the basins and drainage ditch areas
for the mill site Table 1.0 is an organization chart for Mill operations Table 2.0
lists the reagent tanks and their respective capacities Table 3.0 lists the
laboratory chemicals their amounts and their reportable quantities Table 4.0
lists the operations chemicals Table 5.0 lists the chemicals in the reagent yard
their amounts and their reportable quantities Table 6.0 lists the petroleum
products and solvents on site
1.2 RESPONSIBILITIES
Person in charge of facility responsible for spill prevention
Mr Richard Bartlett Interim Mill Manager
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 459-2495 home
Person in charge of follow-up spill record keeping and/or reporting
Mr David Turk Department Head Health Safety and Environmental
6425 South Highway 191
Blanding UT 84511
435 678-2221 work
435 678-7802 home
Refer to Section 1.9 Spill Incident Notification for list of company personnel
to be notified in case of spill In addition an organizational chart is provided
in Table 1.0
1.3 DRAINAGE BASINS PATHWAYS AND DIVERSIONS
The main drainage pathways are illustrated in Figure The map shows
drainage basin boundaries flow paths constructed diversion ditches tailings
cells the spillway between Cell and dikes berms and other relevant
features The White Mesa Mill is zero discharge facility for process liquid
wastes The mill area has been designed to ensure that all spills or leaks
from tanks will drain toward the lined tailings cells
The tailings cells in turn are operated with sufficient freeboard minimum of
three feet to withstand 100%of the PMP Probable Maximum Precipitation
This allows for maximum of 10 inches of rain at any given time
1.4 DESCRIPTION OF BASINS
Precipitation and unexpected spills on the mill property are contained within
their respective drainage basins Runoff would ultimately drain into one of
the three lined tailings cells
1.4.1 Basin Al
Basin Al is north of Cell 1-I and Diversion Ditch No The basin
contains 23 acres all of which drain into Westwater Creek This area is
not affected by mill operations
1.4.2 Basin A2
Basin A2 contains all of Cell 1-I including an area south of the Diversion
Ditch No The basin covers 84 acres Any runoff from this basin
would be contained within Cell 1-I
1.4.3 Basin Bl
Basin Bl is north of the mill property and is not affected by mill
operations The basin contains 45.4 tributary acres Runoff from this
basin drains into flood retention area by flowing through Diversion Ditch
No Diversion Ditch No drains into Westwater Creek
1.4.4 Basin B2
Basin B2 is northeast of the mill and contains only 2.6 acres Runoff from
this basin would drain into Diversion Ditch No Diversion Ditch No
ultimately drains into Diversion Ditch No This basin is not affected by
mill operations
1.4.5 Basin B3
Basin B3 contains most of the mill area buildings ore stockpiles process
storage tanks retention ponds spill containment structures pipelines
and roadways The normal direction of flow in this basin is from the
northwest to the southwest Any runoff from this basin would drain into
Cell 1-I The basin contains 64 acres This basin has sufficient
freeboard to withstand 100%of the PMP Probable Maximum
Precipitation This allows 10 inches of rain for any given storm event
1.4.6 Basin
Basin contains all of Cell The basin consists of 80.7 acres This
basin contains earth stockpiles and the heavy equipment shop The
direction of flow in this basin is to the southwest All runoff in this basin
would be channeled along the southern edge of the basin Runoff would
then flow into Cell via the spillway from Cell to Cell
1.4.7 Basin
Basin contains all of Cell This basin consists of 78.3 acres including
portion of the slopes of the topsoil stockpile and random stockpile The
basin contains all flows including those caused by the PMF
1.4.8 Basin
Basin contains Cell 4A and consists of 43.3 acres All anticipated flows
including those caused by the PMF will be contained within the basin and
will flow directly into Cell 4A
1.5 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL
CONTAINMENT
This section details potential sources of chemical spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States Reportable
Quantities are those identified in 40 CFR Pad 117 Table 117.3 Reportable Quantities
of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act
It is not expected that any spill would reach navigable waters of the United States
However if spill of volume listed below occurs and remains on the mill site which is
the more likely scenario then management is to be notified so that proper internal
evaluations of the spill are made
1.5.1 Reagent Tanks Tank list included in Table 2.0
1.5.2 Ammonia
The ammonia storage tanks consist of two tanks with capacity of
31409 gallons each The tanks are located southeast of the Mill building
Daily monitoring of the tanks for leaks and routine integrity inspections will be
conducted to minimize the hazard associated with ammonia The reportable
quantity for an ammonia spill is gallons
Ammonia spills should be treated as gaseous Ammonia vapors will be
monitored closely to minimize the hazard associated with inhalation If
vapors are detected efforts will be made to stop or repair the leak
expeditiously Ammonia is the only chemical as vapor that has the
potential to leave the site
1.5.3 Ammonia Meta Vanadate
Ammonia meta vanadate is present in the SX building as the process
solutions move through the circuit to produce the vanadium end product
But the primary focus will be on the transportation of this chemical The
reportable quantity for an ammonia meta vanadate spill is 1000 pounds
1.5.4 Caustic Storage Sodium Hydroxide
The caustic storage tank is located on splash pad on the northwest corner
of the SX building The tank has capacity of 19904 gallons The tank
supports are mounted on concrete curbed catchment pad that directs spills
into the sand filter sump in the northwest corner of the SX building The
reportable quantity for sodium hydroxide spill is 85 gallons
1.5.5 Sodium Carbonate Soda Ash
The soda ash solution tank has capacity of 16921 gallons and is located in
the northeast corner of the SX building The smaller soda ash shift tank has
capacity of 8530 gallons and is located in the SX building Spills will be
diverted into the boiler area and would ultimately drain into Cell 1-I There is
no reportable quantity associated with sodium carbonate spill
1.5.6 Sodium Chlorate
Sodium chlorate tanks consist of two fiberglass tanks located within dike
east of the SX building The larger tank is used for dilution purposes and has
maximum capacity of 17700 gallons The smaller tank serves as
storage tank and has capacity of 10500 gallons Daily monitoring of the
tanks for leaks and integrity inspections will be conducted to minimize the
hazard associated with sodium chlorate
Sodium chlorate that has dried and solidified becomes even more of safety
hazard due to its extremely flammable nature The reportable quantity for
sodium chlorate spill is 400 gallons
1.5.7 Sulfuric Acid
The sulfuric acid storage tanks consist of one large tank with the capacity of
16000000 gallons and two smaller tanks with capacities of 269160 gallons
each
The large tank is located in the northwest corner of mill area basin B3 and is
primarily used for acid storage and unloading The tank support for the large
tank is on mound above depression which would contain significant
spill All flows resulting would be channeled to Cell 1-I The tank is equipped
with high level audible alarm which sounds prior to tank overflows
concrete spill catchment with sump in the back provides added
containment around the base of the tank However the catchment basin
would not be able to handle major tank failure such as tank rupture The
resulting overflow would flow towards Cell 1-I
The two smaller storage tanks are located within an equal volume spill
containment dike east of the mill building The tanks are not presently in
use but are equipped with high level audible alarms
The reportable quantity for sulfuric acid spill is 65 gallons 1000 pounds
1.5.8 Vanadium Pentoxide
Vanadium pentoxide is produced when vanadium is processed through the
drying and fusing circuits and is not present in the vanadium circuit until after
the deammoniator Efforts will be made to minimize leaks or line breaks that
may occur in processes in the circuit that contain vanadium pentoxide
Special care will be taken in the transportation of this chemical The
reportable quantity for vanadium pentoxide spill is 1000 pounds
1.5.9 Kerosene Organic
The kerosene storage area is located in the central mill yard and has
combined capacity of 10152 gallons in three tanks Any overflow from these
three tanks would flow around the south side of the SX building and then into
Cell 1-I These tanks have drain valves which remain locked unless
personnel are supervising draining operations The reportable quantity for
kerosene spill is 100 gallons
1.6.0 Used Waste Oil
Used/Waste oil for parts washing is located north of the maintenance shop
in tank and has capacity of 5000 gallons The tank is contained within
concrete containment system Ultimate disposal of the used oil is to an EPA
permitted oil recycler Any oil escaping the concrete containment system will
be cleaned up Soil contaminated with used oil will be excavated and
disposed of in Cell
1.6.1 Propane
The propane tank is located in the northwest corner of the mill yard and has
capacity of 30000 gallons Daily monitoring of the tank for leaks and
integrity inspections will be conducted to minimize potential hazards
associated with propane leaks Propane leaks will be reported immediately
There is no reportable quantity associated with propane spill
1.7 POTENTIAL PETROLEUM SPILL SOURCES AND
CONTAINMENT
This section details potential sources of petroleum spills and reportable quantities For
purposes of this SPCC reportable quantity will be defined as quantities listed below
which could be expected to reach navigable waters of the United States It is not
expected that any spill would reach navigable waters of the United States However if
spill of volume listed below occurs and remains on the mill site which is the more
likely scenario then management is to be notified so that proper internal evaluations of
the spill are made
1.7.1 Petroleum Tanks
1.7.1.1 Diesel
Two diesel storage tanks are located north of the mill building The tanks
have capacities of 250 gallons each One of the diesel tanks is for the
emergency generator The other tank is located in the pumphouse on an
elevated stand Spillage from either tank would ultimately flow into Cell 1-I
The reportable quantity for diesel spill is 100 gallons
1.7.2 Aboveground Fuel Pump Tanks
1.7.2.1 Diesel
The diesel tank is located on the east boundary of Basin B3 and has
capacity of 6000 gallons The tank is contained within concrete catchment
pad The reportable quantity for diesel spill is 100 gallons
1.7.2.2 Unleaded Gasoline
The unleaded gasoline tank is located next to the diesel tank The unleaded
gasoline tank has capacity of 3000 gallons and is contained within the
same containment system as the diesel tank The reportable quantity for an
unleaded gasoline spill is 100 gallons
1.7.2.3 Pump Station
Both the diesel and the unleaded gasoline tanks will be used for refueling
company vehicles used around the mill site The pump station is equipped
with an emergency shut-off device in case of overflow during fueling In
addition the station is also equipped with piston leak detector and
emergency vent Check valves are present along
with tank monitor
console with leak detection system The catchment is able to handle
complete failure of one tank However if both tanks failed the concrete
catchment pad would not be able to contain the spill In this case
temporary berm would need to be constructed Absorbent diapers or floor
sweep would be used in an effort to limit and contain the spill The soil would
be cleaned up and placed in the authorized disposal area in Cell
1.7 2.4 Truck Unloading
In the event of truck accident resulting in an overturned vehicle in the mill
area proper reporting and containment procedures will be followed when
warranted such as when oil or diesel fuel is spilled Proper clean-up
procedures will be followed to minimize or limit the spill The spill may be
temporarily bermed or localized with absorbent compounds Any soils
contaminated with diesel fuel or oil will be cleaned up and placed in the
authorized disposal area in Cell
1.8 SPILL DISCOVERY AND REMEDIAL ACTION
Once chemical or petroleum spill has been detected it is important to take
measures to limit additional spillage and contain the spill that has already
occurred Chemical or petroleum spills will be handled as follows
The Shift Foreman will direct efforts to shut down systems if
possible to limit further release
The Shift Foreman will also secure help if operators are requiring
additional assistance to contain the spill
The Shift Foreman is also obligated to initiate reporting procedures
Once control measures have begun and personal danger is
minimized the Shift Foreman will notify the Production
Superintendent Maintenance Superintendent or Mill Manager
The Production or Maintenance Superintendent will notify the Mill
Manager who in turn will notify the Environmental Health and Safety
Manager
The Mill Manager will assess the spill and related damage and direct
remedial actions The corrective actions may include repairs clean
up disposal and company notifications Government notifications
may be necessary in some cases
If major spill continues uncontrolled these alternatives will be considered
Construct soil dikes or pit using heavy equipment
Construct diversion channel into an existing pond
Start pumping the spill into an existing tank or pond
Plan further clean-up and decontamination measures
1.9 SPILL INCIDENT NOTIFICATION
1.9.1 External Notification
As stated in Section 1.1 spills are not expected to reach navigable waters of
the United States If spill of reportable quantity occurs then mill and
corporate management must be notified and they will evaluate whether or not
the following agencies must be notified
EPA National Response Center 1-800-424-8802
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah 801/538-7200
Water Quality Division 801/538-6146
In case of tailings dam failure contact the following agencies
State of Utah Department of Environmental
Quality Division of Radiation Control 801/536-4250
State of Utah Natural Resources 801/538-7200
1.9.2 Internal Notification
Internal reporting requirements for incidents spills and significant spills are
as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions and accidents
Government investigations information requests or enforcement
actions
Private actions or claims corporate or employee
Deviations from corporate policies or government requirements by
management
Which have or could result in the following
Death serious injury or adverse health effects
Property damage exceeding $1000000
10
Government investigation or enforcement action which limits
operations or assesses penalties of $100000 or more
Publicity resulted or anticipated
Substantial media coverage
Report At The Beginning Of The Next Day
Event Criteria
Was reported to government agency as required by law
Worker employee or contractor recordable injury or illness associated
with release
Community impact-reported or awareness
Publicity resulted or anticipated
Release exceeding the reportable quantities listed in Section 1.5 for
each specific process material waste or by-product
In the event of spill of reportable quantity the Mill Manager is required to
call the Corporate Environmental Manager or the President and Chief
Executive Officer The individual first discovering the spill will report it to the
Shift Foreman Production Superintendent or Maintenance Superintendent
who will in turn ensure that the Mill Manager is notified The Environmental
Health and Safety Manager will also be contacted by the Mill Manager
Name Title Home Phone
Mill Personnel
Richard Bartlett Interim Mill Manager 435 678-2495
Wade Hancock Maintenance Foreman 435 678-2753
David Turk Environmental Health and
Safety Manager 435 678-7802
N/A Production Superintendent
N/A Maintenance Foreman
Scot Christensen Mill Shift Foreman 435 678-2015
Corporate Personnel
Ronald Hochstein President and Chief Operating Officer 604 377-1167
David Frydenlund Vice President and General Counsel 303 221-0098
In the event the next person in the chain-of-command cannot be reached
then proceed up the chain-of-command to the next level Table 1.0 shows the
organizational chart for the mill site
11
1110 RECORDS AND REPORTS
The following reports and records are to be maintained in Central Files by the
Environmental Health and Safety Manager for inspection and review for
minimum of three years
Record of site monitoring inspections
Daily Tailings Inspection Data
Weekly Tailings Inspection and Survey
Monthly Tailings Inspection Pipeline thickness
Quarterly Tailings Inspection
Tank to soil potential measurements
Annual bulk oil and fuel tank visual inspections
Tank and pipeline thickness tests
Quarterly and annual PCB transformer inspections if transformer
contains PCBs
Tank supports and foundation inspections
Spill Incident Reports
Latest revision of SPCC plan
1.11 PERSONNEL TRAINING AND SPILL PREVENTION
PROCEDURES
All new employees are instructed on spills at the time they are employed and
trained They are briefed on chemical and petroleum spill prevention and
control They are informed that leaks in piping valves and sudden
discharges from tanks should be reported immediately Abnormal flows from
ditches or impoundments are of immediate concern In addition safety
meeting is presented annually by the Environmental Health and Safety
Manager to review the SPCC plan
1.11.1 Training Records
Employee training records on chemical and petroleum spill prevention are
maintained in the general safety training files
1.11.2 Monitoring Reports
Shift logs shall provide checklist for inspection items
12
1.12 REVISION
This procedure is to be reviewed by the mill staff and registered
professional engineer at least onc eve ry th ree years and updated when
circumstances warrant revision
1.13 Summary
Below is table listing the specific reportable quantities associated with the
major chemical and petroleum products on-site
CHEMICAL REPORTABLE
QUANTITY RQ
AMMONIA 100 POUNDS
AMV 1000 POUNDS
SODIUM
HYDROXIDE
1000 POUNDS
SODA ASH No Reportable
Quantity
SODIUM
CHLORATE
400 GALLONS
SULFURIC ACID 1000 POUNDS
VANADIUM
PENTOXIDE
1000 POUNDS
KEROSENE 100 GALLONS
OIL No Reportable
Quantity
PROPANE No Reportable
Quantity
DIESEL
UNLEADED
FUEL
100 GALLONS
13
1.14 MILL MANAGER APPROVAL
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with the Standard Operating Procedures
currently in effect
Richard Bartlett
Interim Mill Manager
1.15 CERTIFICATION BY
REGISTERED PROFESSIONAL ENGINEER
hereby certify that have reviewed the foregoing chemical and petroleum
product SPCC plan that am familiar with the International Uranium USA
Corporation White Mesa Mill facilities and attest that this SPCC plan has
been prepared in accordance with good engineering practices
Harold Roberts
Registered Professional Engineer
State of Utah No 165838
14
TABLES
Table
White Mesa Mill Management Personnel
Responsible for Implementing This BMPP
Mill Staff
Personnel Title Work Phone Rome Phone
Other Contact Number
Rich Bartlett Interim Mill Manager 435-678-2221 435 678-2495
Ext 105
Wade Hancock Maintenance Foreman 435-678-2221 435 678-2753
Ext.166
Scot Christensen Mill Foreman 435-678-2221 435 678-2015
David Turk Radiation Safety Officer 435-678-2221 435 678-7802
Ext 113
Corporate Management Staff
Personnel Title Work Phone Rome Phone
Other Contact
Number
Ron Hochstein President Chief Operating 604 806-3589 Cell 604 377-1167
Officer
David Frydenlund Vice President and 303 389-4130 303 221-0098
General Counsel Cell 303 808-6648
TABLE 2.0
REAGENT TANK LIST
QUANTITY REAGENT cAPACITY GAL
DIESEL 250
KEROSENE 10152
USED/WASTE OIL 5000
DIESEL 6000
UNLEADED 3000
PROPANE 30000
AMMONIA 31409
SODIUM HYDROXIDE 19904
SODA ASH SOLUTION 16921
SODA ASH SHIFT 8530
SODIUM CHLORATE 17700
SODIUM CHLORATE 10500
SULFURIC ACID 1600000
SULFURIC ACID 269160
TABLE 3.0
LABORATORY CHEMICAL INVENTORY LIST1
SIw5K
Aluminum nitrate
Ammonium bifluoride
Ammonium chloride
Ammonium oxalate
Ammonium thiocyanate
Antimony potassium tartrate
n-Butyl acetate
Carbon tetrachloride
Cyclohexane
Ferric chloride
Ferrous ammonium sulfate
Potassium chromate
Sodium nitrite
Sodium phosphate tribasic
Zinc acetate
2270 kg
45.4 kg
2270 kg
2270 kg
2270 kg
45.4 kg
2270 kg
4.54 kg
454 kg
454 kg
454 kg
4.54 kg
45.4 kg
2270 kg
454 kg
1.8 kg
2.27 kg
2.27 kg
6.8 kg
7.8 kg
0.454 kg
1.0
24
6.810 kg
0.57 kg
0.114 kg
2.5 kg
1.4 kg
0.91 kg
hemioIuVthtiJescand -flQk Quahtitthtstocl
FihthMiSiVkŁWABfl V4
Chloroform 4.54 kg
Formaldehyde 45.4 kg IL of 37%solution
Nitrobenzene 454 kg 12
Toluene 454 kg 12
Q4Si
Chloroform 4.54 kg 55 gal
Hydrochloric acid 2270 kg 58 gal
Nitric acid 454 kg
Phosphoric acid 2270 kg 10
Sulfuric acid 454 kg 25
Hydrofluoric Acid 45.4 kg
Ammonium hydroxide 454 kg 18
This list identifies chemicals which are regulated as hazardous substances under the
Federal Water Pollution Control Act 40 CFR Part 117 The lab also stores small
quantities of other materials that are not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable
Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean
Water Act
TABLE 4.0
REAGENT YARDISMALL QUANTITY CHEMICALS LIST1
Ammonium Hydroxide 1000 lbs 5L
Carbon Disulfide 100 lbs lbs
Calcium Hypochlorite 10 lbs kg 4.4 Ibs
Chlorine 10 lbs Olbs
Ferrous Sulfate Heptahydrate 1000 lbs kg lIbs
Hydrochloric Acid 5000 lbs 60 gal of 40%
solution
Nitric Acid 1000 lbs 10
Potassium Permanganate 0.1 32 gal kg 11 Ibs
Sodium Hypochlorite 5.5%100 lbs kg 11 Ibs of
5.5%solution
Silver Nitrate lb lbs
Trichloroethylene 100 lb
Xylene Mixed Isomers 100 lbs lbs
This list identifies chemicals which are regulated as hazardous substances
under the Federal Water Pollution Control Act 40 CFR Pad 117 Materials
in this list are stored in locked storage compound near the bulk storage
tank area The Mill also stores small quantities of other materials that are
not hazardous substances per the above regulation
Reportable Quantities are those identified in 40 CFR Pad 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
Acetic Acid Glacial
TABLE 5.0
REAGENT YARD/BULK CHEMICALS LIST1
REAGENT.H
11
Q2 QUANTITYIN
REAGENflARO
Sulfuric Acid 1000 lbs 9000000 lbs
Floc 301 None 1200 lbs
Hyperfloc 102 None 1500 lbs
Ammonia East Tank 100 lbs lbs
Ammonia West Tank 100 lbs 105000 lbs
Kerosene 100 gal 500 gal
Salt Bags None 2000 lbs
Ammonium Hydrogendifluoride None 20450 lbs
Soda Ash Dense Bag None lbs
Phosphoric Acid 5000 lbs 6300 lbs
Polyox None 490 lbs
Millsperse None 1410 lbs
Nalco TX760 None barrels
Nalco 7200 None 1590 lbs
Tributyl phosphate None 9450 lbs
Distillates None 100 gal
Diesel 100 gal Approx 3300 gal
Gasoline 100 gal Approx 6000 gal
Alamine 336 drums None lbs
Floc 109 None lbs
Floc 208 None lbs
Floc 904 None lbs
Hyperfloc 624 None lbs
Salt Bulk solids None lbs
Salt Bulk solutions None lbs
Caustic Soda 1000 lbs lbs
Ammonium Sulfate None lbs
Sodium Chlorate None 20000 lbs
Alamine 335 Bulk None lbs
Alamine 310 Bulk None lbs
Isodecanol None lbs
Vanadium Pentoxide3 1000 lbs 30000 lbs
Yellowcake3 None 100000 lbs
Ammonia Meta Vanadate 1000 lbs lbs
This list identifies all chemicals in the reagent yard whether or not they are regulated as hazardous
substances under the Federal Water Pollution control Act 40 CFR Part 117
Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3 Reportable Quantities
of Hazardous substances Designated Pursuant to Section 311 of the Clean Water Act
Vanadium Pentoxide and Yellowcake the Mills products are not stored in the Reagent Yard itself
but are present in closed containers in the Mill Building and/or Mill Yard
TABLE 6.0
PETROLEUM PRODUCTS AND SOLVENTS LIST1
iPRODUCT QUANTJTY4NH
Lubricating Oils in 55 gallon drums
Transmission Oils
Water Soluble Oils
Xylene mixed isomers
Toluene
Varsol Solvent
2%trimethyl benzene in petroleum distillates
This list includes all solvents and petroleum-based products in the Mill
warehouse petroleum and chemical storage aisles
Reportable Quantities are those identified in 40 CFR Part 117 Table
117.3 Reportable Quantities of Hazardous Substances Designated
Pursuant to Section 311 of the Clean Water Act
100 gal
100 gal
100 gal
100 lbs
1000 lbs
100 gal
1540 gallons
gallons
30 gallons
gallons
gallons
gallons
FIGURES
Figure
White Mesa Mill
Mill Site Layout
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Figure
White Mesa Mill
Mill Site Drainage Basins
APPENDIX
WHITE MESA MTLL
EMERGENCY RESPONSE PLAN
EMERGENCY RESPONSE PLAN
REVISION 1.1
Denison Mines USA Corp
1t7t.-WiT.11
VV IIILC JVICSd IV1III
landing Utah
April 14 1986
REVISED
February 16 2007
Distribution List
Ron Hochstein
RichE Bartlett
David Turk
Michael Spillman
Mill Shift Foremen
Blanding Fire Department
San Juan County EMS Coordinator
State of Utah Department of Radiation Control
Revision Date January 16 2006
TABLE OF CONTENTS
Page
Number
1.0 Introduction .1
2.0 White Mesa Mill Background .1
3.0 Plan Objectives
4.0 Description of Facilities
4.1 Fire Water Supply and Alarm Systems
4.2 Office Building and Laboratory
4.3 Solvent Extraction Building
4.4 Mill Building
4.5 Maintenance Shop/Warehouse/Change Room Building
4.6 Reagent and Fuel Storage
4.7 Boiler House
4.8 Sample Plant
5.0 Organization and Responsibilities
5.1 Mill Manager/Encident Commander
5.2 Operations Superintendent
5.3 Radiation Safety Officer/Fire Chief
5.4 Maintenance Supervisor
5.5 Laboratory Supervisor
5.6 Shift Foremen
5.7 Scale House Personnel
5.8 Emergency Response Teams
6.0 Specific Emergencies 10
6.1 Fire 10
6.2 Chemical or Gas Release 10
6.3 Earthquake 10
6.4 Terrorist/Bomb Threat 10
6.5 Tailings Dam Break and Major Floods 10
7.0 Evacuation Procedure 11
7.1 Notification 11
7.2 Assembly 11
7.3 Specific Procedures for Operations Personnel 11
8.0 Off-Site Emergency Equipment/Personnel Release 11
9.0 Emergency Equipment 12
9.1 Fire Hose 12
9.2 Self Contained Breathing Apparatus 12
9.3 Spill Clean-up Equipment 12
9.4 Fire Fighting PPE 12
10.0 Emergency Transportation 13
11.0 Emergency Evacuation Drills 13
EXHIBITS
Emergency Notification List E-
Internal Notifications E-2
Site Layout Map E-3
Main Shut-off Valves E-4
APPENDICES
Emergency Procedure Response to Fire A-I
Emergency Procedure Response to Chemical or Gas Release A-2
Emergency Evacuation Procedure A-3
FIGURES
Fire System Schematic F-I
ii
INThRNATIONAL URANIUM USA CORPORATION
Rev No R-1
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
INTRODUCTION
This Emergency Response Plan is written not only to comply with Federal State and local
regulations but even more importantly to reduce the risk to our employees and that of the
community in regards to Health Safety and Environmental Emergencies
This plan includes the following
evaluation of the potential risks for fire explosions gas releases chemical spills and
floods including tailings dam failure
specific emergency programs for each potential event
definition of administrative response actions and
definition of the emergency response contacts both internal and external
The White Mesa Mill the Milloperates under the following regulatory agencies
Utah State Department of Environmental Quality Division of Radiation Control
Mine Safety and Health Administration
Environmental Protection Agency
Utah State Department of Environmental Quality Division of Air Quality and
Utah State Division of Natural Resources Bureau of Dam Safety
WHITE MESA MILL OVERVIEW
The Mill processes conventional uranium or uranium/vanadium ores to recover uranium and
vanadium In addition to the processing of conventional ores the Mill also processes alternate
feed materials using similar process steps and chemicals The conventional ore is stored on the
Ore Pad shown in Exhibit Alternate feed materials are also stored on the Ore Pad and may
be stored in bulk form lined burrito bags liners or drums The descriptions of each alternate
feed material are malntained by the Mills Radiation Safety Officer
The Mill utilizes semi-autogenous grind circuit followed by hot sulfuric acid leach and
solvent extraction process to extract uranium and vanadium from ores using large amounts of
sulfuric acid sodium chlorate kerosene amines ammonia and caustic soda in the process The
reagent storage tank locations are described in further detail in Section 4.6
Emissions from the Mill process are in the form of air emissions from exhaust stacks and
solid/liquid tailings which are stored in the Mills tailings cells located west/southwest of the
main Mill building The major exhaust stack parameters are shown in the following table
Description
Height
ft from surface
Diameter
inches
Estimated Flow Rate
cfln
Leach Exhaust l00 36 13700
Yellow Cake Drying
stacks
85 18 4000 per stack
Vanadium Roasting
Fusion
85 38 4100
P\Admin\Master SOPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc
1NTERNATIONAL URANIUM USA CORPORATION
Rev No.R-l
Date Sept 29 2005 WHITE MESA MILL EMERGENCY RESPONSE PLAN Page of 13
There are also smaller exhaust stacks associated with the Laboratory in the Mill Administration
building and the boiler exhaust stack
The Mills tailings cells are comprised of four below grade engineered cells Cell I-I and
4A Liquids are stored in Cell 1-I and Cell the active tailings cell The liquid in the tailings
cells is very acidic In addition to the tailings cells there is also an emergency lined catchment
basin west of the Mill building Solutions in this basin or the tailings cells should not be used to
fight fires in the Mill facility
The products of the Mill include ammonium metavanadate AMV vanadium pregnant liquor
VPL vanadium pentoxide V205 and yellowcake or uranium concentrate U3O8 The V2O5
and U3O8 products are packaged in steel drums for shipment The AM17 is packaged in either
steel drums or super-saks while the VPL is sold in liquid form in bulk
Master files containing Material Safety Data Sheets for all materials in use at the Mill are
maintained at the Safety Office Mill Maintenance Office Mill Laboratory and Mill Central
Control Room Copies are also on file at the Blanding Clinic Doctors Offices Blanding Fire
House and Office of the San Juan County Emergency Medical Coordinator
The nearest residence to the Mill is approximately one mile to the north of the Mill the next is
residence approximately two miles north of the Mill followed by the community of White Mesa
about 3.5 miles to the south The City of Blanding is located approximately miles to the
northeast
The Mill site is near Utah State Highway 191 and can be accessed by paved access road from
the highway to the Mill facilities
PLAN OBJECTIVES
The primary objectives of this plan are
To save lives prevent injuries prevent panic and minimize property/environmental
damage to the lowest possible level
To evacuate and account for all people in the area including visitors truck drivers
contractors etc
To provide assembly areas that are as safe as possible and which can be reached without
traveling through hazardous area Assembly areas will be properly manned to deal with
sick or injured persons and provisions will be made to evacuate those persons to proper
shelter
To make adequately trained personnel available to cope with rescue and recovery
operations as directed by the Incident Commander
DESCRIPTION OF FACILITIES
The Mill facilities are shown on the Site Layout Map included as Exhibit
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4.1 Fire Water Supply and Alarm Systems
4.1.1 Fire Water Supply
The fire water supply facilities include
400000 gallon Storage Tank of which 250000 gallons are reserved for fire emergencies
Centrifugal diesel driven pump rated at 2000 gpm at 100 psi This pump starts
automatically when the pressure in the fire main drops below 100 psi See Figure Fire
System Schematic
When more water is needed for an emergency an additional source is the Recapture Reservoir
supply pipeline which can be utilized in emergencies at rate of about 1200 gpm
4.1.2 Alarm System
The alarm systems include the following
public address system
hand held radios
siren
4.2 Office Building and Laboratory
4.2.1 Office Building
The office building approximately 10000 square feet contains the administration offices
radiation health and safety offices and the Mill laboratory The central file vault and the main
computer system are also in this building The ambulance is kept on the west side of the office
building near the safety office entrance
4.2.2 Laboratory
The laboratory facilities contain the following
three flammable cabinets keys required
chemical storage room south of main lab
six fume hoods hoods 12 and are in the center of the laboratory and hoods and
are along the west wall Hoods and are no longer in service Hoods and are on
the west side and are on the east side of the center cluster of hoods with being in
front Only hoods and may be used for perchloric acid
outside laboratory chemical storage north of office building key required
perchioric acid storage vault located underground west of office building key required
wide variety of chemicals in small quantities are located in the laboratory These chemicals
range from acids to bases along with flammable metal compounds and peroxide forming
compounds Oxidizers and organic chemicals which have strong potential of producing
harmful vapors if the containers are damaged to the point that the chemicals are exposed are
stored in storage room in the laboratory There are no acids stored in this storage room The
acids including but not limited to sulfuric nitric acetic perchloric phosphoric and hydrochloric
acids are stored in the main laboratory area in 2.5 liter or 500-mi bottles MSDS books for all
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chemicals in the laboratory are located in the Laboratory Safety Department Mill Maintenance
office and Mill Central Control room
4.2.3 Electrical
Electrical transformers and electrical switches are located in the laboratory at the east end of the
chemical storage room
4.2.4 Fire Protection System
The fire protection systems in the office building and laboratory include
fire hose station located on the east end of the office building The station includes two
sets of turnout gear two SCBA units and Incident Commander materials
automatic wet sprinlder system which is actuated at 212
portable dry chemical extinguishers strategically located throughout the building
4.3 Solvent Extraction Building
The solvent extraction SX building approximately 21000 square feet houses the uranium and
vanadium solvent extraction circuits and the ELUEX circuit The SX circuits may contain up to
200000 gallons kerosene 757000 liters which has flash point of 185
Associated equipment in the SX building includes temporary boiler located at the southwest
end of the SX building which maintains the temperature for the fire system
Chemicals which may be encountered in the SX building include
Kerosene
Caustic Soda
Anhydrous Ammonia
Sulfuric Acid
Salt Brine
Soda Ash
Ammonium Sulfate
Amines
Alcohol
Sodium Chlorate
Sodium Vanadate
Propane
The VPL product is stored in the SX building
4.3.1 Electrical
All electrical switches are located outside in the MCC room north of the SX building The main
control panel for all of the equipment is located in the Central Control Room in the main Mill
building
4.3.2 Fire Protection System
The SX building fire protection systems include
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wet AFFF foam sprinkler system with heat actuated sprinkler heads that release at
212F
portable dry chemical extinguishers strategically located throughout the building
For fire hydrant and hose cabinet locations in the SX building refer to the Fire System Schematic
included as Figure in this Plan
4.4 Mill Building
The mill building approximately 22000 square feet contains process equipment related to
grind leach counter current decantation precipitation drying and packaging of uranium and
vanadium products
Chemicals which may be encountered in the mill building include
Caustic Soda
Anhydrous Ammonia
Sulthric Acid
Soda Ash
Ammonium Sulfate
Sodium Chlorate
Sodium Vanadate
Propane
The finished products which are contained in the mill building include AMV V205 and U3O8 or
yellowcake
4.4.1 Electrical
The main electrical switch gear is located west of the SAG mill on the ground floor in the north
west comer of the mill building Circuit control panels are located in the SAG mill control room
the central control room the vanadium roaster control room and the AMV area
4.4.2 Fire Protection System
The main mill building fire protection systems include
portable dry chemical extinguishers strategically located throughout the building
water hoses throughout the building
For fire hydrant and hose cabinet locations in the Mill building refer to the Fire System
Schematic included as Figure of this Plan
4.5 Maintenance Shop/Warehouse/Change Room Building
This building approximately 20000 square feet contains the main maintenance shop area
located on the north end of the building the main warehouse located on the south end of the
building and the personnel change rooms and lunch/training room located on the extreme south
end of the building on the ground and second floors
Within the maintenance shop area are the following work area and specialty shops
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the main maintenance shop area contains welding and cutting equipment lathes presses
and drill presses
carpenter shop which contains various saws and planes Fiberglass work is also done
within this shop area and it is located at the northwest end of the maintenance shop area
an electrical shop which is located south of the carpenter shop
heavy equipment maintenance shop area is located at the north end of the maintenance
shop in the center of the building
rubber room for rubber lining of equipment is located east of the equipment shop area
the maintenance shop office instrument shop and tool room are located at the south end
of the maintenance shop area
The warehouse area contains primarily dry good storage for repair parts and consumables for the
operation of the Mill There is an electrical water heater for the change room which is located in
the warehouse area at the south end
Within the warehouse and maintenance shops there are some oils and chemicals stored in the
following locations
small quantities of flammable material such as starting fluid and spray paint are kept in
the warehouse
drums of new oil and anti-freeze are stored along the east wall of the equipment
maintenance area and on the east side of the warehouse on oil storage racks
used oil is stored in tank located northeast of the equipment shop The tank has
capacity of approximately 5800 gallons
in the main maintenance shop area and the rubber room there are flammable storage
cabinets and east of the warehouse there is trailer which is used to store flammable
items such as rubber cements paints and fiberglass resins
compressed gas cylinder storage both empty and flill is located outside east of the
maintenance shop
4.5.1 Electrical
The main electrical circuit breaker for the maintenance shop and warehouse building is located
on the east wall inside the Maintenance shop Auxiliary electrical panels for the change room
and warehouse are located in the southwest corner of the warehouse area
4.5.2 Fire Protection System
The fire protection system within the maintenance shop/warehouse/change room building
includes
wet automatic sprinkler system that releases at 212
portable dry chemical extinguishers strategically located throughout the maintenance
area warehouse area and the change room and lunch room
For fire hydrant and hose cabinet locations refer to the Fire System Schematic Figure
4.6 Reagent and Fuel Storage
The following lists the reagents and fuel stored at the Mill site
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sulfuric acid tank located northwest of the mill building which has capacity of
approximately 1.4 million gallons
storage tank for propane is located on the north edge of the mill site northwest of the
mill building It has storage capacity of 30000 gallons
four sodium chlorate tanks located east of SX building north of the office building and
east of the pulp storage tanks The two tanks east of the SX building are for sodium
chlorate storage and the other two tanks are for dilution of the sodium chlorate
two anhydrous ammonia tanks located east of the SX building with capacity of 31409
gallons each
three kerosene tanks located east of the SX building with capacity of 10152 gallons
each
one caustic soda tank north of the SX building with capacity of 19904 gallons
three soda ash tanks which are located east of the SX building One tank is the dry soda
ash tank with capacity of 70256 gallons Two of the tanks are soda ash dilution tanks
with capacities of 16921 gallons each
diesel fuel and gasoline are stored in two tanks located on the eastern side of the ore pad
The gasoline storage capacity is 3200 gallons while diesel storage capacity is 8000
gallons
Other reagents are stored in steel barrels or super sacs in reagent yard located east of the office
building Typical reagents which are stored in this yard include
polymers and flocculants
boiler feed water chemicals
methanol
tributyl phosphate
dirty soda ash and ammonium sulfate
SX amines and emulsion breakers
decyl alcohol
minimal amounts of acid in barrels
used oil in drums and overpacks
4.7 Boiler Facilities
The main building approximately 12400 square feet is located on the west side of the Mill site
and contains air compressors and water treatment facilities To the north of the main building is
building which houses propane-fired boiler The vanadium oxidation tank oxidation
thickener and pH adjustment tank are located south of the boiler house facilities
4.7.1 Electrical
The main electrical panel for the boiler house is located outside of the building on the south
wall
4.7.2 Fire Protection System
The fire protection system for the boiler facilities is comprised of strategically located portable
dry chemical extinguishers
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4.8 Sample Plant
The sample plant building approximately 8000 square feet is located on the ore pad east of the
maintenance shop/warehouse building The sampling plant equipment has been removed from
the building and it is currently used as storage area for maintenance
4.8.1 Electrical
The electrical panel for this building is located on the east wall upstairs
4.8.2 Fire Protection System
There are no extinguishers or sprinlder systems in the sample plant
ORGANIZATION AND RESPONSIBILITIES
The organizational chart for an emergency situation is illustrated in Figure
5.1 Mill Manager/Incident Commander
The Incident Commander has the responsibility for
preparing an Emergency Plan
communicating the Plan
directing activities during emergencies and
reporting to local State and Federal authorities
The Incident Commander will stop routine radio usage upon learning of an emergency and set up
the base station in safe location for directing activities Radio usage will be limited to the
emergency The Incident Commander has the responsibility to contact all outside services
The Incident Commander has the responsibility to account for all employees at the Mill using
the assistance of supervisors and/or any International Uranium USA Corporation IUSA
personnel The Incident Commander has the responsibility for the news media and reports
directly to the President of IUSA
5.2 Mill General Superintendent
The Mill General Superintendent has the responsibility of directing outside emergency personnel
and has the responsibility for plant security and will report directly to the Incident Commander
The Mill General Superintendent will act as Incident Commander in the absence of the Mill
Manager
5.3 Radiation Safety Officer/Fire Chief
The Radiation Safety Officer will direct rescue operations and provide the necessary emergency
medical personnel and facilities to cope with the emergency Adequately trained fire crews and
operable emergency equipment will be maintained at all times
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As Fire Chief the Radiation Safety Officer has the responsibility to maintain trained fire crews
and operable equipment mobilize and direct the fire crews and equipment in fire emergency or
one containing the threat of fire and to assist in evacuation and rescue or recovery operations
In the absence of the Radiation Safety Officer the Mill Safety Coordinator will assume these
duties
5.4 Maintenance Supervisor
The Maintenance Supervisor will direct all personnel in evacuation and in activities to cope with
the emergency including isolation of utilities and providing technical advice as needed The
Maintenance Supervisor will be assisted by the Mill Safety Coordinator
5.5 Laboratory Supervisor
The Laboratory Supervisor has the responsibility to direct and account for all office personnel
including IUSA personnel and office visitors in evacuation and in activities to cope with the
emergency In case of mill tour the Supervisor accompanying the tour will be responsible for
evacuation of visitors
5.6 Shift Foremen
Shift Foremen are in charge until the Incident Commander arrives and are responsible for all
functions listed above Shift Foremen have the responsibility to account for all of their people in
addition to any visitors contractors etc in their areas and report to the Incident Commander or
in the absence of the Incident Commander to administer all of the above duties
5.7 Scale House Personnel
Scale house person on shift will be responsible to account for ore truck drivers and reagent truck
drivers
5.8 Emergency Response Teams
The response crew for each operating shift will normally consist of the following operators under
the direction of the shift foreman This organization may be changed for individual shifts subject
to the approval of the Fire Chief
5.8.1 Operational Mode
Leach Operator
CCD Operator
Solvent Extraction Operator
Mill Trainee
5.8.2 Non-Operational Mode
Shift Foreman
Operations Personnel
Maintenance Personnel
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Figure
Emergency Response Organizational Structure
Incident Commander
Mill Manager
Director of Security
Operations Superintendent
Fire Chief
Radiation Safety Officer
Shift Foremen Emerpency Response Teams Lab Supervisor
Operational Mode Non-Operational Mode
Leach Operator CCD Operator Shift Foreman Operations Personnel
SX Operator Mill Trainee Maintenance Personnel
SPECIFIC EMERGENCIES
The following details procedures to be followed during specific emergencies but are not limited
to the following
6.1 Fire
Should fire occur the procedure outlined in Appendix for reporting and responding to fires
will be followed Particular areas of concern include
Solvent Extraction Building
Propane Tanks
Lab or Lab Storage Area
6.2 Chemical or Gas Release
The procedures for response to chemical or gas release are outlined as Appendix
6.3 Earthquake
Although this is highly unlikely an earthquake could occur at the Mill severe earthquake
could cause buildings and other structures to collapse chemical and/or gas releases major fires
as well as general panic In the event of major earthquake the evacuation procedures outlined
in Appendix will be followed
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6.4 Terrorist/Bomb Threat
In the event that any person should receive threat of bomb the following evacuation
procedure should be followed
Notify any person of authority i.e Superintendent Foreman Radiation Safety Officer
who will immediately notify law enforcement authorities and evacuate the threatened
area
Evacuate all persons from the affected area and stop all radio transmissions
6.5 Tailings Dam Break and Major Floods
Flood water breaching tailings embankments presents one of the greatest dangers for the sudden
release of tailings solids and impounded water The tailings cells are designed with sufficient
freeboard three feet to withstand back-to-back 100-year storm events or 40%of the probable
maximum flood PMF followed by the 100-year storm event The flood design is equivalent to
15 inches of rainfall In addition the tailings dikes were designed in accordance with U.S NRC
regulations and allow sufficient margin of safety even in the event of an earthquake
The possibility of floods resulting from Westwater Creek Cottonwood Creek and Corral Creek
causing dam failure is extremely remote
The tailings cells and dikes are inspected on both daily and shift basis
Discharges from dike failure would extend three miles before leaving IUSAs property In the
event of dam failure large operating equipment will be mobilized to construct temporary
earthen dikes or berms downgradient to the failed dike In addition the State of Utah
Department of Radiation Control Executive Secretary the Executive Secretary MSHA and
State of Utah Department of Natural Resources Division of Dam Safety shall be notified
In the event of seismic rupture of tailings slurry pipelines the released slurry will be contained
in the tailings cells regardless of the quantity released
EVACUATION PROCEDURE See Appendix
7.1 Notification
Employees will be notified to evacuate the area by dialing 184 on any area telephone and
announcing that the Mill should be evacuated This announcement will be repeated twice When
the paging system cycles through the evacuation siren continuous frequency will automatically
sound for approximately forty-five seconds and then automatically shut off allowing
communications by radio from that point If the 184 number is dialed accidentally the
evacuation alarm may be canceled by disconnecting the phone until the page cycle ends then re
dial 184 See Exhibits and
7.2 Assembly
When the evacuation alarm sounds or when personnel are verbally notified by radio or other
means all personnel will assemble at
The parking lot south of the office
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The scalehouse
North side of Tailings Cell or
North of the Mill
Assembly site will depend upon conditions i.e nature of the emergency wind conditions etc
The Fire Chief or Shift Foreman will specify the appropriate assembly site
7.3 Specific Procedure for Operations Personnel
See specific emergency shutdown procedure for Operations by area under the relevant
Operating Procedure for your area
All employees not mentioned under Operating Procedures are to immediately report to
the assembly area and congregate by crew so that all persons can be accounted for As
employees leave their work areas they must pass the word to evacuate to any persons
who may not be aware of the emergency
After the Mill has been detennined to be safe for re-entry employees will be verbally
notified to return to their work stations
OIl-Site Emergency Equipment/Personnel Release
Any emergency response equipment or personnel that enter the Restricted Area in response to an
incident will be scanned and decontaminated prior to leaving the site according to the procedures
included in PBL-9 End Dump Trailer Acceptance Handling and Release Any equipment will
be decontaminated according to the requirements found in Table of the Nuclear Regulatory
Commissions NRCs Policy and Guidance Directive FC-85-23 Guidelines for
Decontamination of Facilities and Equipment Prior to Release for Unrestricted Use or
Temiination of Licenses for Byproduct Source or Special Nuclear Material issued May 1987
Injured personnel should be evaluated for radiation contamination if there was potential for
contamination at the earliest convenience Should it be necessary contaminated articles will be
gathered by the radiological staff after medical treatment has been rendered If the personnel
cannot be decontaminated notify the clinic/hospital personnel in advance
EMERGENCY EQUIPMENT
Emergency equipment for the Mill is provided as follows
9.1 Fire Hose
Fire hose cabinets are located at the following sites with minimum of 300 feet of 2-1/2 hose
two spanner wrenches spray nozzles and one hydrant wrench
South of SX
West of CCD
North of Mill Building
East of pulp storage tanks
Northwest of Maintenance Shop
West of Warehouse
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East of office building
9.2 Self Contained Breathing Apparatus
Two Self-Contained Breathing Apparatus
are located at each of the following locations
Hose station east of office building
Hose Station South of SX
North End SX Outside Wall
North end of Mill building outside wall
9.3 Spill Clean-up Equipment
Barrels of soda ash are located throughout the Mill to be used in case of chemical spill Soda
ash is also stored in bulk if needed There are also few drums of absorbent stored near the
laboratory The laboratory also contains acid spill kits and absorbent materials to be used in case
of spill
9.4 Fire Fighting PPE
Two complete sets of turnout gear for fire fighting and/or emergency extrication are located in
the Fire Hose Station located on the east side of the office building
9.5 Maintenance of Emergency Equipment
Fire extinguishers are inspected on an annual basis as well as the fire pump system The Mill
Safety Coordinator performs regular spot checks on the emergency equipment locations to ensure
that all of the equipment is in place
10 EMERGENCY TRANSPORTATION
One fully-equipped First Responder Unit Ambulance located west of the office building
Other motor pool vehicles on the property will be utilized as needed in emergency situations with
support as needed from the local Emergency Medical Services
11 EMERGENCY DRILLS AND TRAINING
Quarterly drills as required by MSHA are prepared by the Safety and Radiation Departments to
monitor performance of personnel responding to emergency situations Each drill will be
enacted upon one or more of the potential scenarios by this plan The drill and evacuation
activities are documented by the Mills Safety Coordinator and maintained within plant files
Management will review all drills at quarterly ALARA Committee Meetings
P\Admin\Master SOPsBook 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc 13
EXHIBIT
EMERGENCY NOTIFICATION LIST
ATTEND TO ANY INJURED PERSONS AND NOTIFY THE SUPERVISOR
Give artificial respiration if necessary
Control bleeding
Treat for shock
Immobilize fractures and stabilize for transportation
Scan the injured for excessive alpha prior to transporting if time allows
If alpha is excessive or there is no time to scan notify the clinic/hospital personnel and the
Radiation Safety Office
THE SUPERVISOR OR HIS DESIGNEE WILL NOTIFY THE FOLLOWING AS NEEDED
Blanding Clinic 678-2254 or 678-3434 930 400
San Juan Hospital Monticello ...678-2830 or 587-2116 364 1st
EMT and CPR TRAINED The following personnel should be contacted if they are on-site in the
event of an emergency to aid in the event of any injuries to personnel
David Turk EMT and CPR trained
Mike Spillman CPR trained
AMBULANCE SERVICE
Blanding Dial 911
If the Company Ambulance is used an attendant must ride with the injured in addition to the driver
except where the injured could normally be transported in car or pickup
OTHER EMERGENCY NUMBERS
Fire Department Dial 911 or 678-2313
County Sheriff Dial 911 or 587-2237
Highway Patrol Dial 911 or 587-2000
Blanding Police Dial 911 678-2916 or 678-2334
MANAGERS
The Supervisor will notify one of the following of all incidents
R.E Bartlett 435-678-2495
Turk 435-678-7802 or 435-459-1068
Spillman 435-678-2761
MEMBER OF MANAGEMENT WILL NOTIFY THE PROPER REGULATING AGENCIES
AS REQUIRED FOR EACH INCIDENT
State of Utah Department of Radiation Control 801-536-4250
MSHA Field Off.--801-524-3450 Dist Off 303-231-5465
MSHA Arlington 800-746-1553
State Emergency Response Comm 801-538-3400
State of Utah Natural Resources Dam Safety 801-538-7200
National Response Center 800-424-8802
Utah Poison Control Center 800-456-7707
Notification of surrounding communities and or residences will be handled by the appropriate agencies as
required by EPCRA Emergency Planning and Community Right to Know Act
Revision Date Januaiy 16 2006 Ed
EXHIBIT
INTERNAL NOTIFICATIONS
Internal reporting requirements for Incidents Spills and Significant Events are as follows
Report Immediately
Event Criteria
Release of toxic or hazardous substances
Fire explosions or other accidents
Government investigations information requests or enforcement actions
Private actions or claims corporations or employees
Deviations from Corporate policies or government requirements by Management
Other significant events which have resulted or could result in
Death serious injury or adverse health effect employees or public
Property damage exceeding $1000000
Government investigation or enforcement action limiting operation or penalties
of $100000 or more
Significant criminal actions
Substantial media coverage
Unscheduled down time of more than 24 hours
Report at the Beginning of the Next Business Day
Incident Criteria
Was reported to government agency as required by law
Worker IIJSA or contractor recordable injury or illness associated with release
Community impact reported or awareness
Publicity resulted or is anticipated
Release of process material waste or product in excess of the Reportable
Quantities listed in Section 1.5 of the Spill Prevention Control and
Countermeasures Plan
The local manager in charge is to call Ron Hochstein or Dave Frydenlund
Name Title Office Phone Home Phone
Ron Hochstein President and COO 303-628-7798 office
604-931-6334 home
604-377-1167 cell
David Frydenlund V.P and General Counsel 303-389-4130 office
303-221-0098 home
303-808-6648 cell
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EXHIBIT
SITE LAYOUT MAP
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EXHIBIT
MAIN SHUT-OFF VALVES
During an emergency this list should be used along with Site Layout Map Exhibit to locate
tanks and valves associated with these tanks
REAGENT SHUT-OFF VALVE LOCATIONS
Sulfuric Acid
Main located south side of acid tank
East acid pump discharge valve
West acid pump discharge valve
Main leach area located 25 feet west of Derrick screens next to walkway
1/2 Main SX area located south of Central Control room
Ammonia
Main east tank located on end at bottom
Main west tank located on end at bottom
Valve located on top of tank east tank
Valve located on top of tank west tank
Kerosene
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Pump discharge valve
Soda Ash
Main valve located at bottom of tank dry storage
Main valve located at bottom of tank on 30%dilution tank
Main valve locate at bottom of tank on dilution tank
Salt
Main valve located at bottom of tank
Caustic Soda
Main valve located at bottom of tank east and west between supports
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EXHIBIT
MAIN SHUT-OFF VALVES
Sodium Chlorate
Main valve located at bottom of tank east tank
Main valve located at bottom of tank north tank
Main valve located at bottom of tank south tank
Propane
Main located 15 feet east of tank
Main located on pipe off top of tank
Main located at bottom of tank also fill pipe
PLANT UTILITY SHUT-OFF VALVE LOCATIONS
Process Water
Main valve located on west side of water storage tank
Discharge valve off service water pump east
Discharge valve off service water pump west
Mill process water main located east wall by SAG mill
Fire Water
Main valve located west side of water storage tank
Emergency fire pump discharge valve to fire system
Emergency fire pump discharge valve to header west side of pump house
Main valve located south of Central Control room for SX and boilers
Potable Water
Main suction from potable water storage tank
Main discharge from potable water storage tank
Main located at east wall by SAG mill
Main located south of Central Control room for SX Maintenance shop and offices
Steam
Main discharge valve for Superior boiler located at top of boiler
Main steam valve located south side of boiler house
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EXHIBIT
MAIN SHUT-OFF VALVES
Plant Air
Main valve located at receiver tank in compressor room at boiler house
Main valve to mill building located south of Central Control room
PROCESS SHUT-OFF VALVE LOCATIONS
Pulp Storage
No valve located on west side of tank
No valve located on west side of tank
Preleach old No pulp storage valve located on west side of tank
Preleach Thickener
Main valve located underneath at center cone
Clarifier
Main valve located underneath at center cone
Main valve located underneath at center cone
CCD Thickeners
Main valve located underneath at center cone of each thickener
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APPENDIX
EMERGENCY PROCEDURE RESPONSE TO FIRE
The fire will be reported by dialing 185 on any telephone in the area and announcing the
location of the fire over the paging system This announcement will be repeated twice
for total of three announcements When the paging system cycles through the fire siren
alternating frequency will automatically sound for approximately forty-five seconds
then automatically shut off allowing radio communications to resume
Mobilize the fire crew
Evacuate all personnel
Rescue any victims of the fire do this only with properly trained and equipped personnel
Isolate utility lines affected by the fire
Extinguish the fire and post fire watch for flare-ups
Report the fire to proper local State Corporate and Federal agencies
In cases where the fire is not extinguished within thirty minutes of discovery the area
must be barricaded off after extinguishing and left undisturbed until released by MSHA
and IUSA management
Emergency off-site centers Blanding Fire House and Sheriffs office
Blanding Fire
350 West 200 South Blanding
Phone number is 911
Sheriffs Office
50 West 100 South Blanding
Phone number is 911 or 435 587-2237
P\Admin\Master SOPs\Book 16_Emergency Response PIan\Emergency Response Plan Rev 09.29.05.doc A-I
FIGURE
FIRE SYSTEM SCHEMATIC DRAWING
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APPENDIX
EMERGENCY PROCEDURE
RESPONSE TO CHEMICAL OR GAS RELEASE
chemical or gas release would most likely occur very suddenly The person who would first
witness chemical or gas release should immediately contact his supervisor who would initiate
the procedures outlined below
Activate evacuation alarm by using the dial 184 notification system Evacuate and
account for all personnel
Mobilize trained personnel and emergency equipment such as SCBAs first aid
equipment etc
Initiate rescue operations for any people who may be trapped by the release
Provide first aid and emergency medical care for any ill or injured persons
Initiate necessary steps to contain and/or neutralize the release such as spraying with
water fog turning off valves etc
Guard against possible fires by shutting off electrical circuits isolating gas lines and
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P\Admin\Master 5OPs\Book 16_Emergency Response Plan\Emergency Response Plan Rev 09.29.05.doc A-I
APPENDIX
EMERGENCY EVACUATION PROCEDURE
Activate evacuation alarm by using the dial 184 notification system Evacuate and account
for all personnel
Personnel are to assemble in one of the following areas
The parking lot south of the office building
The scalehouse
The north side of Tailings Cell or
North of the Mill
Mobilize trained personnel and emergency equipment such as SCBAs first aid equipment
etc
Initiate rescue operations for any people who may be trapped
Provide first aid and emergency medical care for any ill or injured persons
Guard against possible fires by shutting off electrical circuits isolating gas lines and
eliminating ignition sources from the affected area
P\Admin\Master 5OPs\Book 16_Emergency Response Plan\.Emergency Response Plan Rev 09.29.05doc A-i