DWQ-2025-002919

,l
Brosor,ros FAcrLrrY rxspncrroN
GENERAL INFORMATION
p4. March 13,2025
Time In_ Time Out
Facilify pu*" Tremonton \ A|/TP
E-mail
Reason for Inspection: I Routine lComplaint
Type of Facility
Approved Pretreatment Program
POTWFIow> I MGD
! Domestic Wastewater Treatment Works > 2000
GPD
Ll other
! Reuse Effluent (other than at facility)
Method of Solids Disposal
I Land Application (beneficial use)
I euk Ag Land o/o
ffi Compost t@ %n other %
Mailing Address 1 O2 Sorrfh Tremonton Sfreet
Tremonton, Utah 84337
4. Are records available for all use or disposal practices?
5. Are the number and location of sludge disposal sites available? (i.e., location maps)
6. Are self-monitoring data available for all regulated pollutants?
7. Are Pathogen and Vector Attraction Reduction method descriptions and certification statements
available?
8. Are accurate records of sludge volume or mass maintained, where appropriate?
9. Are self-monitoring activities conducted at required frequencies? (See Figure-1)
contu.t/ritl" P?ul Fulgh?ffi, Publ
prron" (45) 251-2ffi4 fl Surface Disposal
Discharge Permit #uT0020303
n Landfill
! Transferred to Another Facility
Other
Biosolids permit + UTL020303
Dan Griffin/State
PERMIT VERIFICATION
EvnNnN/A l. Are 40 CFR Part 503 sludge use and disposal requirements contained in:
ENPoes Permit?
[NfOeS Sludge Only Permir?
nBPa REGIoN 8 General Permit?
EePe Region 8 Individual Permit?
InCne Subtitle C permit?
Ellbctive date(s) of applicable permit o6t01t2024 09t30t2028
2 Annual Sludge Production 831 DMT (mtlyr,T/yr) last calendar year | 2024 l
tr V n N n N/A 3. Are number and location of disposal sites/activities described in permit or approved management plan?
RECORDKEEPING AND REPORTING EVALUATION :
frv nN n N/A
t"nN nN/A
6vAN I N/A
dvZN ! N/A
AtlN ! N/A
AtlN n N/A
Page 1 of11
Minimum Frequency of Monitoring (40 CFR Part 503.16, 503.26. and 503.46)
Amount of Biosolids Disposed Per Year Monitoring Frequency
Dry US Tons Dry Metric Tons Per Year or Batch
>0to<320 >0to<290 Once Per Year or Batch
>320to < 1650 > 290 to < 1,500 Once a Quarter or Four Times
> 1,650 to < 16,500 > 1,500 to < 15,000 Bi-Monthly or Six Times
> 16,500 > 15,000 Monthly or Twelve Times
FIGURE - 1 FREQUENCY OF BIOSOLIDS SAMPLE COLLECTION AND ANALYSIS
RECORDKEEPING AND REPORTING EVALUATION CONTINUED
I V n N n N/A 11. Are sludge data reported to the appropriate regulatory authority?
If so,how often? Annualy
SLUDGE SAMPLING AND ANALYSIS EVALUATION
fraN EN/A
F"ZN E N/A
Et ZN ! N/A
Sample collection procedures :
Ft aN n N/A
C"lN !N/A
/"lN EN/A
FrON E N/A
15. Are results reported on a dry weight basis? If no, how?
16. Were percent total solids analyzed?
17. Are chain-of-custody procedures properly employed?
18. Are chain-of-custody records available on site?
sludge records maintained for at least 5 years?
by facility ! Maintained by Contractor E other
ofeach pollutant
for both Pathogen and Vector Attraction Reduction
of how Class A/B requirements are met
of how Vector Attraction Reduction requirements are met
Description of site restrictions (if applicable)
Site locations, area, date, time and amount of sludge applied (if applicable)
72. Are sludge sampling locations appropriate for obtaining a representative sample?
13. Is sampling equipment adequate?
volumes obtained?
techniques used?
Types of Containers Used?
Samples analyzed in the appropriate time frames?
uate number of samples to obtain a representative sample?
ing and Analysis Plan Available?
GENERAL SLUDGE PROCESSES
Desoibe the sludge process control at the facility
t, ZN ! N/A 20. Does the facility have sludge back-up units/equipment? Describe
Page 2 of11
,F* AN n N/A 21. Does facility have capacity (>30 days)?5T-
dt nN ! N/A 22. Are plans for sludge disposal? Describe
t" ZN n N/A 23. Is the solids handling operation adequate to manage volume of sludge? Explain
LAND APPLICATION OF BIOSOLIDS
1. Biosolids Beneficial Use practice(s)Ta Bulk biosolids
Bulk material derived from biosolids
Sold or given away in bag or other container
Other
2. Biosolids or material derived from biosolids land applied to
I Agricultural Land
Reclamation Site
Lawn or Home Garden
Forest
Public Contact Site (park, golf course, etc.)
Other
tr V n N n N/A 3. Are pollutant concentrations below ceiling concentration values shown in Figure 2 Below (Table I)?
EX V E N n Nle 4. Do monitoring results show pollutant concentrations below limits in Figure 2 Below (Table III)?
FIGURE 2. POLLUTANT LOADING LIMITS
PATHOGEN CRITERIA
5. Classification of Biosolids with respect to Pathogens:
IClassA !ClassB !Unknown
EvXNf]N/A 6. Are the appropriate Class A or Class B Pathogen Reduction requirements being met for the disposal
practice?
Class A requirements must be met when bulk biosolids are sold or given away to the public for lawn or home garden use or
when bagged or containerized (one metric ton or less) biosolids are sold or given away. Also, Class A requirements or Class B
Page3ofll
Pollutant Limits, (40 CFR Part 503.13 ) Dry Mass Basis
Heaw Metals Table I Table2 Table 3 Table 4
Ceiling Concentration
Limits. (me/ke)
Cumulative Pollutant
Loading Rates, (mg/ha)
Pollutant Concentration
Limits, (ms/ke)
Annual Pollutant Loading
Rates, (me/ha-yr)
Total Arsenic 75 4l(37lbslac)4t 2.0
Total Cadmium 85 39(35 lbs/ac)39 1.9
Total Copner 4,300 1,500(1,335 lbs/ac)1 500 7.5
Total Lead 840 300(268 lbs/ac)300 l5
Total Mercury 57 17(15 lbs/ac)17 0.85
Total Molybdenum 75
Total Nickel 420 420(375lbs/ac)420 21
Total Selenium 100 100(89 lbs/ac)100 5.0
Total Zinc 7,500 2,800(2,500 lbs/ac)2800 140
requirements with appropriate site restrictions must be met when bulk or bulk derived material from biosolids is applied to
agricultural land, reclamation sites, forests or other public contact sites.
7. Indicate which method is used to meet Class A or Class B requirements:
Class A Class B
n e-t Time and Temperature
A-2 Alkaline Treatment
A-3 Prior Testing (EV & VHO)
A-4 No PriorTesting (EV &VHO)
A-5 PFRP
4'-6 Equivalent PFRP
CLASS A RECORDKEEPING CHECKLIST (SKIP IF CLASS B)
Alternative A-l Time and Temnerature I Nre
! Fecal Coliform (MPN)Analytical results are for densify ot ! Salmonella sp. Bacteria (#/4 g) OR
Z.zN Drly" %
nnntrT
B-l Fecal Coliform < 2,000,000 MPN or CFU
B-2 PSRP
B-3 Equivalent PSRP
Sludge percent Solids
Sludge temperature _oc OF
Time temperature maintained _ Days Hours Minutes
Alternative A-2 Alkaline Treatment ElNra
! Fecal Coliform (MPN)Analytical results are for density of: I Salmonella sp. Bacteria (#/4 g) OR
Sludge pH (logs of pH from beginning, middle and end of treatment) >12 S.U.
Time pH maintained > 12 (minimum 72 hours) Hours
Logs of sludge temps from beginning, middle, end and hourly - Minimum 12 hours > 52"C (125.6 "F)
Percent solids in sludge after drying _ t 5O%
Alternative A-3 Prior Testine E Nla
Analytical results are for density of: ! Salmonella sp. Bacteria (#/4 g) OR ! Fecal Coliform (MPN)
n Analytical Results (prior to pathogen reduction and, when appropriate, after treatment):X Density of Enteric Viruses (l plaque forming unit per 4 giams of total solids)
! Viable Helminth Ova (1 per 4 grams oftotal solids)
! Oetalled Sampling and Analysis Plan Available
tr Values or range ofvalues for operating parameters to indicate consistent pathogen reduction treatment
Alternative A-4 No Prior Testins El NIA
Analytical results are for density of: ! Salmonella sp. Bacteria (#/4 g) OR ! Fecal Coliform (MPN)
Analytical Results (prior to pathogen reduction and, when appropriate, after treatment):T Density of Enteric Viruses (1 plaque forming unit per 4 grams of total solids)
Viable Helminth Ova (l per 4 grams of total solids)
Detailed Sampling and Analysis Plan Available
Alternative A-5 Process to Further Reduce Pathosens (PFRP)n Nla
Heat Drying EN/A
Analytical results are for density of ! Salmonella sp. Bacteria (#/4 g) OR ! Fecal Coliform (MPN)
n Moisture content of dried sludge _ < l0%
tr Logs documenting temp of sludge particles or the wet bulb temp of gas in contact is > 80 "C (176 "F)
(continuous reading or once per shift, minimum 2 readings per day)
Page 4 of11
Thermophilic Aerobic Digestion E Nle
Analytical results are for density of, f] Salmonella sp. Bacteria (#/4 g) OR ! Fecal Coliform (MPN)
n
Dissolved oxygen concentration in digester
Temperature logs 55 oC <:> 60 "C (l3l oF <:> 140 "F)
Mean Cell Residence Time (MCRT) l0 days running average _ days (see equations below)
For complete mixed, constant feed & withdrawal with decanting:^ VCvHn=-qcq
V : reactor volume q: flow rate leaving Cv: concentration ofsolids in reactor
Cq : concentration of solids in existing sewage sludge 0n: MCRT (running average solids residence time)
For batch withdrawal, daily step feeding and decanting: 0n = t:::]:)
" E(6s)or ^ E(Vi*Ci*Ti)un=-X(Vi*Ci)
6s : an increment of sludge solids that leaves the reactor 0 : time period this increment has been in the reactor
Vi : volume of daily batch feed (incremental) to digester Ci : average concentration of solids in daily feed stream
Composting ! Nl,q,
Analytical results are for densify of: ! Salmonella sp. Bacteria (#/4 g) OR I Fecal Coliform (MPN)
Composting method: I Windrow I Static Aerated Pile ! Within -vessel ! Othe,
! Temperature logs: > 55 "C (l3l 'F) for 3 days if within-vessel or static aerated pile method
(continuous reading or one reading per shift, minimum 2 readings per day)
I Temperature logs: > 55 "C (131 "F) for 15 days if windrow method
(one reading per shift, minimum 2 readings per day)
I Records of pile turnings - minimum of 5 if windrow method
Gamma Ray lrradiation E NIA
Analytical results are for density of: ! Salmonella sp. Bacteria (#/4 g) OR ! Fecal Coliform (MPN)
! Gamma ray isotope used (e.g., Cobalt 60 or Cesium 137)
! Ambient room temperature log (continuous reading or one reading per shift, minimum 2 readings per day)
Alternative A-6 PFRP Equivalent E Uln
Analytical results are for density of: ! Salmonella sp. Bacteria OR I Fecal Coliform (MPN)
! Operating parameters or pathogen levels as necessary to demonstrate equivalent PFRP
(must have written approval from EPA Region 8 and the Pathogen Equivalency Committee (PEC)
Records
Documenting Sampling and Analysis for Salmonella sp. Bacteria or Fecal Coliform and Percent Solids
Sampling Records
and times of samples collected
Sampling locations documented
types listed
Sample fypes appropriate
le volumes recorded
ames of persons sampling recorded
of sample containers listed
le containers appropriate
of preservation including cooling
Sampling quality assurance/quality control (QA/QC) available
Page 5 of11
Analytical Records
and time of sample analysis
Name of analyst
cal methods used
Analyses and calculation results properly documented or verifiable
All analyses are reported on a dry weight basis
Name of Contract Laboratory, if applicable:Cl.-- *{-'e.E tr-n L
/Analytical quality assurance/quality control (QA/QC) available
fr Analy tical results avai lable
CLASS B RECORDKEEPING CHECKLIST (SKIP IF CLASS A)
Alternative B-1 Fecal Coliform Count
! Analytical results for density of fecal coliform collected for each sample
! Number of samples collected over two-week period (7 minimum)
fl Nte
! Geometric Mean Calculation < 2,000,000 MPN or CFU (Standard Methods 92218 or 9222D)
Root of the product of n factor - G.M. : (Xr * X, * X, * Xo *...Xn) '/n
Common Log Factor - G.M. : Antilog [(Log1sX1 + Logr6X2 + Log16X3 ... + LoglsXn)/n]
X : Fecal Coliform Density (dry weight basis) n : number of samples
Required Site Restrictions.
n public Access ! Harvesting ! Grazing
Alternative B-2 Process to Sienificantlv Reduce Pathoeens (PSRP) E Nle
Aerobic Digestion nUle
! Dissolved oxygen concentration profile n total Solids obtained and the feed and withdrawal streams
I Mean Cell Residence Time (MCRT) calculations of sludge in digester (see equations below)
For complete mixed, constant feed & withdrawal with decanting: 0n =Ynrn
V : reactor volume q : flow rate leaving Cv : concentration of solids in reactor
Cq : concentration of solids in existing sewage sludge 0n: MCRT (running average solids residence time)
For batch withdrawal, daily step feeding and decanting: 0n : t:::t) or en = t!uj:rt:I')
E(6s) X(Vi*Ci)
6s : an increment of sludge solids that leaves the reactor 0 : time period this increment has been in the reactor
Vi : volume of daily batch feed (incremental) to digester Ci : average concentration of solids in daily feed stream
! Temperature logs - 60 days @ 15 "C (59 "F) to 40 days @ 20 "C (68 "F)
(continuous reading or once per shift, minimum 2 readings per day)
Required Site Restrictions
fl pubtic Access ! Harvesting
Page 6 of11
! Grazing
Y
Description of drying bed design (sand drying beds, paved, unpaved beds
Depth of sludge on drying beds _ (in, ft)
! Orying time in days _ > 3 months
! laity average ambient temperature logs (2 of 3 months, ambient daily
Required Site Restrictions
! pubtic Access ll Harvesting
Anaerobic Digestion nNa
Total Solids obtained and the feed and withdrawal streams
Mean Cell Residence Time (MCRT) calculations of sludge
i
Air Drying
For complete mixed, constant feed & withdrawal with
V : reactor volume q : flow rate leaving Cv
Cq: concentration of solids in existing sewage sludge
For batch withdrawal, daily step feeding and
6s: an increment of sludge solids that leaves the
Vi : volume of daily batch feed (incremental) to
Temperature logs: > 40 "C (104
Demonstration that for 4
Required Site Restrictions.! ruutic Access
Lime Stabilization
! Raised pH > 12 after hours ofcontact
!Na
> 0 "c (32 "F)
Grazing
(see equations below)
gn -YYqcq
ofsolids in reactor
0n: MCRT (running average solids residence time)
^ X(6s*0)un=-E(6s)
^ X(Vi*Ci*Ti)un=->(vi*Ci)
I Temperature logs - 25 days @ 35 "C (95"F)55 "C (l3l"F) and 60 days @ 20 "C (68"F)
(continuous reading or once per 2 readings per day)
Required Site Restrictions.
! puutic Access I Harvesting ! Grazing
Composting
Composting method: n
E Nle
Liquid Sludge
! Quantify of
! single grab, pH
! Temperature of
pH correction temperature other than 2SqC =
or
0 : time period this increment has been in the reactor
Ci: average concentration ofsolids in daily feed stream
E static Aerated Pile n wittrin -vessel E other
for 5 days (continuous reading or one reading per shift, minimum 2 readings per day)
hours during the 5 days the temperature exceeded 55 'C (131"F)
! Harvesting ! Grazing
nNle
(-0.03 pH Units* (25qC-TmeasuredaC))
1.0"c
Dewatered Sludge (Cake)
0 hr._S.U.@2hr._S.U trn Quantity of Sludge and Alkali
5 min. composite, pH at 0 hr. S.U.@2 hr._S.U
and Alkali
ocloF (temp correction) f, Temperature of sample oCfF (temp correction)
pH new: pH measured - pH correction
Page 7 of11
Alternative B-3 PSRP Equivalent
! Operating parameters or pathogen levels as necessary to demonstrate equivalency to PSRP
I Operating parameters or pathogen levels as necessary to demonstrate equivalent PFRP
(must have written approval from EPA Region 8 and the Pathogen Equivalency Committee (PEC)
Required Site Restrictions (see Figure 2 on back of this page)
E Public Access ! Harvesting
Records
Documenting Sampling and Analysis for Fecal Coliform and
Sampling Records
! Dates and times of samples
Sampling locations
Sample types listed
Sample types
Sample vo recorded
n Names sampling recordedtrn
! Grazing
Solids
Analytical Records
Date and time of sample analysis
Name of analyst
Analytical methods used
Analyses and calculation results properly documented or verifiable
All analyses are reported on a dry weight basis
Analytical results available
Analytical QA/QC available
nnnnnnnsample containers listed
containers appropriate
of preservation including cooling
Sampling QA/QC available
Name of Contract Laboratory, if applicable:
VECTOR ATTRACTION REDUCTION METHODS
tr V E N n N/A 8. Is a Vector Attraction Reduction method practiced?
One of the VAR methods 1-10 must be used when land applying bulk biosolids to agricultural land, forest, a public contact site
or a reclamation site. One of the methods 1-8 must be used when distributing bulk, bagged or containerized biosolids for
public or lawn or home garden use.
9. Indicate Vector Attraction Reduction Method used
Z t - zsN Volatile Solids Reduction
2 - Anaerobic Bench Scale Volatile Solids Reduction
3 - Aerobic Bench-Scale Volatile Solids Reduction
4 - Specific Oxygen Uptake Rate (SOUR)
5 - Aerobic Process
6 - Alkaline Stabilization
7 - Moisture Reduction without Unstabilized Primary Solids
8 - Moisture Reduction with Unstabilized Primary Solids
9 -Subsurface Inj ection
I tO - Soil Incorporation
VECTOR ATTRACTION REDUCTION RECORDKEEPING CHECKLIST
Ontion I - Volatile Solids Reduction (VSR)ENre
n Log data showing VS concentration of raw and withdrawal sludge stream.
Composite sample
Test Method (SM 2540G) for Total Solids and Total Volatile Solids
Holding time and preservation followed (24hrs 4 "C for TVS)
Calculation showing > 380% reduction of volatile solids using the Van Kleeck Equation (see below)
ZSR = Vsin-vsout
VSin-(VSin*VSout)
Page 8 of11
VS;n = Fractional VS in feed stream
VSout : Fraction of VS from bottom stream
Fractional VS : Fraction of VS vs. Total Solids
Ontion 2 - Anaerobic Bench-Scale Volatile Solids Reduction E Nre
E tS-tOO ml flasks flushed with N2 ! Collect 50 ml in each 100 ml flask
I Temperature logs (at least two per day) showing temperature between 30 oC - 37 "C (86 "F - 98.6 "F)E t-og showing results of random test of 5 flasks for TS &TVS at0,20,& 40 days
! Test method (SM 2540G) for TS & TVS
! Calculation showing < 17 o/o reduction of volatile solids using the Van Kleeck Equation (see below)
ySR = vsin-vsout
VStn-(V Sin*v Sout)
VS;n: Fractional VS in feed stream
VSout : Fraction of VS from bottom stream
Fractional VS : Fraction of VS vs. Total Solids
Ontion 3 - Aerobic Bench-Scale VS Reduction
! Description of bench-scale digester
ENre
! Description of bench-scale digester _
!trnunnn
Collection of 12L of sludge (maintain by adding distilled water daily) @2o/oIf dilution was required, what was used
Log showing D.O. at least 2 mg/l
effluent)\
Calibration records for D. O. meter
Temperature logs (at least two per day) showing temperature maintained at20'C (68 'F)
Log showing results of TS & TVS (2 sets every week for 5 weeks)
Test method (SM 2540G) for TS & TVS
Calculation showing < 15 V, reduction of volatile solids using the Van Kleeck Equation (see below)
VSR = VSin-VSout
V Sin-(VSin+V Sout)
VS;n: Fractional VS in feed stream
VSout : Fraction of VS from bottom stream
Fractional VS : Fraction of VS vs. Total Solids
Option 4 -Snecific Oxvsen Uptake Rate (SOUR)E Nla
Collection of representative sample ml, L, gal.)
Times when samples were collected & tests performed (l hour holding)
E O.O.readings for sludge samples for l5 minutes or less (0,1,2,3...15 min) n l.O.calibration records
! temp readings at beginning and end of procedures ! temp correction performed if not at 20'C (68 "F)
E log showing results of TS for sludge sample (g/l) ! Test method (SM 2540G) for TS & TVS
! Calculations showing SOUR < 1.5 mg O2lfulgTS (2 sub samples) n errg. of 7 or more calculations
! Test Method SM 2710B (Apparatus, Procedure and Calculation), modified by White House Manual (pg. 95)
Option 5 - Aerobic Process n Nre
I Documentation showing aerobic process time 15 > 14 days
I Temperature log (continuous or at least two per day) showing average temperature > 45 oC (l l3 "F) and
minimum temperature > 40 "C (104 "F) for 14 consecutive days
Page 9 of11
Ontion 6 - Alkaline Treatment A
Log demonstrating pH > 12 S.U. for 2 hours in every batch
Log showing pH remains > I 1.5 for 22 hours without additional alkali demonstration of adequate mixing)n Test intervals at 0,2,24 hours
Amount of sludge treated (gal., lbs) n e alkali added_(lbs., gal.)
Liquid mixture - grab sample, pH testing in each batch E Cate minute composite, several pH tests per day
Option 7 -Moisture Reduction without Unstabilized Primarv Solids E Nla
fl Description of method used to air dry the sludge
! Results of percent solids (dry weight)test > 75%a Test Method SM 2540G for TS
E Nle
! Description of method used to air dry the
! Results of percent solids (dry test > 90%n Test Method SM 2540G for TS
Option 9 - Subsurface Iniection E Nre
nu
! Documentation of compl
and injection, no significant
ZZ
! ttClass A - must be inj within 8 hours ofdischarge from pathogen reduction process
Eil NIe
! Documentation of iance (copy offield notes - how incorporated, class A or B, time elapsed between pathogen
reduction
! Surface be incorporated within 6 hours after placed on the landn lf class A -be incorporated within 8 hours ofdischarge from pathogen reduction process
RECORDS DOCUMENTING SAMPLING AND ANALYSIS F'OR METALS
Sampling Records Analvtical Records
and times of samples collected Date and time of sample analysis
Sampling locations documented
Sample types listed
Sample types appropriate
Sample volumes recorded
Names of persons sampling recorded
Types of sample containers listed
ame of analyst
and calculation results properly documented or verifiable
All analyses are reported on a dry weight basis
Analytical QA/QC available
[l Sample containers appropriate
I trrtethods of preservation including coolingp Sampling QA/QC available
(copy offield notes - how injected, class A or B, time elapsed between pathogen reduction
on surface after I hour)
methods used
results available
Name of Contract Laboratory, if applicable:ct-*-*tt/k F"nA-
COMMENTS
Page 10 of11
METALSWORKSHEET
trvENENre
EvtrNlNra
EvnN!Nte
!v[]NINre
COMMENTS
If A > B then bulk biosolids or biosolids in a bag or other container CAN NOT be beneficially used
If A < C then High Quality (HQ) Biosolids
If A < B then bulk biosolids or biosolids in a bag or other container CAN be beneficially used
If A > C then documentation of site loadings
A B C D E
Pollutant
Actual
Sludge
Concentration
me/ke
Table I
Ceiling
Concentration
melke
Table III
Pollutant
Concentration
mg/ke
Table II
Cumulative
Pollutant
Loading
Rate
ks/ha
Table IV
Annual
Pollutant
Loading
Rate
ks.lhalyt
Sample
Preparation &
Analytical
Methods
sw-846
Preservation
and Holding
Time
Sample
Type
500 ml
As
18
75 4l 4t 2.0 3050/305 l+
60101706117060
Cool 4'C
180 days Composite
32
Cd
0.5
85 39 39 1.9 3050/305 l+
60101713117130
Cool 4'C
180 days Composite
2.7
Cu
203
4,300 I,500 I,500 75 3050/305 I +
6010/7210
Cool 4'C
180 days Composite
341
Pb
7
840 300 300 l5 3050/305 l+
60101742U7420
Cool 4oC
180 days Composite
27
Hg
I
57 t7 l7 0.85 747U7470 Cool 4"C
28 days Composite
3.9
Mo
11
75 3050/305 I +
60r01748u7480
Cool 4'C
1 80 days Composite
22
Ni
16
420 420 420 2t 3050/305 l+
601017520
Cool 4'C
180 days Composite
36
Se
6.5
100 100 100 5.0 3050/305 1 +
60101774U7740
Cool 4'C
180 days Composite
26.3
Zn
413
7,500 2,800 2,800 t40 3050/305 l+
601017950
Cool 4'C
180 days Composite
733
4t'r.AEATaon
Page 11 of11