DAQ-2025-002460

1

DAQC-425-25
Site ID 10238-B4

MEMORANDUM

TO: STACK TEST FILE – PACIFICORP ENERGY – Huntington Power Plant

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Paul Morris, Environmental Scientist

DATE: May 5, 2025

SUBJECT: Location: Huntington Power Plant, Huntington, Carbon County, Utah
Contact: Tom Wiscomb, – [phone]
Tester: Montrose Air Quality Resources, LLC
Source: Unit #1 and #2
FRS ID#: UT0000004901501001
Permit# Title V permit 1501001006 dated November 21, 2024
Action Code: 3A
Subject: Review of Stack Test Reports Dated April 21, 2025
On April 25, 2025, the Utah Division of Air Quality (DAQ) received stack test report for the PacifiCorp Energy
Huntington Power Plant Unit #1 and #2 located in Castle Dale, Utah. Testing was performed on March 25 and
27, 2025, to determine compliance with Conditions II.B.2.c, II.B.2.g, II.B.3.d, and II.B.3.f. The DAQ calculated
results are:

Source Test Date RM/Pollutant DAQ Result Test Result Limit
Unit #1 3/25/2025 RM 5/PM10, PM 0.005 lbs/MMBtu 0.005 lbs/MMBtu 0.030 lbs/MMBtu
53 lbs/hr 53 lbs/hr 74 lbs/hr

Unit #2 3/27/2025 RM 5/PM10, PM 0.003 lbs/MMBtu 0.003 lbs/MMBtu 0.030 lbs/MMBtu
15 lbs/hr 15 lbs/hr 70 lbs/hr

DEVIATIONS: The emission limit references PM10. However, PM10 sampling cannot be
performed on the stack due to the presence of water droplets. The total PM
concentration was used to show compliance with the PM10 limit.

CONCLUSION: The PacifiCorp Energy Huntington Power Plant stack emissions test report for
PM/PM10 emissions appears to be acceptable.

RECOMMENDATION: Unit #1 and #2 should be considered to have been in compliance with the
applicable PM/PM10 emission limits at the time of testing.

HPV: No.

ATTACHMENTS: PacifiCorp Energy - Huntington Plant test report received April 25, 2025, and DAQ
generated excel spreadsheets. 6 3
I
I
I
I
I
I
I
I
I
I
Yr*g.fJsg"s.r
Huntington Power Plant
6 miles west of Huntington, Utah on Hwy. 31
P.O. Box 680
Huntington, Utah 84528
April21st,2025
Mr. Bryce Bird, Director
Utah Department of Environmental Quali$
Division of Air Quality
195 North 1950 West
P.O. Box 144820
Salt Lake City, UT 84114-4820
Attn: Rob Leishman
Subject: 2025 Annua! PM Test Report for the PacifiCorp, Huntington Plant Units I and 2.
Dear Mr. Bird:
PacifiCorp is submitting the results of the 2025 Annual PM Test Report for the PacifiCorp, Huntington
Power Plants, Unit 1 and Unit 2. The tests on Unit 1 were conducted on March 25, 2025. Testing on Unit
2 was conducted on March 27,2025. The Unit 2 test was originally planned to be conducted on March
26. However, due to an unplanned maintenance outage, the testing was postponed for 1 day. Alltests
meet the requirements for filterable PM as required by the Huntington Power Plant Title V Permit
#1 501001 006.
I am authorized to make this submission on behalf of the owners and operators for the affected source or
affected units for which the submission is made. I certify under penalty of the law that I have personally
examined, and am familiar with, the statements and information submitted in this document and its
attachments. Based on my inquiry of those individuals with primary responsibility for obtaining the
information, I certify that the statements and information are to the best of my knowledge and believe
true, accurate, and complete. I am aware that there are significant penalties for submitting false
statements and information or omitting required statements and information, including the possibility of
fine or imprisonment.
Should you have any questions regarding this report, please do not hesitate to call Terry Guthrie, Hunter
and Huntington Plant Environmental Manager at 435-6874334 or Tom \Mscomb at [phone].
/
Sincerely, i
Managing Director - Hunter and Huntington Plant
Designated Authori$
I
I
I
i\
I
T
I
I
I
t
U AH DEPARI I/i.TJT OF
ENVIRONMENTAL QUALITY
I]I\/ISION OF AIR OIJALITY
T
I Enclosures: "Source Test Report tor 2025 Compliance Testing - Unit 1 and Unit 2"I cc: Tom Wiscomb - NTO Wo enclosure
I Rn!"#,ffff1h1J3tx.",ilil1,i,Ti.,o,,,."
I
I
I
I
I
t
I
I
I
t
Source Test Report for 2025 Compliance Testing
Units 1 and 2
PacifiCorp
Huntington Power Plant
Huntington, Utah
Prepared For:
PacifiCorp
L4O7 W North Temple, Suite 210
Salt Lake City, Utah 84116
Prepared By:
Montrose Air Quality Services, LLC
990 West 43rd Avenue
Denver, Colorado 80211
For Submission To:
Utah Division of Air Quality
195 North 1950 West
Salt Lake City, UT 84116
Document Number: GPO43AS-O5298O-RT-1881
Test Dates: March 25 & 27 | 2025
Submitta! Date: April 27t 2025
SIAEffib{rios*rCfr\MON I ROSE
Title:
I
I
I
I
I
T
I
I
I
I
I
I
I
I
I
I
t
I
I
Review and Certification
All work, calculations, and other activities and tasks performed and presented in this
document were carried out by me or under my direction and supervision. I hereby certify
that, to the best of my knowledge, Montrose operated in conformance with the
requirements of the Montrose Quality Management System and ASTM D7O36-O4 during this
test project.
e/.,,^> 10*ll Date:April L4,2025
Chris Wall Field Project Manager
I have reviewed, technically and editorially, details, calculations, results, conclusions, and
other appropriate written materials contained herein. I hereby certify that, to the best of my
knowledge, the presented material is authentic, accurate, and conforms to the requirements
of the Montrose Quality Management System and ASTM D7036-04.
Signature:
Name:
April L4,2025
QA/QC Specialist
Signature:
Name:
GP043AS-052980-RT- 1881 Page 2 of 91
Table Contents
Section Paqe
1.0 Introduction... .............. 5
1. 1 Summary of Test Program ... . .. ............. . 5
1.2 Key Personnel........... ............... 6
2.0 Plant and Sampling Location Descriptions............ ..........8
2.L Process Description, Operation, and Control Equipment..... .............8
2.2 Flue Gas Sampling Location ...,........8
2.3 Operating Conditions and Process Data.. .............8
3.0 Sampling and Analytical Procedures ...... 9
3.1 Test Methods......,..... ..............9
3.1.1 EPA Method 3A......... ..,..,.....9
3.1.2 EPA Methods 5 and 2O2.. .................,.11
3.2 Process Test Methods..... .............12
4.0 Test Discussion and Results......... ............13
4.L Field Test Deviations and Exceptions.... ..........13
4.2 Presentation of Results....,.... .....13
5.0 Internal QA/QC Activities ............13
5.1 QA/QC Audits ...,......13
5.2 QA/QC Discussion. ........,...13
5.3 Quality Statement ,.......,......13
List of Appendices
A Field Data and Calculations........ ...........15
A.1 Sampling Locations.. ,............16
A.2 Particulate Matter Results and Data Sheets .....18
A.2 .1 Unit 1......... ,.........19
A.2 .2 Unit 2......... ..........25
A.3 Example Calculations....... ..........31
B Facility Process Data.. ...'..35
8.1 Unit 1....... ..........36
B.2 Unit 2....... ...'.....49
C Laboratory Analysis Data .. ......62
C,1 Gravimetric Analyses ,..........'63
D Quality Assurance/Quality Control ............'....'71
D.1 Units and Abbreviations....... ...........72
D.2 Manual Test Method QA/QC Data. ............80
I
t
I
T
I
I
I
I
I
I
I
I
I
I
I
IGP043AS-052980-RT-1881 Page 3 of 91
I
I
I
I
I
I
T
I
I
I
I
D.3 Instrumental Test Method QA/QC Data.... .............84
D.4 Accreditation Information/Certifications ....,.........88
List of Tables
Table 1- 1 Summary of Test Program.. ........... .... ... ... 5
Table 1-2 Summary of Average Compliance Results ..... 6
Table 1-3 Test Personnel and Observers..... ...............7
Table 2-1 Sampling Locations........... ............8
List of Figures
Figure 3-1 EPA Method 3 Sampling Train........ .........10
Figure 3-2 EPA Methods 5 and 202 Sampling Train ................ 12
Page 4 of 91GP043AS-052980-RT-188 1
1.O Introduction
1.1 Summary of Test Program
PacifiCorp contracted Montrose Air Quality Serices, LLC (Montrose) to perform a
compliance test program at Huntington Power Plant located near Huntington, Utah. The
tests are conducted to determine compliance with the applicable UDEQ permit.
The specific objectives were to:
. Perform annual Particulate Matter (PM) emissions testing on the exhaust
stacks of Unit 1 and Unit 2
. Perform diagnostic Condensable Particulate Matter (CPM) emissions testing on
the exhaust stacks of Unit 1 and Unit 2
. Conduct the test program with a focus on safety.
Montrose peformed the tests to measure the emission parameters listed in Table 1-1.
Table 1-1
Summary of Test Program
To simplify this report, a list of Units and Abbreviations is included in Appendix D.1.
Throughout this report, chemical nomenclature, acronyms, and reporting units are not
defined. Please refer to the list for specific details.
This report presents the test results and supporting data, descriptions of the testing
procedures, descriptions of the facility and sampling locations, and a summary of the quality
assurance procedures used by Montrose, The average emission test results are summarized
and compared to their respective permit limits in Table 1-2. Detailed results for individual
test runs and all supporting data can be found in the appendices.
The testing was conducted by the Montrose personnel listed in Table 1-3. The tests vrere
conducted according to the test plan (protocol) that was submitted to and approved by
UDEQ.
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
tGP043AS-052980-RT-1881 Page 5 of 91
I
I
I
I
I
I
I
I
I
I
t
I
I
I
I
I
I
I
I
Table 1-2
Summary of Average Compliance Results
March 25 &27,2025
A list of project participants is included below:
Facility Information
Source Location: PacifiCorp
Huntington Power Plant 8 Miles
West of Huntington on HWY 31
Huntington, Utah 84528
Project Contact: Tom Wiscomb
Role: Sr. Environmental Advisor
Company: PacifiCorp
Telephone: [phone]
Email : [e-mail]
Agency Information
Regulatory Agency: Utah Department of Air Quality
Agency Contact: Rob Leishman
Telephone: [phone]
Email: [e-mail]
Testing Company Information
Testing Firm: Montrose Air Quality Services, LLC
Contact: Craig Kormylo
Title: District Manager
Telephone: [phone]
Email: [e-mail]
Russell Willson
Senior Environmental Analyst
PacifiCorp
(435) 687-433t
Russel l. Wi I lson @ PacifiCorp. com
Particulate Matter (PItl)
40 CFR Part 63, Subpart UUUUU
Operating Permit 1501001006
40 CFR Part 63, Subpart UUUUU
Operating Permit 1501001006
*Note: The Unit 1 emission limit references PM10. However, PM10 sampling cannot be performed on the stack
due to the presence of water droplets. The total PM concentration is used to show compliance with the PM10
limit.
1.2 Key Personnel
GP043AS-052980-RT- 1881 Page 6 of 91
I
I
Test personnel and observers are summarized in Table 1-3.
Table 1-3
Project Manager
Qualified Individual (QI)
Trailer operator
Sample train operator
Calculations and report preparation
I
IGP043AS-052980-RT- 1 88 1 Page 7 of 91
I
t
I
I
I
I
I
I
I
T
I
I
I
I
I
I
t
I
t
2.L Process Description, Operation/ and Control
Eq uipment
The Huntington Plant comprises two pulverized coal-fired boilers. Huntington Unit #1 is
equipped with low-NOx burners and overfire air for nitrogen oxides (NOx) control, a flue gas
desulfurization (FGD) scrubber for sulfur dioxide (SO2) control and pulse-jet fabric filters for
particulate matter (PM) control. Huntington Unit #2 is equipped with low-NOx burners and
overfire air for NOx control, an FGD scrubber for SO2 control and pulse-jet fabric filters for
PM control.
2,2 Flue Gas Sampling Location
Information regarding the sampling location is presented in Table 2-1.
Table 2-1
Sampling Locations
Sampllng
Locatlon
Unit 1
Unit 2
Dlrtancc from Nearrrt
Dleturbane
Stack Inrldc DownrtrramDlamctcr EPA *B" Uprtrcam EPA Numbor of Traverrc(ln.) (ln./dla.) 'A" (ln./dla.) Polntr
323.3 2586 / 8 647 / 2 Isokinetic: 12 (3/port)
322.7 25BZ / B 645 / 2 Isokinetic: 12 (3/port)
Sample location(s) were verified in the field to conform to EPA Method 1. See Appendix A.1
for more information.
2.3 Operating Conditions and F'rocess Data
Emission tests were performed while the source/units and air pollution control devices were
operating at the conditions required by the permit. The unit(s) were tested when operating
Plant personnel were responsible for establishing the test conditions and collecting
applicable unit-operating data. The process data that was provided is presented in
B. Data collected includes the following parameters:
. Unit Load (MW)
. Relevant CEMS Parameters
GP043AS-052980-RT- 1BB 1 Page 8 of 91
t
I
3.O Sampling and Analytical Procedures
3.1 Test Methods
The test methods for this test program have been presented in Table 1-1. Additional
information regarding specific applications or modifications to standard procedures is
presented below.
3.1.1 EPA Method 3A, Determination of Oxygen and Carbon Dioxide
in Emissions from Stationary Sources (Instrumental Analyzer
Procedure)
EPA Method 3A is an instrumental test method used to measure the concentration of Oz and
COz in stack gas. The effluent gas is continuously or intermittently sampled and conveyed to
analyzers that measure the concentrations of Oz and COz. The performance requirements of
the method must be met to validate data.
Pertinent information regarding the performance of the method is presented below:
Method Options:
o Single-point sampling is performed if Oz and COz measurements are for
molecular weight calculations only
Method Exceptions:
o Samples are collected in a Tedlar bag and analyzed on-site.
The typical sampling system is detailed in Figure 3-1.
I
I
I
I
I
I
I
t
I
I
I
I
I
I
I
I
IGP043AS-052980-RT-1881 Page 9 of 91
Figure 3-1
EPA Method 3 (Tedlar Bag) Sampling Train
t
FILTER
(GLASS WOOL)t
I
I
FLEXIBLE
TUBING
I
3.1.2 EPA Methods 5 and 2O2
Determination of Particulate Matter from Stationary Sources and Dry
Impinger Method for Determining Condensable Particulate Emissions from
Stationary Sources
EPA Methods 5 and 2O2 are manual, isokinetic methods used to measure FPM and CPM
emissions. The methods are performed in conjunction with EPA Methods 1 through 4, The
stack gas is sampled through a nozzle, probe, heated filter, unheated CPM filter, condenser,
and impinger train. FPM is collected from the probe and heater filter. CPM is collected from
the unheated CPM filter and the impinger train. The samples are analyzed gravimetrically.
The sum of FPM and CPM represents TPM. The FPM, CPM, and TPM results are reported in
emission concentration and emission rate units.
Pertinent information regarding the performance of the method is presented below:
o Condensed water is measured gravimetrically
o The post-test nitrogen purge is performed by passing nitrogen through the
train under pressure
o To simplify shipping arrangements to remote locations, stainless steel
probe liners and nozzles are used. Aftereach run, the nozzle and probe
liner are brushed and washed a total of six times with reagent-grade
acetone to assure complete recovery of all particulate matter. The brush is
given a final rinse with acetone and the nozzle and probe liner are given a
final rinse with acetone and all rinsate is collected into the appropriate
sample container
The typical sampling system is detailed in Figure 3-2.
I
t
t
I
I
I
I
I
I
I
I
I
I
I
I
I
I
IG P043AS-052980-RT- 188 1 Page 11 of 91
Figure 3-2
EPA Methods 5 and 2O2 Sampling Train
3.2 Process Test Methods
The test plan did not require that process samples be collected during this test program;
therefore, no process sample data are presented in this test report.
Emtrv
'l0o ml lto
(modn.d, m tlp)erpty (t'dtdlrcl&,2OtLi)0g
Sltca G€l(ndfidlnlb)
THERMOCOUPLESIJ
BY.PASS VALVE(h.d'..) VACUUM GruGE
4.O Test Discussion and Results
4.1 Field Test Deviations and Exceptions
The Unit 2 test was delayed from March 26th to March 27th. No further field deviations or
exceptions from the test plan or test methods were identified by the Project Manager.
4,2 Presentation of Results
The average results are compared to the permit limits in Table 1-2. Emissions are reported
in units consistent with those in the applicable regulations. Additional information is included
in the appendices as presented in the Table of Contents.
5.O Internal QA/QC Activities
5.1 QA/QC Audits
The meter box and sampling trains used during sampling performed within the requirements
of their respective methods. All post-test leak checks, minimum metered volumes, minimum
sample durations, and percent isokinetics met the applicable QA/QC criteria, except where
noted in Section 5.2.
EPA Method 5 analytical QA/QC results are included in the laboratory report. The method
QA/QC criteria were met, except if noted in Section 5.2. An EPA Method 5 reagent blank
was analyzed. The maximum allowable amount that can be subtracted is 0.001o/o of the
weight of the acetone used. The blank did not exceed the maximum residue allowed, except
where noted in Section 5.2.
EPA Method 202 analytical QA/QC results are included in the laboratory report. The method
QA/QC criteria were met, except where noted in Section 5.2. An EPA Method 202 Field Train
Recovery Blank (FTRB) was performed for each source category. The maximum allowable
amount that can be subtracted is 0.002 g (2.0 mg).
5.2 QA/QC Discussion
All QA/QC criteria were met during this test program.
5.3 Quality Statement
Montrose is qualified to conduct this test program and has established a quality
management system that led to accreditation with ASTM Standard D7O36-O4 (Standard
Practice for Competence of Air Emission Testing Bodies). Montrose participates in annual
functional assessments for conformance with D7036-04 which are conducted by the
American Association for Laboratory Accreditation (A2t-A). All testing performed by Montrose
is supervised on site by at least one Qualified Individual (QI) as defined in D7036-04
Section 8.3.2. Data quality objectives for estimating measurement uncertainty within the
documented limits in the test methods are met by using approved test protocols for each
I
I
t
I
t
I
I
I
I
I
I
I
I
I
I
I
I
I
IG P043AS-052980-RT- 188 1 Page 13 of 91
project as defined in D7036-04 Sections 7.2.L and 12.10. Additional quality assurance
information is included in the report appendices. The content of this report is modeled after
the EPA Emission Measurement Center Guideline Document (GD-043).
Appendix A
Field Data and Calculations
Appendix A.1
Sampling Locations
PacifiCorp Huntington Power Plant Sampling Locations
Particulate Matter Sampling Points
<4
Stack Cross Section (A-A)
Unlt
Diameter (D)
t2323.3" 322.7"
Upstream Distance (A) >220' >220'
Downstream Distance (B) >266' >266'
Sample Point Distances from Stack W.ll
Traverse Point 1
Traverse Point 2
Traverse Point 3
L4,L" L4.L"47.3" 47.3"95.7" 95.5"
Appendix A.2
Particulate Matter Results and Data Sheets
Appendix A.2.1
Unit 1
GP043AS-0s2980-RT-188 1 Page 19 of 91
I
I
I
PROJ{329&
P.diCorD
HundrtM Unt I
tlz9lm2'
a
EPA M.drod 2 D.b
/a",Mt)Nll(-()5t
Runl 1 IlunTlm. 8:U 10:57Sbrnm 10:24 13:10
3.@hnm (nln.l 120 120
t
l3:53
t5:12
120
1 2 t Aw.t.
I D.
q
T,
P.
q
q
323.3
23.89
{.2
0.84
0.8357
110.75
570.084
{.31
30.20
28.92
23.S8
570.75
54.9
,3,5t4,557
1,225,243
323.t
23.70
4.2
0.84
0.ut5
1!2.11
570.084
{.3r
30.22
28.78
23.39
572.11
56.2
73,352,516
L,222,5t1
lnpuB
St.ct Diamater(lncharl
8.rom.tdc Prc$ura ("H81
Si.cl Static Pr.$u.. ("HrO)
Pitd T!b! Cocfficicnt (unitla$)
Av!. velocity H..d ofSl.ck G.s v("HrO)
St.ck 6.s Temp.niure l'f)
calolatlont
st.ck Arr. (ft'1)
St.ct Statia Prltiur! ("HBl
Srck G.s Mol..ul.r w.ltht, dry basis (lb/lb-ml.)
St.ck G.5 MolacularWdot, w.t basis (lb/b-mol.)
AbsluE Stack Prersura ('XB)
Abroluta Steck G.sT.mp...tur. ('R I
St.ck G.s vcloclty (fvt.cl
SE*G.. Dry Volum.tdc Flow &te {d*f/hr)
St..k Gar Dry Volumatdc Fl* R.t. (di.tnln)
323.3 323.1
23.65 A-rS
{.2 1.2
0.8r 0.14
o_u27 0.il4
112-92 112
570.0u 3r0.08'l.0.r1 {.r1
n.22 *.2
24.15 T.A
23.14 2a-U
5?2.92 372
55.9 55.7
72,381,W 7a,r5,,U
1,200,731 '.219,Ln
o"
c1
c2
I
I
I
I
I
I
I
I
I
I
I
I
t
I
I
olluoto.E 1 2 3 Avota
Or (*vd) 1.1 5.9 7.1 ,.0
COr (96vd) 12.0 12.2 r2.1 [.1
EPA M.$d. D.b
hp6
Vt Volumc ofw.tcr Condaniad (mL)
V. Volum.ofStack Gas Coll.d.d (dc0
Y M.tarc.libGtlon F ctor(unltlaid
6H Prcrorc Dlff.r.ntl.l Ac.o$Orific. ("HrO)
T. Tamprrature at Ga! Matar ('t)
C.ldhtl6
P- Ab$lur. Pressuro.t 6.i M.t.r ('H8)
T- Abelut€ T.mfr.tur. .t 6.. Mcter {'Rl
vdr., Volunc olwai.rcond.n..d (iO
vntdr sampla Ga,voluma (dsct)
8-r Obrry.d St.cl G.r Mollturc Content (X/100)
B-.r saturat.d Moisiur. cont.nt (x/lm)
8- Moinur. Ont.d Usd {X/lm,
r86.4
92.8{E
0.9970
1.1
6s.1
21.07
s2s.1
8.17
74.65
0.105
0.113
0.105
219.3
96.325
0.9970
1.8
64.57
23.83
524.67
10.32
75.96
0.118
0.118
o.l 18
217.8
94.646
0.9970
1.8
67.t
23,78
527.8
10.2S
75.m
0.120
0.121
o.120
20r,8
94.392
0,9t 70
t.E
€5
2t.t!
521,9
9.74
,3.91
0.115
0.11,
0.113
Norrla dlameter ("1
M.$ ot PM coll.d.d on tllt.r (mt)
M.s olPM collcdcd ln ilnra (mg)
M.tl ot.c.tonc bl.hl lml)
0.234
0.0
9.9
0.0
I
0.234
0.0
9.6
0.o
3EPA M.thod 202 D.h
lnpuu
M.ss ot lnorg.nlc Condcnslblc PM (m8)
M.s! otOr!.nlc Cond.nrible pM (msl
Tol.l CPM Mass lma)
Mrls ofrain bl.nk (m!)
Tot.l CPM M.$ la$ Elanl (m8)
lhlslon cahuladona
F. Fucl F-Faator (saf/n60tul
lh Crcss-s.ctlonal.r.. ot noul. (rt1)
I lsklrcllcvad.tbn (ta)
Tot.l Fih.Eble PM m.rs l.B bl.nk (ma)
q Fllt.r.bl.Pefricul.t.com.ntr.tion(8rldko
g Flltaabh Paftlcul.t. conc.ntr.tion {lbldrc0
Ero, Flltarrbl. P.frlcul.t. m.$ rmlssion r.t. (lb/hr)
Boll.r Lo.d (MW)
Fllt.nbl. P.nicul.t. m.$.mlt3ion Etc (lb/Mw-h.l
t. Fllt.nbl€ P.nicul.t. m.$.ml$lon Et. llb/mmBtu)
u@ hdr fllt.r.bl. P.dlcul.t. m.sscmislff nt. (lonrF.r)
q Cond.nsibhP.ftlcul.lacom.ntr.tion(rrld$l)
q CondlnslblaPrdlculataconcantratlon(lb/dio
Eu. Condantibla Paniculitr m.i3 emlrsion Bt! (lb/hr)
F. Cond.nalblc Pr^lcul.la d.r3 anl3aion 6t. (lb/mmgtu)
al@n$ty Cond.n3lblcP.nlcul.t.m$r.masionnt.(tonr/yaar)
Tot.l p.dlculat. cff c.ntr.tlon (trld5c0
Tot.l Padlculata conaantration (lb/drco
Total Partlculata mass amlario^ ratc (lb/hr)
8oll.r Load (MW)
Tobl p.dlculat. m.!5.m|!slon r.t. (lb/Mw-hr)
Tot.l P.dkul.te ms3 ami rlon r.t. (lb/mmBtu)
Total Pani(ulata mati amiralon ralc ltonrEar)
5.3
1r.8
19.1
2.0
17.1
1840
2.99€4
97.0
15.5
0.m3
4.588-07
33.7
491
0.07
0.007
111.4
0.m4
5.05E{7
t7.1
0,008
152.6
0.007
9.63r{7
70.8
491
0.14
0.015
310.0
3.1
9.8
12.9
2.0
10.9
1840
2.998"04
1m.2
9.9
0.002
2.8IE4?
20.8
494
0.04
0.@a
91.1
0.m2
3.12E{7
22.9
0.m5
1m.3
0.m
5.95E{7
43.7
491
0.G)
0.009
191.4
2.7 '.710.3 11.313.0 S.0
2.0 2.011.0 13.0
1840 1?O
2.99E44 2.99c.oa
98.7 $.5
9.6 11,'
0.@2 0.@2
2.82E{7 3.alr{7
20.5 25.0
177 07
0.04 0,05
0.m4 o.ms
89.7 tot./t
0.m2 0.m6
3.23E-O7 '.t0E{723.5 27,a
0.m5 0.m6
102.8 X[.9
0.u o.ml
5.06E-07 '.2LES'(.0 s2.l477 47
0.(D 0.110.@9 0.011192.3 231.3
GP043AS-052980-RT- 188 1 Page 20 of 91
.l
2^
l
<o'[
l
T
P'r
o
l_
o
,(dtt
-i
l
r
-
ot
,
1
t
l

,.
'^
i
{
q
l
.i
q

*.
,
rl
t
-
i
-
r
.
,
-l
o
,t
;
tJ-
rl
l
-
1
.
r,
l
v
r
u{
--
-
II
vf
\
n
.4
w
-i
-
ol
-
,
q!t,arot>:
i'

I=oc!qEogaE&Ioa
II
/d{
!I
I
I,t
-
.
i
ge
jJ
g
=
l

I
<
4-
t
<
EoEIc:.3oaaaoG!va'
..
.
J
EacTIsrj
.
i
I
re
l
Nl
l
rn
i
/.sJ
i
fe.
l
JI
Il-
t
l'
+
ilir
Jt,,

I
i;

t
la
l
iH

r3l
tJ
J
a
U'
Y
oad'
t-
l
-Zi
oe7it
It
E
\
-r
l
-.
o
Q
t
:'
e
3
ai
>3
E!
-Y
Gts
F
Ei
I
c(>
^i
;
o
1e
r
eePI3o
-
Oe

t
rE
IS
r

E
S
a,
l
*l
-
^

E'
lr

A
ii
i
i
i
i
i
IATEE
Iqo
7naoC6IT
IAFt-t
-)qIcotn
I
,-
l
rlqol
IIIIlr
t
4<
114r
Irtl
ovF..
J
rAoI
IIItIIIIIIIIITI
:(tlo.-
,

ONNoc,
l
(go-
0
,ltt
.'
;
9u
tbE9E!
lo
i
I!!E
E
E
(,
O
,
{
-
6F
al}fc.
)oo
]-
f
f
:
lr
r
t
!
il
t
i
-i

;-
f

i
--
i
ll
i
t
li
i
l
l
ol
q
o
c.
J
i

o
lilr
l
"
ll
ti-
s
oo6E-
roEoForioEoFoooo
goc,o2_ocEaaaoEE\
.J
l2l
cUEoso-I
sl
'9
1
DllcJc!o&tt
:Ia!:SIII6o
o
Ao
o
Oa
J'rFtdIrro
t@E9
ti
,
i
toSr
n
B<
o1
r
l
$
xo>a
-
(,
tJ
J
i
oyo,
d'
1-
azi
oe7,
iE
Oa
c
fi
'
s
E
is

s;

X.
i
l@

a,

t
3
s
6*
i
?
i
o
;E
a
;
e
g
c-
-
qE3
-
:
i
P
u
fr
F

F
F
!
g
i.
a
II
,t
<r
'o
.
r
,
R
P
2i
g
*e
l
cl

b>
EE
c
g
E9
-Y
c
ca
=@c
9
€-
"
8
<g
a
li
.
lO

el
lr
-
,

)
l*
r

i
E:
i
E
E
E-
A
O
ao
O
-
-
ii

Ei
:
lc
x
{

4
Hr
r

di
:
i
?i
i
g
i
i
$;
i
,
I
{d

3l
!
ii
i

rl
/'
T
'i
^
l
<;"[

I
ag
I
I
;'
i
i
l
l
'i
t
,
t
n
l
q
i
r
.
a
d
n
r
?
o

J\.A'v
I
.r
.
.
>
a
f5'
(
.
r
,{
v
+-
-
-
i
*-
:
-
T1
(l,
I
|
\-
i
--
c
-l3rl
,o
l
l
*-
-
-
-

I
l1

gl
ri

.l
lr
-
l
i"
:
r-
l
i,
r
l
i
li
C
i
'-
t

,
lli,
-
:
li
l
-
ir
i
l
rl
l
,
-t

'-

'l
li
i
ii
l
-t
*

-l
|l
t
li
;
l
fi
t
il

it
l
i
lrr++
-i
-
-

-+
-
LI
il
I
'lrtrttIr
Ilr
li
t
4
Ii
t:
tl
f'
n

,-
V-

*
-r
t
u
i
t
t
l
.
i
;]
5
5
s
\
r
;
v
,
!

I
,i
i
i

;;
i
.
*
9j

rl
-
,

E
*.

.>
,
j
>

{v

r}
*
.I
i
-
l
r
.
L
.
-
1
r
n
f
1
i
_
r

rs
i
i
I-
[
'

i1
-
l
.

I
I
I
Y-
,
)
\l
J+
'a
Y
;i=t
$
\o
l
rfrl#lii-
-
i
!
""
i
"'
l

r
rfli
I rz
r
i
,
ll
.
I
-l
:
ot
s
!
J:
=
=<e
&
!
IIIIIIIIiIilII
il
dAst
(/
)EII
IEqItt!(lEoIU3
=c,ca?GaI
rvtJEsoE
I4,i5t
i'
u
E
3
t
E
h"
zL
c
l
E
ii
E
!r
t
\.
!
t

'1
<.
^v
Q
r
{g
r
91
oF
a
c=
i;
g
.L
g
a
=
=r
n
I
]-
-l:E
(
9=
e
i
r
i.

>t
E
Pr
^
gE!
?
.
-
6d
c
u
L
]s
r
e.

'
Yl
t
r
I
s
o
8.
.
ii

I
g
ii
l-
l
r
l

I
"i
!
$
{
.
t
n4
I
!E$
Dt
,

i
9,

I'
II
f
l
I
#
3
I
o-
,)
Il
J
:
,
q)
y
oad'
t-
azi
oe7iE
r','r] ":*S[npa. R.cotlty 3 Ca[rldon Ch.ct tn-hr.t0d, llgN,T+g.s.E
I
I
I
I
I
I
I
I
I
II
t
I
I
I
I
Srr0llcrllan &on-Drrtttotn'l!{
Balanco
tlroldtbw gLr^f__.
Holrl$at$
O,SISLEEI
hll!dr-.*
-
tatE JJffidtlr..e
FEBrllE e
frrf HilrrtlatralubEtlll,"@ )f,i u -zsl
ztffir m
-e
-:-
,rrr,rr o errr o rb o r o -rrr-;d f*- fclir" (""+rJ
nr. Pr* ord o lod B *dt o cr
tr tr crtr otr o r
Et errrr P qy o rl! Ittftr " o-g,ZAL nr ?271 -l,,.r. e.ST
o gr o lrrr pr.o ffi tr adr
ErLs+*a
Page 24 of 91
Appendix A.2.2
Unit 2
GP043AS-052980-RT- 1 88 1 Page 25 of 91
T
I
t
I
I
I
I
I
I
I
I
I
Pnots2s
Prdf,Corp
Huntlnato Unh 2
,l2rlzOE
s
tPA M.$od 2 D.b
[v r r\l()r\ lK()\t
D,
g
T,
a
a
t22-7
23 67
-4_2
0.9
0.7r20
113.58
s67 _970
.0.31
30.33
28.m
21.36
573.58
51.1
65,392,434
1,105,541
322-1
23.59
4.2
0.84
o_7475
114 57
567 -970
-0.3r
30.31
2A_14
23.38
s74_51
49.5
63,798,599
1,063,310
Run, 1Sbnflm. 9:06Stopflm. 7l:22
S.md. nm. (mln.l I20
2
12:45
r5:00
120
2
3
l5:25
t7:35
120
3
372.7
2:.S9
4.2
0.84
0.1192
11S.5
127.7
23.'
1.2
0.14
0,7662
115
567.970 56r.970
{.31 {,r1
30_31 m.32
74.76 2t.tl
23_28 lt-aa
575.5 Sr3
51-9 50.9
66,139,567 6s,{3,5rt1.102.326 1.0110.726
Ollu.ntorb 1 2 t A6..ta
CO, (96vd) 12.9 12.8 12.8 12.!
EPAMaolod{O.E I I 3 A[r.1.
Vk Volumc ofW.t.r Cond.ns€d (mI)
v- Volum. ofSt.cl Ger Collectcd (dco
Y Metlr C.libration Ficlor (unille$)
AH Pr6tur. Olfflr.nilal kross Oriticc ("HrO)
lnpuE
Sr.cl Oi.m.trr(inch.r)
B.rom.t.k Pr.s!urc l"Ht)
Steck Strtic Pressur€ ("H)O)
Pitot Tub. Co.ffici.nt luniil.ss)
Avg. V.locity H..d olStack G.s Vl"HrO)
Stack Gas Teftp..ature l'F)
C.kulatlont
Stect Ar.. (ft))
St.cl Static Pressur€ ("Hgl
Stack G.s Molecular WeiSht, dry basas (lbllb-mole)
Stack Gas Mol.cularW.lSht, w.t besis (lb/lb-mol.)
Ab3olute 5t.ck Pressure ("H8)
Absolui€ Stack Ga! Temperature ('R )
St.ck G.s Veloclty (ft/r€c)
St.ck Gaa DryVolumetric Flow Rate (dscflhr)
Stack Gas Dry Volum.trlc Flow Rat€ {dscf/mlnl
T.
s.,
218
7N.729
0 9900
1.8
74 96
23.m
534.95
70.26
78_21
0.116
0.123
0.116
1
226.9
98.834
0.9ffi
1_1
84-67
23.82
5{.57
10 68
75.47
0.124
0.127
o_121
7
241_6
103.329
0.9900
t.9
86
23.73s
11.37
1a.42
0.127
0.131
o_121
228.8
100.964
0.9300
1.t
t2
23.74
541.9
to.n
n39
0.12
o.Lz,
0.!u
T.molratur. at Gas Meter ('F)
Crlolatlon,
Absluta Pr€srurc at 6a3 Meler ("H81
abslute T€mp€r.t!rc at G.s Meter ('R)
Volume of W.tcr CondenEd (sc0
$mpl. Gas Volum. (d!c0
Obs.ded Stack G.r Moisture Gnrenr (*/lm)
Satur.ted MoBtur€ Cont.nt (*/1m)
Morstur. Cont.nt Us.d (*/1m)
EPA i/i.drd 3 D.b
lnPub
O^ ilozzlc di.m.ter (")
Cl Mais of PM .ollected on fihe. (me)
C2 Mais of PM coll€cted ln ilnse (mt)
w. Mars of e..tone bl.nk (m8)
EPA Mdh6d 202 D.t.
0.249
0.1
10.5
0.0
0.245
01
6.9
oo
0.245
0.0
6.3
o.o
I
0.245
0.1
7.9
o_o
lnput
Me$ o[ lnorg.nic Cond.nsibl€ PM (mt)
M.ss ofO[.nic Condcnsible PM lmg)
Toral cPM Ma5s (mg)
Masroftraln blenk(mt)
Tot.l CPM M.ir l€ss 8l.nk (m8)
Ehlrrlon Olc!latlont
Fuel f Factor (sflmmBtu)
crois.s.ctlonel ar.a of norzle (ft')
lsolln.ilc vail.tion (Xl
Tot.l Flltlr.bl! PM mass lcss bl.nk (m8)
filt!rabl. Paticulatc concentration (8rlds0
Fih€rable Peniculete concentration (lb/dscf)
tilt.r.bl" P.niculat. m.r! €mi55ion r.te (lbAr)
Boil.r Lo.d (MW)
1_9
6.5
t4.4
2.O
17-4
1&0 lm
3.27E44 t.zrC-g
102.9 102.5
6.3 t.0
o.ml 0.@l
t_77E41
'.27a4111.7 14.9
42 4g
0.03 0.03
0.003 o.oot
51.3 65.1
0.m2 0.m2
3.49E"07
'.07C.4723-r 20.0
0.005 0,u101.0 t7.6
0.m 0.@a
5.26t{7 S.l{{'34.8 14.'u2 4g
0.08 o.ot0.008 0.m152.3 152.7
1ilo
3.27e44
102.3
10.6
0.m2
2.99E47
19.8
450
0.u
0.m
86.8
0.m1
1.49E{7
9.9
0.002
13_4
0.m3
4.48t{7
29.7
@
0.s
0.006
130.2
11.4
S,1
15.5
2.O
r4.5
1840
3.27t.O1
702.7
7.O
0.ml
2.04E{7
r3.0
4m
0.01
0.003
s7l
o.@3
4.24E.O7
27.O
0.ffi
118.4
0.004
6.28E{7
40.1
4m
0.8
0.009
175.5
7.8
5.0
t2.7
2.0
lo.7
I
c,
c,
I
t
t
I
Falt.rabl. Padi<ul.t. ma!r.mrr$on r.t€ (lb/Mw-hr)
F. Filter.bl. P.nicul.t. mr$ emistion rate (lb/mmBtu)
A7@ htslrt Fllt.r.bl. P.dicul3t. mais.misslon rate {tons/yea4
q Cond.nribl.P.ni.ulat.conccntratio.(trldsco
q Cond.nsibleP.ticul.t€concentration(lb/drcf)
E,w Condchtlbl. P.daculat. m.is emrssion r.te (lb/hr)
F. Condcnslbl. 9.dlcul.t. mrss.mlssion ret€ (lb/mmStul
a7@fit/y. Cond.nsiblc Paticul.tc mass €misron rate (tons/ye.r)
Total P.iicul.t. con(.ntration (8rldsco
Tot.l P.nicul.te conccntr.tion (lb/dsc0
Total Partlculate mass emisrion rate (lb/hr)
Boll.r Load (MW)
Total P.rticul.t! m.ss lmission r.te (lb/Mw-hr)
Total Pani.ul.te mass emi5sion rat. (lb/mmBtu)
Total Padicular€ mas3 emisraon rate (ton3/year)
GP043AS-052980-RT-188 1 Page 26 of 91
IIiItIIIII
I,
IA
t!EToII-ECllIc,
IIr:8II
:.HEBOdOr
JFtd
.
I'lo
:,
8
tqIYgl
,5$TE
(,(Jo3
gaT$o.EE6*
QIbTEE1olCI-qo'Iaa6-
cY
l
lqsciEFT5qIcgIp
nI
I'
cETET
'TTT
a2
33Ogat
:+i
aa6tPioo
tr
.

I
sF
a
3E

E
Ef
r
!E2L
otEgI€
a26caIaEoaecl
IE6t,iiI:
t^
'
r
l
..
i
44It9n
r.
{

.
rl

^
-1

-
II
^"
1
-
q-
:
Lf
,ILf5aEoI
EcaEo,EoUTEaE!.n
oEFE8*
Dfi
.
s
1t
:
-:
_

-
8r
5F
ipF
,I
)I-l!qEr
!
(a
y
cad'
l-
aZ1oa7,
i
€
-q
i
l
q
r
It@8EoIaEa8Eo,
IgfIII
iiE
tit+E*
gNlns{
IE6*uv3
cC I
^lrl
fr{g()o'c
iFc)CG:
I4,1Ioo?c
;,1ct
l,jia!
!'
i
4
il
'-
l
'r
l
:
]
rl
l
'^
i

..
]
qeQ€
t
E_
s
CDZI>:
J
ECaEo.Ec,el
=5eE.l
-,
1EE6i
$eEI
ExET
'i
"
]
"l
x
l
,l
t
4
I
l-
o-
E
-.
isl9T
't

€
o-
e
33
.
E;
t
iE
$
-:
i3J
E
ltr
.E9nob
oIoC)Etfi
o6Iac:d
I
a2cI6ELeaoec
cl

"
..
{
t
.
"f
.
I
t1II
t-
i
lttt
9tsts
CE'
:_qoEr
-
fl
.
i-
.
i3
I
IFoIIIaafoIt
J*
lol
"J
l
EEIJc-
J
il
lEI
:
t)
yOZd-
l-
i
Zzoe2iE
II
iIIIIIIIIIIIIIiiI
I!
IEToa=aa.caaaoItl!^/
lRlt!ETJe1Ll
)
l
eEToIIa!qIEtaD
IEgII3tdRBIFt4
.c
)p3
3l

c{
o
lt
)
ao
EId(
,o<rsQOgb
oE
II
,I
.r
l<l
.qE;
Ii
t!uln,,oaPjIll
I
'.
.
:

i
^llo
r
,t

-1
4r
J
{,

ci
cn
'
Q_r
-
it
'
rO
III
..
:
.
i
Cl

rl
-lE
/-
i
E<
t
a<a'
oUO
=La-E9
-
02
)JI<+.\.JI'l
CA
I
::niititU
ol,I;c-
i
l
Io,gar/
lJIr-
-NIc4g
c!aEoI
|-
yw:
::E
i5EE
e!Ec6EGJ,"
{^locgtaPo-
!.6iEoF=TE
I
.J
l
/rl
I
ocgeaPA
l3
r
EB
g
+:
o
9.
:
-
t
!4i6tEoec,EEoct!=
7G;Io(,,EoEgo=c
ciooocaDIo7
r-qoIEqoIEot=
l^
l
r{5iiot-
LlEI
>t-l
.l
I:I{l
I
El-1
!lzl3i
goo{,a=oo;EF8l)ta.oouttoE
"*--LnJ-
I
I
I
I
t
I
I
I
I
I
II
I
t
I
I
iI
I
Srmplr Rrconry 3 Crllbrellon Ch"cl Drtnhr.t
, -L3 S/z,ou opcratlr frq)
mcf A.d^(F'oroH,"HEE
sEndru mas.i. o '-Sdo. OFlaEtrdencrmassng -W
05e ol dr.d( urrgrf nr$s)
lil.rnldlt-% -iln'F A6
htuE tlI5!E. EE ,r, Xt n- .rsrlt tilrl tU D ltm ln ortra n o.r nitrrtr.brrr -Z{S ot ,ZI{( w .ZYS o0.Zil("^-T
ZtE'rEt D1 n t,3
lrlrlIr Oi Ol ---B_ Alr1abr o qra oF o .r o mnt. o ffi pcr- le(/q. ?o.t- Pa outrr. o *od o *cou tr d:t- trqrrooh- trr Fr*, tr dr
o qrrb.iDj516r o T-t o Tfirr o c:w,t-4-tutx ?Uo n^* ZZll *trt oqrlrtrrt Ptara T.rrhft tr*
tr uar-
0u&(laef*22S
Page 30 of 91
Appendix A.3
Example Calculations
I
I
I
t
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
PROJ{52980
PacifiCorp
Huntlngton Unlt I
Run t1 Sample Calculatlon3
EPA Method 5: Determination of Partlculate Matter Emlsslons (/rc CFR Part 60, Appendix A-11
lv i Nlt)r\ I l(().\l
Varlable Value Deflnition Unlt of Measurement
D.323.3 Stack Diameter inches
A 570.08 :ross-Sectional Area of the Stack ft'
P.-4.20 Stack Static Pressure in. H2O
P.-0.31 Stack Static Pressure in. Hg
%co1 12.0 :onc€ntration of Carbon Dioxide Orv Volume Percent (%vd)
%oz 7.1 :oncentration of Oxvcen Dry Volume Percent (%vd)
Md 30.20 )ry Molecular Weight of the Stack Gas (default)lb/lb-mole
Pt..23.89 larometric Pressure in. Ht
AH L.7t ,ressure Differential across Orifice in. H2O
P-24.O2 \bsolute Pressure at Gas Meter in.Ht
t-65 Temperature at Gas Meter .F
T-525 \bsolute Temperature at Gas Meter .R
K1 0.04706 :onversion Factor ft'lmt
186.4 /olume of water Condensed 8
8.77 /olume of Water Condensed scf
K4 77.64 :onstant 'R/in.Hg
0.9970 Meter Calibration Factor Unitless
92.805 /olume of Stack Gas Collected dcf
74.549 iample Gas Volume dscf
B*,0.105 itack Gas Moisture Content %l7OO
M5 28.92 \ctual Molecular Weight of the Stack Gas lbllb-mole
P 23.58 \bsolute Stack Pressure in. Hg
T 110.75 \verage Stack Temperature I
Trtatn 571 \verage Absolute Stack Temp€rature .R
KP 85.49 :onversion Factor (ftlsec) x v(((lbllb-moleXin.Hg))/(('R)(in.HrO)))
ce 0.84 ,itot Coefficient Dimensionless
AvgYAp 0.8357 \verage Square Root of Velocitv Head Readings in. HzO
s4.90 \verate Stack Gas Velocity ft/sec
T*a s28 ;tandard Absolute Temperature .R
P 29.92 itandard Absolute Pressure in. Hg
a 73.5t4.557 )rv Volumetric Flow Rate Corrected to Standard Conditions dscf/hr
D"o.234 'lozzle Oiameter inches
An 2.99E-O4 :ross-Sectional Area of the N02zle ft'
mn 32.60 otal PM and CPM Mass mg
q 9.53E-07 )articulate Concentration lb/dscf
Eto/1.70.8 )M Mass Emission Rate pounds per hour
F 1E40 :-Factor from EPA Method 19 scflmmBtu
Eb/mmBtu 0.015 )M Mass Emission Rate pounds per million Btu
Eton.r,,310.0 PM Mass Emission Rate tons per year
K5 0.0945 :onstant (in.Hg. min) / ('R.sec)
e L20 iample Time minutes
97.O%sokinetic variation percent
GP0434S-052980-RT-188 I Page 32 of 91
PROr-{t52980
PacifiCorp
Huntln$on Unlt I
Run 11 Samph Calcul.tions
EPA Mcthod 5: Drt.rmlnation of Particulat. Mrttcr Emissions (f{l CFR Part e0, App.ndL A-11
A= n(D,/24)'?
11323.3124l,^2
= 570.08 ft^2
\= Ps/L3.6
= -4.2/13.6
= -0.31 ln. Ht
Md = (0.44 x %CO2) + (0.3 2 x %O2) + 0 .?A|LOO-%CO r%O 2l
= (0.44 x 12.0) + (0.32 x 7.1) + 0.28(100 - L2.O - 7.L|
= 30.20 lb/lb-mole
P.= Pb.+(AH/13.6)
= 23.89 + (1.71113.6)
= 24.02 in. Hg
T..460+t-
= 450 + 65.1
=525 R
Vwq.dl= KrxVtc
= 0.04706 x 186.4
- 8.77 scl
V-tot= (.xYxV.xP.
T.
= 17.54 x 0.997 x 92.806 x 24.02
525
= 74.55 dscf
B$= Vx(*dl
(Eq.4-3)
VwcGtal + VmGto)
8.77
8.77 + 74.65
= 0.10s {9(/1(nl (Eq. a-a)
M, = Mo x (1-B*J + (18.0 x B*')
= (0.44 x 12.0) + (0.32 x 7.1) + 0.28(100 - 12.0 - 7.1) x (1 - 0.105) + (18.0 x 0.105)
= 28.92 lb/lb-molc (Eq.2-5)
Pr= Pb.r + P.
= 23.89 + (-0.31)
= 23.58 ln. Ht
Tl.u= 460+T,
= 460 + 110.75
=571 R
,ar \ M()N lli().\t t
I
I
I
I
T
I
I
I
I
I
I
t
I
I
I
I
t
IGP043AS-052980-RT- 188 1 Page 33 of 91
T
I
I
I
I
t
I
I
I
I
I
I
I
I
I
I
t
I
I
PROJ-0529t0
PaclflCorp
Huntlnllon Unlt 1
Run ll Sample Calculations
EPA MGthod 5: D.tGrmin.tion of Partlcul.tc Mattc. Eml3sions (/o cFR Part 50, ApP.ndix A-11
V, = Ke x ce x AvgvAP x
= 85.49 x 0.84 x 0.8357 x
= 54.9 ft/scc
Q = 3600 x (1-B*) x (v.) x (A) x (T.,a x P,l
(T1.5ry x Pr,6)
= 3500 x (1 - 0.105) x (54.90) x (570.08) x (s28 x 23.s8)
= 7t,514,557 dscllhr
A = r(DJ24)'z
n(o.234124],^2
= 2.99E{4 ft^2
{.s71x29.921
(Eq. 2-8)
(m&/g) (8,/lb) (V.rnd,)
= 32.6
( looo (4s3srr) (?4^64r)
= 9.63E-07 lb/dscf
E575,= C.xQ
= 9.63E-07 x73574557
= 70.t lblhr
E"r..'.=-!L1l]4-
(COr%vd)
= 9.63E-07 x 1840 x 100
(12.0)
= 0.015 lb/mmBtu
E,o7n. x (Hrs/yr)
(lbs/ton)
70.78 x8,750
2000
= 310.0 toni/ye.t
| = K5 xT.1.6.1xV-1161x 100
Pr{.br} x V, xAn x e x (1-BB}
= 0.0945 x 571 x 74.5,49 x 100
23.58 x 54.90 x 3.0E-04 x 120 x (1 - 0.105)
= 97.O*
GP043AS-052980-RT-188 1
Cr=
(23.58 x 28.92)
(Eq.2-7)
(Eq. s-7)
Page 34 of 91
Appendix B
Facility Process Data
Appendix B.1
Unit 1
Source
OU25l25 08:11
Average Data - Run 1
Plant: HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 08:11 Through0312512025 10:24
10.9 1.4 107.O2
I
I
I
I
Time Online Criteria: 1 minute(s)
UNITl
BARPRESS
(INHG)
co2
(PCT)
OPACITY
JPCTI
STKTEMP
(DEGF)
UNITLOAD
(tliiw)
Ogl25l25 08:12 1.4 106.74
03125125 08:13 10.9 1.4 10€.71 IOA25l25 08:14 23.900 10.9
Ogl25l25 08:15 lo.9 1.1 't06.85
Ogl25l25 08:16 23.900 I10.9 1.1
03125t25 08:17 1.4 106.90
03125125 08:'18 23.899 1.4 107.05
03125125 08:19 1.1 107.10 I03125125 08:20 23.899 '1.1 107.33
Ogl25l25 08:21 '1.5 107.45
03125125 08:22 23.899 1.4 107.38
TOgl25l?5 08:23 1.1 107.32
03125125 08:24 10.9 1.4 107.45
03125125 08:25
oais-ns -0826 ----
23.899 1.4
1.1
107.59
107.{',1 I
03125125 08:27 't.1 107.36
O3l?5125 08:28
- 03/25/25 0829
23.900 I't0.8 '1.4 107.63
1.1 107.7A
O3n5l25 08:30 23.900 1.1 '107.55
03125125 08:31 1.1 107.57 IOgl25l25 08:32 't.4 107.86
Ogl25l25 08:33 '1o.7 1.4 107.97
03125125 08:34 I10.7 1.4 108.12
Ogl25l25 08:35 23.901 10.7 1.4 '107.89
03125125 08:36 1.1 107.37
03t25125 08:37 23.gOl I10.7 1.5 107.3.t .190
O3l25l?5 08:38 23.S00 1.1 107.04
0U25125 08:39 10.8 1.1 107.93
03125125 08:40 1.4 107.94 I03125125 08:41 10.8 1.1 107.71
$n1l?s 08:42 23.90'l
- OUa5125 OeL+g -----Zeeol
'1.1 107.77
1.1 107.74 IOil25l25 O&4 10.8 1.4 107.60
031251?5 08:45 23.900 1_1 107_56 491
Ogl25l25 08:46 1.1 107_50 I
o3125t25 0A..47 '1.4 107.04
0U25125 08:/18 1.1 107.79
Page 37 of 91
F = Untt otfltne
E = Exceedance
M = Malntenance
T = Out Of Control
Report Generated: 04/ 14 / 25 06:2L
GP043AS-052980-RT-1881
C = Calibration
S = Substltuted| = Suspect
I
I
I
I
I
I 03125125 08:.19
Average Data - Run 1
Plant: HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 08: 1 1 Through 0312512025 10:24
Time Online Criteria: 1 minute(s)
23.808 ',10.8 1.4 '1o7.76
OSt25l25 08:50 1.4 107.87
03125125 08:51 1.1 107.90I03125125 08:52 10.7 1.4 107.74
03125125 08:53 10.7 1.1 107.71
03125125 08:il 10.7 1.4 107.70t03125125 08:56
I 03125125 08:58 10.8 1.4 107.35
03125125 08:59 10.8 '1.1 107.37
031251?.5 09:00 10.8 107.91I03125125 09:01 10.8 1.5 108.27
03125125 09:02 23.899 10.8 't08.78
03125125 09:03 10.7 1.4 108.87Iou25l25 09:04 'to.7
Ogl25l25 09:05 1.4 108.24
03125125 09:08 10.7I03125125 09:07 1.4 108.42
03125125 09:08
I 03125125 09:09 10.8 1.4 108.42
03125125 09:10 10.8 1.4 '108.51
031?5125 09:'l l 10.8 1.4 108.64
I 03125125 09:12 23.90'l '1.1 108.6 t
03125125 09:'13 23.901 10.8 1.1
03125125 09:14 10.8 1.5 108.24
I 03125125 09:15 't.4
03n5125 09:18 23.901 1.4 108.21
03125125 0e:17 t0.8 1.4
I 03125125 09:18 1.4 108.0r1
ou25l25 09:19 23.899 r0.8 11 108.34
03125125 09:20 !0.8 lt 108.73
I o3125t25 05"21 '10_7 1.4 108.75
03125125 09'.22 23.898 't0.6 t.5 108.27
03125125 O9:23 t.5 108.05
I Ogl25l25 09:24 23.897 1.1 r08.28
OU25l25 09:25 23.857 to.7 t.4
03125125 09:26 't0.7 1.1 108.65I03125125 09:27 23.897 't0.7 1.4 108.86
03125125 09:28 10.7 1.4 '108.83
03125125 09:29 23.896 1.410.7 108.93
Page 38 of 91
I
I
t
F = Unit Offline
E = Exceedance
M = Malntenance
T = Out Of Control
Report Generated: 04/14125 06:21
GP043AS-052980-RT-1881
C = Calibration
S = Substltuted
r = Suspect
03125125 09:30
Average Data - Run 1
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 08: 1 1 Through 0312512025 10:24
Time Online Criteria: 1 minute(s)
10.6 '1.4 108.88
I
I
I481
Ogl25l25 09:31 1.4 r08.56 4U
03125125 09:32 10.6 1.4 107.52
03125125 09:33 10.7 1.5 107.68 I03125125 09:34 23_895 1.4 107.A1
03125125 09:35 10.8 1.5 108.08 457
03125125 09:36 t0.8 't.5 108.30 I03125125 09:37 1.5 108.55
03125125 09:38 10.8 't.5 108.53
OSl25l25 09:39 1.5 108.48 IOgl25l25 09:40 r0.7 1.4 108.63
03125125 09:41 1.1
Ogl25t25 Og:42 1.4 't08.69 IOgl25l25 09:43 11 108.54
Ogl25l25 09:rl4 't.4
03125125 09:45 1.1 I03125125 09:48 10.8 1.4 108.54 187
03125125 09:47 23.897 10.8 1.1
03125125 09:48 I491108..101.4
03125125 08:,tg 23.857 10.8 1.4 108.63
03125125 09:50 23.857 10.7 1_4
03125125 09:51 11 T501108.30
03125125 09:52 10.8 1.4 108.42
03125125 09:53 23.895 10.8 1 ./t t03125125 O9:54 10.7 1.4 't08.58 481
03125125 09:55 23.895 10.7
03125125 09:58 11 108.47 I03125125 09:57 23.894 10.6 1.4
03125125 09:58 1.t 107.85
Ogl25l25 09:59 23.894 10.7 1.4 108.07 I03125125 10:00 1.4 108.10
Ogl25l25 10:01 10.8 't.4 108.35
03125125 10:02 23.894 '10.8 1.4 I03125125 lO:O3 10.7 1.4 108.79
03125125 10:04 23.893 10.7 1.4 108.57
03125125 10:05 10.7 1.1 108.45 I03125125 10:06 23.89.1 10.7 1.4 108.23
03125125 10:07 1.4 108.10
03125125 '10:08 1.4 108.38 I03125125 10:09 23.893 1.4 108.7210.8
108.77
Page 39 of 91
03125125 10:10 1.4
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 04/ 74 I 25 06:21
GP043AS-052980-RT-188 1
C = Calibration
S = Substitutedt = Suspect
I
I
I
I
I
I 03125125 10:'l l
Average Data - Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 08:11 Through0312512025 10:24
Time Online Criteria: 1 minute(s)
23.893 10.8 1.1 108.89
03t25t25 10'.12 1.5 109.00
OU25l25 10:13 23.893 10.8 1.6 108.93I03125125 10:14 t.5 108.93
03125125 10:15 23.492 10.8 1.4
03125125 10:16 23.492 t0.8 1.5 'to9.91IOgl25l25 '10:17 23.892 11 1 10.13
03125125 10:18 'l.4 109.91
03125125 10:19 10.8 1.4
1.4t03125125 10:20 10.7
03125125 'lO:21 10.7 1.4
03125125 10:22 10.7 1.1 109.94
1.4I03125125 10:23 10.7 110.07
03125125 10:24 10.7 '1.4
I
T
I
I
I
I
I
t
I
t
I
T
Avefage
Minimum
Marimum
Summation
Goometric M6an
lncluded Data Point3
Total numbar of Data
P^inta
23.897
23.891
23.901
3,202.249
134
1U
10.8
10.6
10.9
1,442.6
1.4
1.4
1.6
't89.7
108.21
106.71
't 10.13
14.500.42
491
477
506
05.856
1y
'lu
1U
1U
134
1
1U
134
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Contro!
Report Generated: 04/ 1,4 | 25 06:2t
GP043AS-052980-RT- 1881
C = Calibration
S = Substltuted
* = Suspect
Page 40 of 91
Average Data - Run 2
Plant: HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 1 0: 57 Through 0312512025 13: 10
t
I
I
I1.4
Solrce
03125125 10:57 r09.78
Time Online Criteria: 1 minute(s)
UNITl
BARPRESS
(INHG)
co2
(PCT'I
OPACITY
lPCT)
STKTEMP/NEAE\UNITLOAD/t r)
03125125 10:58 1.4 109.49
Ognsn5 10:59 '10.8 1.5
03125125 11:00 23.882 I1.6 109.59
03125125 11:01 10.8 '1.5 109.59
0U25125 11:02 1.4 109.75
03125125 1 1:03 23.88't I1.4 109.82
OU25l25 11:04 109_51
03125t25 1 1:05 I1.1 109.54
OU25l25 11:06 1.1 109.89 152
O3nil25 11:07 1.410.8 109.76
03125125 11:08 1.1 109.57 I0U25125 1l:09 '1.5 109.60 490
03125125 11:10 10.9 1.4 109.77
03125125 11:11 I1.4 110.13
03125125 11:12 10.8 1.1 110.26
Ogl25l25 11:13 23.879 1.4 '110.il
I1.4
1.410.8
10s.7723.879
biTs
Ogn5l25 '11:14
Ogl25l25 11:16 1.1
03125125 11:17 10.8 I1.4 109.71
03125125 11:18 23.879 1.110.9
l1:19 1.1
O3n5l25 11:20 23.879 I1.410.9 109.71
03125125 1'l:21 1.1
03n5l25 11:22 23.874 1.1 10s.50
03125125 11:23 t1.4
03125125 1'l:21 10.9 1.5 109.70
03t25125 11:25 23.877 1.110.9 110.30
03125125 11:2A I1.410.9 1 lO..ts
03t25t25 11..?7 23.877 1.4 110.38
03125125 11:28 1.410.8 110.30
03125125 '11:29 23.876 I'1.4 110.16
I 1:30 1.1
OU25n5 1l:31 10.8 1.4 110.32
Ogl25l25 11:32 23.875 I1.1
10.8
110.12
Page 41 of 91
03125125 1'l:33 1.4'to_8
O3nSl25 11:34 23.875 1.1
F = Unat offlane
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 04h41 25 07 :aO
GP043AS-052980-RT-188 1
C = Callbration
S = Substituted
* = Suspect
I
I
I
I
I
I 1 1:35
Average Data - Run 2
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: 031 25 I 2025 1 0: 57 Th rou g h O3l 251 2025 1 3: 1 0
Time Online Criteria: 1 minute(s)
23.874 10.7 1.5 109.93
1 1:30 23.874 1.410.7 1 r0.05
11:37 23.873 10.7 1.4 109_95
'110.031.410.7I1 't:38 23.873
I 1:39 23.873 t0.7 1.4
t.410.7l1:40
109.361.410.7I11:11 23.471
1.410.7l1:42
1 'l:43 1.110.7 109.35
1.4t10.711'.U
1.410.7'l 1:.15
1.410.71 l:48
109.451.4I11147
1 l:48 1.5
11:49 't.5 10s.12
1.4I1 1:50 23.871 10.9 108_77
'l 1:51 '1.4
1.111.0I11:52 23.871
1 1:53 1.4 t08.71
23.870 't.411.2 109.10
1.4I1 l:55
1.111.2 't09.9
11:57 1.1 t09.33
't09.141.5'11.2I1 1:58
109_37't.511.2
12:00 1.5 109.79
t09.801.5I12:O'l
12:O2 1.1
12:03 1.5 !09.96
1.5I1?:U
12.O5 23.868 '1.511.2 109.78
12:00 23.868 1.5't't.'l 109.63
'109.69't.511.1I12:07
12:Og 23.868 't.511.2 109.79
12:09 1.511.2 109.86
1.511.2I12:1O
23.866 1.511.2 109.93
12:'12 '11.2 1.5 110.07
1.5I12:13 23.866 110.24
12'.11 1.511.1 1 10.14
Page 42 of 91
1?.'15 23.4e7 't.51t.rI
I
I
F = Unit Offline
E = Exceedance
M = Malntenance
T = Out Of Control
Report Generated: 041 L4/ 25 07 :4O
GP043AS-052980-RT- 188 1
C = Calibratlon
S = Substitutedi = Suspect
o3t25t25 12tA
Average Data - Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period : 031 251 2025 1 0: 57 Th roug h O3l 251 2025 1 3: 1 0
Time Online Criteria: 1 minute(s)
23.866 11.1 1.5 109.80
I
I
I03125125 12:17 1.5
03125125 12:18 11.2 '1.5
tt.5 I 10.13
1.5 110.10
12:21 11 .1 '1.5 109.98
03125125 '12:22 1.5 109.92 I12:23 1.5 109.93
03125125 12:24 11.2 1.5 I'12:25 11.2 't.1
Ogl25l25 12:28 1.411.2 109.62
03nil25 12:27 1.111.2 110.02 I1.111. t 110.39
110.40't.511.112:29
03125125 12:30 23.865 1.51'.t.'l 110.17 I1.511.1 1 to.t4
1.511.112:32 110.34 495
03125125 12:33 23.4U '1.5t1.t 110.20 I1.511.1 1't0.87't2:u
03125125 12:35 'L51 1.1
t1.41t.t 1 I 0.6612:36 23.863
1 1 0.20't.111.112:37
12:38 23.863 1.1 110.06
I1.1'11.2 110.2912'.39 23.562
Ogl25l25 12:40 1.411.2 110.8 t
23.4ts2 1.111.2 110.91
03125125 12:42 I1.411.1 110.36
1.4'l1.112:43 23.801 1 t0.13
03125125 12:4 23.861 1.11 1.1 110.28
12:45 23.860 I'1.4'I 1.1 110.U 489
12:44 1.111.1 110.41
Ogl25l25 12:47 1.51 1.1 110.14
I1.511.112:48 I 10.1523.880
1't0.171.511.1'12:49
12:50 23.859 1.5 t 10.54
o3t25t25 12..51 I1.111.2 1 10.80
03125125 12:52 1.1 1't0.79
1.511.012:53 23.858 't10.75
03125125 12:54 I1.411 .0 I 10.67
1.41 2:55 23.856
Ogl25l25 12:56 1.1 111.27
Page 43 of 91
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generate d: 04 h4 / 25 07 :4O
G P043AS-052980-RT- 188 1
C = Calibration
S = Substituted
* = Suspect
I
I
I
I
I
I o3125t25 12'.57
Average Data - Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : 031 25 I 2025 1 0 : 57 Th rou g h 03 I 251 2025 1 3: 1 0
Time Online Criteria: 1 minute(s)
23.855 10.8 1.4
03125125 t2:58 23.855 1.5 1 10.82
O3125t25 12:59 10.7 11 1 10.80
1.4t03125125 13:00 23.854 10.7 110.43
03125125 13:01 to.7 l4 109.94
03125125 13:02 23.853 1.4 1 10.06
1.1T03125125 13:03 1'to.75
03125125 13:04 1.4 't 10.50
Ogl25l25 13:05 14 110.14
1.4I03125125 13:06 109.97
03125125 13:07 23.851 1.510.8 1t0.o5
Ogl25l25 13:08 1.510.9
1.510.9I03125125 13:09 110.83
03125125 13:10 't.5'10.9
t
I
I
I
I
I
I
I
I
I
I
I
Av€rage
Minimum
Maximum
Summation
Gsornetric Mean
lnclud6d Oata Points
Total number of Dala
P^i^tc
23.868
23.850
23.883
3.198.348
11.0
10.7
11.2
1.423.7
1.4
'1.4
1.0
'192.8
10s.98
104.71
111.27
14,737.32
494
$2
505
46,142
134
't34
134
1
130
'tu
134
134
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 04/74/25 07:4O
cP043AS-052980-RT-1881
134
134
C = Calibration
S = Substituted
* = Suspect
Page 44 of 91
Source
03125125 13:53
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 1 3: 53 Through 0312512025 16 12
11.0 1.5
I
t
I
I
Time Online Criteria: 1 minute(s)
UNITl
BARPRESS
(INHG)
co2
(PCT)
OPACITY
TPCT\
STKTEMP
(DEGF)
UNITLOAD(m/o
03125125 13:54 1 t.0 1.1 110.?2
03125125 13:55 11.0 1.4 1 r0.52
03125125 13:56 1 1.0 1.1 'l lO.8/t t
O3lZSl25 13:57
03125125 13:58 23.A32 10.9 1'1o.12 I03t25125 13:59 23.833 1.4 110.21 t93
03125125 l4:0o 10.8 1.1 110.38
03125125 14:01 1.4 1'10.46 IOU25t25 14:02 1.4 110.32
03125125 1/+:03 10.7 1.4 I 10.10
o3125t25 14..U 23.831 10.7 1-1 1 10.00 I03125125 14:05 10.7 1.4
1.4 1 10.54
03125125 11:07 23.829 1.1 t l 0.63 I03125125 14:08 1.4
Ognilz1 14:09 10.5 1.5 't10.27
03125125 '14:'10 23.829 1.1 109.98 TOU25l25 11:11 1.1
03n5n5 fi:12 23.830 10.5 1.1 110.25
$n5125 14:13 I4871.4
03125125 11:11 23.825 1.4 110.06
$nSnS 14:'15 10.7 1.4 110.08
Ogl25l25 1.1:18 10.7 '1.1 110.02 I03125125 11:17 10.7 1.4 109.73
03125125 14:18 10.7 '1.4
03125125 14:19 1.1 IO3l25nS l:2O 1.1 100.50
03125125 14:21 10.7 1.4 109.53
03t25125 14i22 '1o.7 1.1 IOgl25l25 11:?3 10.7 1.4 109.91
0U25125 11:24
--- ost2sizs_-Tq;N
10.7 1.5 110.22
110.12'1o.7 1.1 Io3t25t25 142A 10.7 '1.4 '110.37
03125125 14:27 10.7 1.1 I10.31
OU25n5 fi:28 1.4 '110.25 I03125125 11:29 .l.4 1 t0_4010.6
110.35
Page 45 of 91
l4:30 1.4
r = untf UIIllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated 04/ L4/ 25 07 :aL
GP043AS-052980-RT- 188 1
C = Calibration
S = Substituted
* = Suspect
I
I
I
I
I
T 03125125 11:31
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 031251202513:53 Through 0312512025 16:12
Time Online Criteria: 1 minute(s)
23.828 10.6 1.1 110.33
0u25t25 14'.32 23.428 10_6 1.4 110.24
03125125 14:33 23.827 1.4 110.21I03125125 14:?1 10.7 1.4 110.4
Ogl25l25 '14:35 23.827 10.7 1.4 1't0.49
03125125 14:36 23.827 '1o.7 1.4 1 10.50I031?5125 14:37 10.7 11 110.49
03125125 14:38 23.826 10.7 1.4 110.52
03125125 14:39 11 1r0.62
1.4IOgl25l25 14:40
03125125 14:41 10.6 11 110.48
03125125 14:12 10.6 1.4I03125125 '14:43 10.6 1.4 110.58
03125125 14:44 1.4 110.67
03125125 14:45 1.4 't 10.50I03125125 14:46 1.4 t 10.40
03125125 14:17 23.824 1.1 110.49
I 03125125 14:48 23.824
03125125 14:49 23.824 10.6 1.1 111.19 483
10.6 1.4 110.91 484
Ogl25l25 '14:50 10.5 1.4 1't 0.63
I 03,125125 t4:51 10.5 1.4 110.28
03125t25 14.52 23.826 'to.6 '1.4 110.24
03125125 14:53 10.6 1.4 110.68
I 03125125 14:54 23.826 1.4 110.86
03125125 14:55 10.7 1.4 1'10.57
03125125 14:56 10.7 1.5 110.71
I Ogl25l25 14:57 23.A25 10.6 1.5 1 11.36
03125125 14:58 10.6 1.5 1 11.30
03125125 14:59 10.5 1.5 1 11.41
I 03125125 15:00 10.5 1.5 1r 1.58
03125125 15:0'l t0.5 t1 111.52
Ogl25l25 15:02 10.5 l1
'1.4I03125125 15:03 10.5 111.33
03125125 15:04 t0.6 t.4 111.2',1
03125125 15:05 1.4 'l 1 1.39IOgl25l25 15:06 10.7 't11.62
ogl25l25 15:07 10.7 1.4
OJl25l25 15:08 10.7 1.4 1',t'1.20
1.5I03125125 '15:09 10.7
03125125 15:10 23.421 10.7 1.4 'l to.78
Ogl25l25 1 5:'l 1 1.410.7 110.77
Page 46 of 91
t
I
I
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generate d: 04/ 74 I 25 O7 :a7
GP043AS-052980-RT- 1881
C = Callbration
S = Substituted
* = Suspect
15:12
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0312512025 1 3: 53 Through 031251 2025 16 12
Time Online Criteria: 1 minute(s)23.824 10.7 t.4 'I 11.04
I
I
I15:13 10.7 1.5 1 11 .08
15:14 t.4 1 r0.75 I15:15 10.7 1.4
1.4 110.46 495
10.8 1.4 110.78 I1.123.823
'15:19 1.4 11 1.'10
15:20 10.7 1.1 1 10.54
23.823 10.7 1.4 110.83 486 I15:22 23.823 10.7 1.1 I 1 0.55
15:23 23.822 10.7 1.1 110.44 490 I
'15:26 23.821 1.1 110.83 429 I/tl915'.27 10.8 1.5
15:28 10.7 1.5 'l11.63
15:29 '1.1 1 10_70 481
15:30 1.4 110.86 471 I
15:31 23.819 1.4 1 10.61
23.820 10.5 1.4 109.78
15:33 10.6 1.1 110.27 I
l5:34 23.819 10.7 1.4 1 r 0.32
15:35 '10.8 11 r r0.23
23.818 10.8 I1.4 110.45
'15:37 23.818 'to.8 11 1 10.70
l5:38 23.817 10.7 I1.tl 1 10.64
23.417 10.7 1.4 'flo.50
15:4O 1.1
l5:41 23.817 I1.4 110.30
10.7 1.1 1',t0.26
23.816 10.7 '1.4
23.816 10.7 I1.1 109.81
23.8't6 't0.7 1.1 r09.77 458
23.815 'to.7 1.4 10s.92
I1.410.7
23.816 10.7 1.4 110.01
23.81 5 't0.7 11 1 10.03 471
I1.4 1 r0.0623.815
23.8't 5 1.1 't't o.1s
Page 47 of 91
23.81 5 1.4
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Contro!
Report Generated: 04h4125 07 :4t
GP043AS-05298o-RT- 1881
C = Calibration
S = Substituted
* = Suspect
I
I
I
I
I
I '15:53
Average Data - Run 3
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period : 03 I 251 2025 1 3 : 53 Th rou g h 031 251 2025 1 6: 12
Time Online Criteria: 1 minute(s)
23.815 10.8 1.4 1 10.15
15:il 23.81 5 10.9 '1.4 110.13
23.815 '1.4 t 10.46
15:56 23.415I 1.4 110.71
1 5:57 23.815 'l.1
1 5:58 23.815 10.7 1.1 't'11.57II 5:59 23.8't4 10.5 1.4 111.26
't.4 1'.11.O7
23.81 3 1.4 110.45I23.813 95 i
- ---__- 1t,; I
1.4
---li
110.27
irozo23.813
23.813 't.4 110.03
109.8t1.4I
23.813 10.4 1.4 10s.72
10.5 1.5 't09.95 447
1.4It0.523.813
'1.4 1 1 0.5r1
1.4tt0.516:10 ?3.813
16:1 I 't.4 1 10.35
'!.6:12 1.1 il0.33
I
I
I
I
I
I
I
I
I
I
Awrage
Minlmum
Maimum
Sumrnatiof,
Gsometric Mean
lncludsd Data Points
Total numb€r of Data
pdnta
23.423
23.813
23.833
3.335.220
10.7
10.4
'I 1.0
1.450.4
1.1
'1.4
1.5
197.4
1 1 0.50
109.50
111.63
15,469.97
477
419
506
64.827
140
140
140
'140
136
140
140
140
140
140
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: O4l 74/ 25 07 :4L
GP043AS-052980-RT-1881
C = Calibration
S = Substituted| = Suspect
Page 48 of 91
Appendix 8.2
Unit 2
I
I
I
I
t
Average Data - Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period : 031 27 I 2025 09: 06 Th roug h 031 27 I 2025 1 1 :22
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
03127125 09:06
UNIT2
BARPRESS
(tNHG)
co2
(PCr)
UI.AUI I Y
(PCT)
UIAIEMP
(DEGF)
UNI I LOAU
(tfv9
23.697 I 0.9 106.14
03127125 09:07 0.71 t.5
0312712.5 09:08 23.898 0.711 .5 108.1 I
0.711 .6IOgl27l25 09:09 106.48
03n7125 09:10 23.697
Ogl27l25 09:11 0.7'l 1.6 106.45I03127125 09112
0U27125 09:'13 o.711.8 106.31
OU27n5 09:14 0.811 .6
1 t.6IOgl27l25 09:15
Ogl27l25 09:16 1r.6 tw.25
03127125 09:17 I 1.6 100.55
106.560.7I 1.5IOg27n5 09:18
0U27125 09:19 0.7't 1.5
Ogl27l25 09:20 0.7't1.5
0.91 1.5IOSl27l25 09:21 23.699
03127125 00:22 23.699 t.o'l 1.5 106.55
1 1.5
11.5I03t27t25 09'.21 23.699 0.9 100.87
03127125 09:25 0.711.5
03127125 09:28 0.711 .5 107.05I0U27125 09:27 23.698 107.05
0U27125 09:28 0.6 106.38 1A2
o.7I03127125 09:29 23.657 104.06
03127125 09:30 23.696 t1.0 104.06
Ogl27l25 09:31 0.71 1.6
I OU27l25 09:32
03127125 09:33
Ogl27l25 09:34
t 03127125 09:36 11.7 0.7
031271?5 09:37 11.7 0.7
I 03127125 09:38 1 t.8 106.73
03127125 09:30 11 .8
03127125 09:40 1 1.6
10a.71
Page 50 of 91
I 03127125 09:41
03t27t25 F9,SrCeedan6923.696 o.7t
I
I = lnvalld
M = Maintenance
Report Generated: 04/74/25 07:42
GP043AS-052980-RT- 188 1
l, - uailoraflon
S = Substituted
T = Out Of Control
Average Data - Run 1
Plant: HUNTINGTON PIANT
lnterval: 1 Minute
Type: Block
Report Peri od : 031 27 I 2025 09 : 06 Th roug h 031 27 I 2025 1 1 :22
Time Online Criteria: 1 minute(s)
11.4 0.6
I
I
I
03127125 09:44 107.'t 3
Ogl27l25 09:45 11.1 I
0U27nS 09:48 11 .4 106.92
o3t27t25 09..17 11.4 0.6
03127125 09:48 't 1.5 I
03127125 09:40 11.5
Ogl27l25 09:50 11.5 o.7 I03127125 09:51 23.694 0.6
03127125 09:52 23.684 'l 1.8
03127t25 09:53 23.694 0.6 'to8.75 IOgl27l25 09:54 o.7 r06.34
03127125 09:55 'I 1.5 0.6 104.94
03127125 09:50 23.6U I03127125 09:57 0.7 103.76
03127125 09:58 11.6
031271?5 09:59 0.6 103.59 IO3lZ7l25 10:00 11.6 0.6 t03.50
03127125 10:0'l 23.692 11.8 0.6 't03.72
Ogl27l25 10:02 23.693 1 1.6 0.6 t03127125 l0:03 1 1.8 't03.68 441
03127125 10:04 23.693 1't.6
OSl27l25 1O:O5 103.18 IOgl?7125 10:06 1 1.6 102.91
03127125 10:07 11.0 102.78
03127125 10:08 1't .6 0.6 103.10 IO3t27125 10:09 23.691 1 t.0 103.48
03127125 '10:10 11.0
03127125 10:11 23.691 11.6 105.e6 I03t27t25 10"12 106.01
03127125 10: 1 3 23.691 11.5
03127125 '10:14 o.7 1 06.32 I0U27125 10:15 23.690 t't.5 t06.23
Ogl?7125 10:18 11.5 0.7 106.32
03127125 10:17 1 1.5 I03127125 10:'18 23.689 11.5
0U27125 10:19 1 t.5 o.7 r06.62
03127125 'lO:2O 23.688 1 1.5 0.7 106.58 IO3t27t25 10121 23.689 11.5 o.7
03t27t25 10:22 23.689 11.5 0.7 108.59 480 I
I = lnvalid
M = Maintenance
Report Generateil O4l L4/25 07.42
GP043AS-052980-RT- 1881
C = Calibration
S = Substltuted
T = Out Of Control
I
IPage 51 of 91
I
I
t
Average Data - Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : 031 27 I 2025 09: 06 Th rou g h O3l 27 I 2025 1 1 :22
Time Online Criteria: 1 minute(s)
23.688 1 1.5 0.603127125 '10:25 107.13
11.5Iogl27l25 10:28 107.16
03127125 10:27 o.7I 1.5 107.28
ogl27l25 10:28 23.687 1 1.5 't 07.16
11.5I03127125 10:29 107.07
03127125 10:30 23.687 11.5 10a12
11 .5IOgl27l25 10:31
03127125 10:32 't1.5
03127125 10:33 11.5
103.75t't .8I03127125 10:34
03127125 10:35 23.080 1't.6
03127125 10:36 1 1.6 103.72
11.6I03127125 10:37 23.685
Ogt27l25 '10:38 1 1.6
03127125 10:39 23.6821 11.6
103.86o.71 1.6Iogl27l25 10:/t0
03127125 10:41 'I 1.6
03127125 10:42 0.61 1.6
4611 1.6I03127125 10:43
03127125 10:14 23.681 4010.61 1.6 103.81
03127125 10:45 't 1.6 105.17
1 1.6I03127125 10:46 461
03127125 10:17 23.478 I 1.6 107.O2
OU27l25 1O:,+8 23.674 0.61 1.5 107.19
11.5IOgl27l25 10:,19 107.38
03127125 10:50 23.477 0.811 .5 107.24
03127125 10:51 11 .5
0.011.1I0'3127125 10:52 107.03
03127125 10:53 23.474 0.6
03127125 10:il 11.4 107.11
0.61 1.5IOgl27l25 10:55 107.15 rt61
0U27t25 10:56 23.674 0.6
03127125 10:57
0.6IOil27n5 10:58 't07.o2
93127125 10:59 1't.5 107.03
OSl27l25 1 1 :0O 0.7'l't.5 107.06
0.711.5IO3n7l25 t 1:01 107.24
03127125 1'l:O2 11.5 107.42
03127125 l l :03 0.611.4 107.63
0.7I
I
t
03127t25 1 l:04
03t27125 11
11.1
I = lnvalid
M = Maintenance
Report Generated: O4l 74/ 25 07 :42
GP043AS-052980-RT-1881
C = Calibration
S = Substituted
T = Out Of Control
11.4
107.52
Page 52 of 91
Average Data - Run 1
Plant: HUNTINGTON PIANT
lnterval: 1 Minute
Type: Block
Report Period: 0312712025 09:06 Through 0312712025 11:22
Time Online Criteria: 1 minute(s)
1',1.4 0.6
I
I
I
03127125 I'l:06 107_63
03127125 '11:07 11.1 107.60
03127125 1 1:08 1'1.4 107.49
03127125 'l 1:09 11 .5 107.50
03127125 '11:10 I11.5
Ogl27l25 11:'ll o.511.5 107.70
03127125 11:12 I441t 1.5 107.55
03127125 1 l:13 1 1.5 107.17
03127125 11:14 11.5 107.42
O3l27l?5 11:15 I4530.511 .4 106.52
03127125 11:'16 45211.4 104.89
0Xl27l?5 11:'17 o.51't.4 'to1_77
Ogl27l25 11:18 I0.61 l.5 104.70
03127 125 't 't ; 1 I 0.611.5 't04.46
0U27125 11:20 o.611 .5 104.34
0U27t25 11:21 I0.6 104.17
o3t27t25 11..22 0.6 1O'1.03
A\rerage
Minimum
Matimum
Summation
lncluded Data
P^i^ta
Total number of
nrtr D^i^ta
23.086
23.060
23.699
3,245.021
11 .5
11.4
'11.7
1,579.2
105.88
102.78
'1o7.70
't4,504.89
137
137
460
452
447
03,024
137
157
157
't37
137
'137
0.6
0.5
1.0
88.1
C = Calibration
S = Substituted
T = Out Of Control
t
I
I
I
I
I
I
I
I
I
137
137
F = Unit Offline
E: Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04 | l4l 25 07 t42
GP043AS-052980-RT-1881 Page 53 of 91
I
I
I
I
Average Data - Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : O3l 27 I 2025 1 2 : 45 Th rou gh O3l 27 I 2025 1 5:0O
Time Online Criteria: 1 minute(s)
So:rce
Parameter
(Unit)
o3t27t25 '12..15 0.511.4 107.57
UNIT2
BARPEESS
(INHG)
c02
(Pcr)
OPACITY
(PCT)
S'TKTEMP
(DEGF)
UNI I LUAL'
(r{w)
03127125 12:46 0.511.1 106.73
105.570.511.4IOgl27l25 12:17
03127125 12:48 0.51'1.1 105.12
03127125 12:19
I 1.5I0U271?5 12:50
03127125 12:51 23.619 105.46
03127125 12:52 11.5
11 .5I03127125 12i53 23.618 105.79
O3n7l25 12:*0.5ll.5
03127125 12:55 23.417
't 1.5Iog27n5 12'.8 0.5 105.21
03127125 '12:57 23.6',t7 1 1.5 105.04
1'1.5I03127125 12:58 0.5 105.25
03127125 12:59 23.616 11 .5 105.4S
0U27125 13:00 11 .5 0.5 105.9e
1 t.5IOgn7l25 13:01 r07.36
03127125 13:Oz 23.614 0.5 107.90
03127125 13:03 23.613 11.4 107.80
0.5
11.1IOgl27l25 13:04
03127125 13:05
23.411
23.6't0
107.74
't07.86
03127125 13:06 0.511.4 1 07.79
0.51'1.1I03127125 13:07 107.78
03127125 13:08 23.008 11.4 401
OSl27l25 13:09 23.807 0.511.1
I 03127125 13:10
03127125 13:11 11.4 108.15
03127125 13:12 0.511.1 108.18
0.511 .4I03127125 13:13 104.12
Ogl27l25 13:14 0.5'l 1 ./t
Ogl27l25 '13:15 11.4 108.13
0.511.4I03127125 13:16 '108.15
Ogl27l25 13:17 11.4 108.15
03n7125 13:18 11.4
11.4I0U27125 13:19 108.10
Page 54 of 91
03127125 13:20 11.1
03127t25 ',t3"z'l 23.599 0.5'11.4
1'l.1Io3t27t25F Jtifnit offrinett uo'
I
I
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4/L4125 07:a2
GP043AS-052980-RT-1881
C = Calibration
S = Substltuted
T = Out Of Control
03127125 13:23 23.601
Average Data - Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 031271202512:45 Through 0312712025 15:00
Time Online Criteria: 1 minute(s)
0.5 108.05
I
I
I
03127125 13:24 23.599 1 1.5 0.5 108.05
03127125 13:25 23.598 1 1.5 0.5 108.03 IO3127t25 13:26 23.597 'l 1.5 0.5 107.52
03t27t25 13..27 1 1.5 0.5 107.88
0u27t25 '13..28 I4610.5 108.06
03127125 13:29 1't.5 o.5
03127125 13:30 0.5 10€.93
03127125 '13:3'l 23.589 11.4 0.5 I03127125 13:32
03127125 13:33 23.588 11.4 0.5
O3l?7125 13:34 IOU27l25 '13:35 105.57
03127125 13:36 105.20
03t27125 '13:37 23.586 '11.1 o.5 104.97 I03127125 13:38 104.75
Ogl27l25 13:39 11.5 1 04.87
Ogl27l25 13:40 23.582 'l 1.5 0.5 1 05.07 I03127125 13:41 23.581 105.?7
03127125 13:42 23.580 11.5 0.5
03127125 13:43 23.579 11.5 107.01 I03127125 13:44 23.579 0.5 't07.47
03127125 13:45 23.578 11.5 0.5
03127125 '13:46 23.578 0.4 108.10 IOgl27l25 13:47 11.1 1 08.02
03127125 13:t+8 23.577 11.1 0.4 107.87
03127125 13:49 I11.4 0.5 107.75
03t27125 13:50 11.4 107.74
03127125 13:51 23.576 11.4 0.5 107.92
03127125 13:52 I1'1.4 '107.98
03127125 13:53 23.574 1',|.1 107.U
03127125 13:54 1'1.4 1 08.1 3
o3t27125 13:55 23.575 I't1 I 1 08_28
03lZTl25 13:56 23.575 11.4 0.6 I 08.23
0U27125 13:57 11.4
03127125 13:58 23.575 I11.4 0.5
03127125 13:59 1'1.1 461
03127125 14:00 2?.571 11.4 0.6
Ogl27l25 14:01 25.575 I11.4 0.0 r08.78
Page 55 of 91
03127125 14:02 11.t
03127125 14:03 IF = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated: 04/74/25 07:42
GP043AS-052980-RT- 188 1
C = Calibration
S = Substituted
T = Out Of Control I
I
I
I
I o3t27t25 11:U 23.575
Average Data - Run 2
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Peri od : O3l 27 I 2025 1 2: 45 Th rou gh 031 27 I 2025 1 5:00
Time Online Criteria: 1 minute(s)
'11.4 0.5 r08.92
O3l?7125 14:05 25.576 11.1 109.03
11.1I03127125 14:06 23.575 108.76
03127125 14:07 0.511.4 108.64
03127125 14:08 23.574 0.51'.t.1 108.85
11.1I03127125 14:09 23.572 0.5 109.02
03127125 14:10 ?3.572 108.90
Ogl27l25 11111 23.572 11.4 0.5 't08.54
I 03127125 14:12 23.57'l 107.98
0U27125 14:13 23.570 0.5 106.71
03127125 14:'14 0.51 1_5 105.79
0.5I03127125 14:15 23.547 '105.73
03127125 14:16 1 1.5 105.70
03127125 14:17 23.586 0.5
0.511.5I0,3127125 14:18 105.39
03127125 14:19 23.560 r05.r4
03127125 14:20 1't.5 105.OO
0.4I0u27t25 14'21 23.506 105.42
03127125 11:22 23.560 1 1.5 105.54
03127125 11:23 23.500 0.511.5 r05.59
11 .5IOU27l?5 14:24 107.31
03127125 11:25 23.566 0.51'1.4 t08.65
Ogn7l25 14:26 11.4 1 08.41
0.511.4I03127125 14:27 23.566 108.30
Ogl27l25 '14:28 23.547 11.4
03127125 '14:29 t 1.3
0.511.4IOU27l25 14:30 r08.17
03127125 14:31 23.*2 11.1
03127125 14:32 0.511.4
't't.4I03127125 14:33 r08.25 459
03127125 ',t4..U 11.4
03127125 14:35 23.558 1'.t.4
46111.4I03127125 14:36 108.20
o3127t25 ',t1..37 0.51 1.4 108.14
0s127t25 1/t:38 23.557 't 1.4 108.17
0.511.1I0'3127125 14:39 23.557
Ogl27l25 '14:40 23.556 108.35
0.5t03127125 14:41 23.558 1 08.1 9
03127125 14..42 23.557 108_12
03127125 14:43 23.557 0.51't.4 108.19
0.511 II03127125 11:11 23.558 108.29
Page 56 of 91
I
I
F = Unrt unilne
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4174/25 O7:42
GP043AS-052980-RT-1881
C = Calibration
S = Substltuted
T = Out Of Control
Average Data - Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 031271202512:45 Through 0312712025 15:00
Time Online Criteria: 1 minute(s)
'11.1 0.4
I
I
0u27t25 '14'.15
o3t27125 1!'AA 108.53
I0.511.403t27t25 14..17
03127125 14:48 108.31
03127125 14:49 23.557 0.511.4
Ogl27l25 '14:50 23.558 108.'14 I03127125 11:5'l 23.558 1',|.4 108.05
o3t27t25 14'.52 11.1 108_21
03127125 14:53 23.556 I11.4 108.22
03127125 14:U 23.555 0.51'.1.1 107.80
03127125 14:55 23.554 't06.67
03127t25 '14:56 23.553 I0.511.4 105.89
03t27t25 14:57 23.551 0.511.4 105_50
0U27|ZS 14:58 23.551 0.511.4 105.36
I0.511.403127125 14:59
O3t27125 15:00 11.1 105.40
Averaoe
Minimum
Maximum
Summation
lncluded Data
P^inta
Total number of
nrt. hi^te
23.582
23.551
23.624
3,207.r53
1 07.31
104.75
109.05
'14.593.60
11.4
11.3
't1.5
1,554.3
0.5
0.4
0.6
68.9
460
453
408
42,562
I
I
I
t
I
I
I
I
I
I
t
136
136
136
136
r30
'136
136
136
'136
136
F = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated: 04/74125 07:42
GP043AS-052980-RT-1881
C = Calibration
S = Substituted
T = Out Of Control
Page 57 of 91
I
I
I
I
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : Ogl 27 I 2025 1 5: 25 Th rou gh O3l 27 I 2025 17 :35
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
03127125 15:25
UNIT2
BARPRESS
(rNHG)
co2
(PCr)
OPACTTY
(PCr)
STKTEMP
(DEGF)
UNITLOAD
(tYfW)
I
Ogl27l25 15:26 0.511.4IO3n7t25 15:27 23.il2
03127125 15:28 23.512 11.4 0_5
03127125 15:29 23.541 11.4
0_511.4IOSl27l25 15:30 23.540
03127125 15:3'l 23.539 'l 1.3 108.72
0U27n5 15:32 23.539 108.53
1 1.3I03127125 15:33 108.73
03127n5 15:34 23.538 1 1.3 108.70
03127125 15:35 11.4 108.50
0.411.4IOil27l25 15:36 ?3.537 108.88
O3n7l25 15:37
Ogl27l25 15:38 23.W 0.5 105.77
0.511.1I03127125 15:39 105.87
03127125 15:40 23.538 0.5
1'1.1
T
03127125 15:41 105.68
Ogl27l25 15:42 0.511.1
031?7125 15:43
0.511.1IOgl27l25 15:4 23.538 105.49
0U27125 15:45 ?,3.537
0U27t25 15:46 11.4 105.84
11.4I03127125 '15:47 107.56
03127125 15:48 23.535 11.4 108.10
03n7125 15:49 't1.4
0.511.1I03127125 '15:50 23.535
11.1 108.94
03127125 15:52 1 1.3
ll.3I03127125 15:53 23.535 109.13
0U27125 15:54 23.s33 'I 1.3 108.95
03127125 15:55 I 1.3 108.91
1 1.3I03127125 15:56
ouittu --ts:st iis ---23.525 r0s.12
Ogl27l25 15:58 0.511.3 I 08.75
1 1.3I0U27125 15:59 23.5?9 108.74
Page 58 of 91
03127125 16:00 23.528 0.511.3
03127125 16:01t03127125 16:02 23.527F = llnif ()fflina
t
I
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated 04/ L4/ 25 07 :42
GP043AS-052980-RT- 188 1
C = Calibration
S = Substituted
T = Out Of Contro!
Ogl27l25 16:03
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : O3l 27 I 2025 1 5 : 25 Th rou g h 03 I 27 I 2025 17'.35
Time Online Criteria: 1 minute(s)
23.527 11.3 0.6 108.62t
I
I
I
03127125 16:04
03127125 '16:05 23.527 108.64 I03127125 '16:06 108.72
03127125 16:07 108.82
OU27l25 18:08 108.7/t I0U27125 16:09 23.524 0.5 108.75
OU27l25 16:10 23.524 11.3 0.5 108.72
Ogl27l25 16:1 1 23.523 1t .4 I0.5 108.63
03t27t25 1A12 11.3 108.72
03127125 16:13 23.522 11.3 0.5 104.77
OU27l25 10:1.1 23.521 1 't ..1 I0.5 108.79
Ogl27l25 16:15 23.522 11.4 o.5 10,4.77
O3n7l25 16:18 11.3 1 08.56
03127125 18:'17 23.525 11.3 Io.5 107.6S
03127125 16:18 23.522 1'1.3 108.43
03127125 16:19 23.522 11.4 105.90
03127125 16:20 11.4 t0.5
OA27n5 1A:21 23.523 11.1 0.5 106.12
Ogl27l25 16:22 11.1 105.91
03127125 16:23
istzTns rei+-
2e.520 11.1 105.77 I0.511.4 107.00
Ogl?7l25 16:25 23.519 1'1.4 107.47
Ogn7l25 16:26 23.519 I0.511.4
03127125 16:27 11.4 108.40
03127125 16:28 23.521 11 I
03127125 16:29 t0.511.4 I 09.1 5
03127125 15:30 11.1
03127125 16:31 23.526 0.5't'l .3
03127125 16:32 t0.5't1.3 t08.97
03127125 16:33 23.523
ogrzlns - ios4 -_-- -- 2r.5is
11 .3
rr: --0.5 108.67
03127125 18:35 t1't .3
03127125 16:36 23.521 0.511 .3
03127125 18:37 47111.1 108.32
03127125 16:38 23.518 I
03127125 16:39 23.521 470
Ogl27l25 18:40
ouiirN
23.517 It 1.5
1'.1.4
03127125 16:12 23.5',t7 11.1
11.4
108.78
Page 59 of 91
03127125 16:43 23.517 IF = Untt unilng
E = Exceedance
I = Invalid
M = Malntenance
Report Generated: 04/74/25 07:42
G P043AS-052980-RT- 1 88 1
C = Calibration
S = Substituted
T = Out Of Control I
t
I
I
I 03127125 1A:11 23.517
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0312712025 15:25 Through 0312712025 17:35
Time Online Criteria: 1 minute(s)
1r.3 0.4 108.88
03127125 16:45 23.515 o.4I1.3
o.4'l 1.3Iou27t25 16:46 23.519 t09.15
O3l?7125 1647 23.515 1',1.2 l@.21
0,3127125 16:48 23.517 0.411.2 109.29
11.2IOSl27l25 16:49 23.514 109.46
03127125 16:50 23.516 417
03t27125 t6:51 23.516 41411.2 109.14
1'110.4I03127125 10:52 109. t3
03127125 16:53 23.516 'l't.2 109.28 111
03127125 16:54 11.2 108.43
11.'lIogl27l25 16:55 23.515 107.24
03127125 16:56
03127125 16:57 23.518
'I r.1I03127125 '16:58
03127125 t0:59 1't .'t
03127125 17:00 23.514 11.1I03127125 17:01 23.511
Ogl27l25 17:02 23.512 'tl.1
03127125 17:03 23.512 109.3/+
0.4'11.1I03t27t25 17:U 23.513 to9.48
0U27125 17:05 23.5't4 109.78
03127125 17:06 23.515 0.4't 1.0
1't.0IOU27l25 17:07 23.515 109.77
03127125 17:08 23.514 0.41 t.0
O3t27125 '17:09 23.516 0.4 t0s.89
10.9I03127125 17:10 23.51 5 109.57 401
03127125 '17:1'l 23.516 o.4 1 09.1 I
Ogl27l25 17:12 23.516 1r.0 109.20
111IOgl27l25 17:13 23.516
03127125 17:11 23.515 4t30.4 109.35
03127125 17:'15 23.5r5 4151 t.0 10s.12
416o.410.9I0,3127125 17:'16 23.517 109.23
03t27125 17:17 23.517 0.410.9 109.21
03127125 17:18 23.516 41711.0
0.4I03127125 17:19 23.516 108.97
03127125 17:20 23.516 414, 't.0
o3t27t25 ',t7'.z',l.23.516 0.4 109.05
0.61 1.0I 109.0323.515Ogl27l25 17:22
109.05
414
Page 60 of 91
Ogl27l25 17:23 23.51 5 0.4 108.85
I 03127125 17:21 23.511
I
I
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generated: O4h4/25 07:42
GPO43AS-052980-RT-1881
G = Calibration
S = Substituted
T = Out Of Control
03t27125 17:25 23.514
Average Data - Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 031271202515:25 Through 0312712025 17:35
Time Online Criteria: 1 minute(s)
0.4 108.95
I
I
I/tl 5
03127125 17:26 23.51 3 'I 1.0 108.89 416
Agl27l25 17:27 23.51 3 108.86
O3l27l?5 17:28 23.512 11.0 I4'19108.62
Ogl27l25 17:29 23.512 11.0 108.46
03127125 17:30 11.0 104.42 I03127125 17:31 23.511 110 108.37 418
03127125 17:32 11.0 106.44
Ogl27l25 17:33 23.5'11 I416't 1.0 106.26
Ogl27l25 17:34 23.510 4130.5 105.85
O3t27t25 17:35 23.508 0.5 't05.48
Avera0e
Minimum
Maximum
Summation
lnclud6d Data
9^inta
Total number of
nrt. D^i6ta
23.523
23.508
25.543
3,081.541
131
131
F = Unit Offline
E = Exceedance
I = Invalid
M = Maintenance
Report Generated: O4/ 74 / 25 07 :42
GP043AS-052980-RT-1881
0.5
0.4
0.6
59.9
'13'l
'13'l
C = Calibration
S = Substituted
T = Out Of Control
1',t.2
10.9
11.5
1,4U.7
125
131
108.26
105.48
1 09.89
r4,1 82.00
131
131
442
394
473
57,926
131
131
I
I
I
t
I
I
I
I
I
I
I
I
T
Page 61 of 91
Appendix C
Laboratory Analysis Data
Appendix C.1
Gravimetric Analyses
Page 63 of 91
I
I
I
I
I
t
I
I
I
t
I
I
I
I
I
I
I
t
I
ry \ Nt ( ) N I l(( r5 t EPA Methodslz02GravimetricAnalysis Report
Proiect Code: PROJ-052980
Date Finalized: 41L012025
Analyst: Crig Kormylo
Analytical Narrative
Filters were dessicated and tared to a constant weight in the MAQS laboratory prior to sampling. Following testing,
the filters were dessicated for at least 24 hours, then weighed to a constant weight (10.5 mg). The acetone rinses
were measured to the nearest milliliter, transferred to tared aluminum weighing dishes, taken to dryness under a
fume hood, dessicated for at least 24 hours, then weighed to a constant weight (10.5 m8). Each result above
represents total filterable particulate matter for each test run (acetone rinse + filter catch), with no blank correction
performed unless otherwise indicated.
Teflon CPM filters were extracted in a sonicator three times with water and three times with hexane. The extraction
water was added to the back-half impinger contents and extracted with hexane three times in a separatory funnel.
The inorganic fraction was transferred to a tared Teflon baggie, baked at 105C until 10 mL remained, taken to dryness
under a fume hood, dessicated for at least 24 hours, then weighed to a constant weight (10.5 mg). The organic
fraction was combined with the acetone and hexane field rinses, measured to the nearest milliliter, transferred to a
tared aluminum weighing dish, taken to dryness under a fume hood, dessicated for at least 24 hours, then weighed to
a constant weight (t0.5 mg). No blank correction was performed unless otherwise indicated.
lnstrumentation
All measurements were taken using a Sartorius Entris ll Analytical Balance under laboratory conditions. The
instrument is auto-calibrated and challanged with three NIST-traceable reference weights daily.
Detection Limit / Sensitivity
All measurements are recorded to 0.00019 (0.1mg).
Notes
No deviations from the analytical procedures from EPA Method 5 were noted. All samples were received in good
condition. After analysis, all samples are archived for a period of one year.
Attachments
Gravimetric Analysis Logs
Sample Chain of Custody
Laboratory Results Summary
Samole lD Filterable Particulate Matter lmrl
Huntincton Unit 1, Run #1 15.5
Huntington Unit 1, Run #2 9.9
Huntinston Unit 1, Run f3 9.6
Sample lD Condensable Particulate Matter (mg)
Huntincton Unit 1. Run #1 t7.1
Huntinston Unit 1, Run #2 10.9
Huntinston Unit 1, Run #3 11.0
,lo acetone blank corrections were performed,
:PM value includes a field blank correction.
GP043AS-052980-RT- 188 1 Page 54 of 91
/av \ M(.,N I l(t)St EPA Method 5 Gravimetric Analysis Log
Project Code:PROJ-0s2980
I
I
tUnit lD:Huntington Unit 1
Front-Half Partlculate Matter Filter Catch T
Filter #
Final Filter Weight f1 (g)
Final Filter Weight f2 (g)
Fllter Tare Weight f1 (g)
Filter Tare Weight f2 (g)
Filter Catch (g)
Run fi1
2272
Date weiSht (t)
Run f2
2271
Date weight (g)
Run *3
2256
Date weight (8)
Blank
22s3
Date weiSht (8)I
I
IFront-Half Particulate Matter Acetone Rinse Catch
4/712s 0.3558 417lzs 0.3636 4l7lzs 0.3630 4/712s 03644
418/2s 0.3666 4/812s 0.3634 4l8l2s 0.3631 4l8l2s 0.364s
3l14l2s 0.3666 3/L4l2s 0.3639 3lt4l2s 0.3633 3114/2s 0.3549
3/7712s 0.3666 3/17/2s 0.3640 3lL7l2s 0.3635 3/L7l2s 0.3647
0.0001 -0.0005 -0.0003 -0.0003
Rinse Volume (mL)
Rinse Mass (g)
Tin #
Final Dish Weight #1 (c)
Final Dish Weight f2 (g)
Dish Tare Weight (gl
Dish Tare Weight (gl
Total Rinse Catch (g)
Total Particulate Catch
Run f1
!25.r
98.2
8859
Date W€ight (g)
Run f2
125.2
98.3
8907
Date WeiSht (8)
Run f3
121.0
95
8911
Date Weight (8)
Blank
109.3
85.8
8892
Date WeiSht (g)
t
I
I
4l7l2s 6.3841 4l8l2s 6.3878 4l8l2s 5.4188 4l*lLs 5.3343
4l8lzs 6.3843 4lsl2s 6.3875 4/el2s 6.4186 4/el2s 5.334
3lL8/2s 6.3688 3/L8l2s 6.3778 3/1.8/25 6.409 3l74l2s 6.3342
3/26/2s 6.3687 3/2612s 6.3777 3126/2s 6.4091 3h8125 6.3346
0.0154 0.0099 0.0096 -0.0002
Filter catch (8)
+ Rinse Catch (g)
- Acetone Blank (g)
Run S1
0.0001
0.0154
0.0000
Run #2
0.0000
0.0099
0.0000
Run f3
0.0000
0.0096
0.0000
I
ITotal PM (t)
I
I
I
I
I
I
T
GP043AS-052980-RT- 1 881 Page 65 of 91
ry \ M(-)N I t(US t EpAMethodzozGravimetricAnalysis Log
Proiect Code:PROJ-052980
Unit lD:Huntington Unit 1
Back-Half Organlc Particulate Matter Catch
Run fl
8908
Run S2
8901
Run S3
8909
Blank
8900Tin f
Final Weight *1 (g)
Final Weight *2 (g)
Tare Weight #1 (g)
Tare Weight f2 (g)
Organic CPM Catch (t)
Back-Half lnorganic Particulate Mafter Catch
Date Weitht (8) Date Date Date
4l8l2s 6.4203 418/2s 6.4032 418/2s 6.4379 4l812s 6.4205
419l2s 6.4202 4/el2s 6.403 4ls/2s 6.4378 4/e/2s 6.4203
3lL7lzs 6.4063 3lt7/2s 6.3934 3117/25 6.4275 3117l2s 6.4L7
3/t8l2s 6.4067 3l18l2s 6.3932 3l78l2s 6.4277 3i18l2s 6.4168
0.0138 0.0098 0.0103 0.0035
I
I
I
I
I
I
I
I
I
t
I
I
I
I
I
I
I
I
I
Teflon Baggie fr
Final Weight fl (g)
Final Weisht f2 (g)
Tare Weight #1 (g)
Tare Weight fi2 (g)
lnorganic CPM Catch (8)
Condensable Particulate Catch
Run fll
2027
Wei8ht (8)
Run f2
2025
oate weiSht (8)
Run #3
2040
Date Weitht (g)
Blank
2022
Date Weitht (8)
418125
4/e125
3.7501
3.7596
4/8/2s
4/elzs
3.742
3.7416
418/2s 3.9254 4/el2s
4h0l2s
3.7L6
3.71584le/2s 3.9251
5 3.7548 3/t4l2s 3.7389 3lL4l25 3.922s 3174/2s 3.71s6
3lt7l25 3.7543 3h7lzs 3.7385 3lt7/2s 3.9226 3/t7l2s 3.7152
0.0053 0.0031 0.0027 0.0005
Organic CPM Catch (g)
+ Inorganic CPM Catch (g)
- CPM Blank (g)
Run fr1
0.0138
0.0053
0.0020
Run #2
0.0098
0.0031
0.0020
Run #3
0.0103
o.oo27
0.0020
Total cPM (8)0.0171
GP043AS-052980-RT-1881 Page 66 of 91
Laboratorv Results Summary
Sample lD Filterable Particulate Matter (mel
Huntington Unit 2, Run #1 10.6
Huntington Unit 2, Run #2 7.O
Huntington Unit 2, Run #3 5.3
Sample lD Condensable Particulate Matter lmcl
Huntington Unit 2, Run f1 5.3
Huntington Unit 2, Run #2 14.5
Huntincton Unit 2. Run #3 L2.4
,lo acetone blank corrections were performed.
:PM value includes a field blank correction.
ry \ ^vt()N
ll(())l
Project Code:
EPA Method 51202 Gravimetric Analysis Report
PROJ-052980
t
t
I
I
I
I
I
T
I
I
I
I
I
I
I
I
I
T
I
Date Finalized:4170/202s
Analyst:craig kormylo
Analytical Narrative
Filters were dessicated and tared to a constant weight in the MAqS laboratory priorto sampling. Followingtesting,
the filters were dessicated for at least 24 hours, then weighed to a constant weight (t0.5 mg). The acetone rinses
were measured to the nearest milliliter, transferred to tared aluminum weighing dishes, taken to dryness under a
fume hood, dessicated for at least 24 hours, then weighed to a constant weight (10.5 mg). Each result above
represents total filterable particulate matter for each test run (acetone rinse + filter catch), with no blank correction
performed unless otherwise indicated.
Teflon CPM filters were extracted in a sonicator three times with water and three times with hexane. The extraction
water was added to the back-half impinger contents and extracted with hexane three times in a separatory funnel.
The inorganic fraction was transferred to a tared Teflon baggie, baked at 105C until 10 mL remained, taken to dryness
under a fume hood, dessicated for at least 24 hours, then weighed to a constant weight (t0.5 mg). The organic
fraction was combined with the acetone and hexane field rinses, measured to the nearest milliliter, transferred to a
tared aluminum weighing dish, taken to dryness under a fume hood, dessicated for at least 24 hours, then weighed to
a constant weight (10.5 mg). No blank correction was performed unless otherwise indicated.
lnstrumentation
All measurements were taken using a Sartorius Entris ll Analytical Balance under laboratory conditions. The
instrument is auto-calibrated and challanged with three N|ST-traceable reference weights daily.
Detection Limit / Sensitivity
All measurements are recorded to 0.00019 (0.1mg).
Notes
No deviations from the analytical procedures from EPA Method 5 were noted. All samples were received in good
condition. After analysis, all samples are archived for a period of one year.
Attachments
Gravimetric Analysis Logs
Sample Chain of Custody
GP043AS-052980-RT- 188 1 Page 67 of 91
I
I Ov \ M()N I l(()5t. EpAMethod5GravimetricAnalysisLog
Proiect Code: PROJ-052980IUnit lD:Huntington Unit 2
t Front-Half Particulate Matter Fllter catch
Run f1 Run f2 Run #3 Blank
I Filter # 2254 2210 22tt 2253
Final Filter Weight fll (S)
I Final Filter Weight f2 (g)I il:::l:::w:::il[8
- Filter Catch (g) I 0.0001
I Front-Half Particulate Matter Acetone Rinse Catch
Date Weisht (s) Date weight (t) Date weiSht (g) Date wei8ht (8)
4l7lzs 0.3652 4l7lLs 0.3628 4l7lzs 0.36s3 4l7l2s o.3644
4l8l2s 0.3651 4l8l2s 0.3628 4l8l2s 0.3655 4l8l2s 0.3645
3174/2s 0.3651 u24/25 0.3627 Ll24l2s 0.36s6 3lt4l2s 0.3649
3h7/2s 0.3651 u3ol2s 0.3627 Ll30/25 0.36s8 3l77l2s o.3647
0.0001 0.0001 -0.0003 -0.0003
I Run #1 Run f2 Run f3 Blank
98.6 125.0 109.3Rinse Volume (mL) 7L4.3
Rinse Mass (g) 89.7
Tin fl 8904
Total Particulate Catch
77.4
8899
98.1
8910
85.8
8892
I Fina! Dish weight f1 (g)
Final Dish Weight f2 (g)
- Dish Tare weight (g)
I Dlsh Tare Weight (g)f Total Rinse catch (g)
Date WeiSht (8) Date Weight (8) Date weiSht (8) Date weiSht (t)
4/7lzs 6.4655 4/8/2s 6.4597 4l8l2s 6.437 418l2s 6.3343
4l8l2s 6.4652 4lsl2s 6.4596 4/912s 6.4369 419l2s 6.334
3lt7l2s 6.4548 3lL7l2s 6.4528 3lt7lzs 6.4306 3l14l2s 6.3342
3h8l2s 6.4549 3lr8/2s 6.4528 3/!8/2s 6.4308 3lt8l25 6.3346
0.0105 0.0069 0.0063 -0.0002
I
I
Run fl Run #2 Run #3
Filter catch (8) 0.0001 0.0001 0.0000
+ Rinse Catch (g) 0.0105 0.0069 0.0063
- Acetone Blank (g) 0.0000 0.0000 0.0000
Total PM (s) 0.0106 0.0070 0.0063
t
I
I
I
I
t
I
GP043AS-0s2e80-Rr-1881 Page 68 of 91
iav \ Ivl u N I i(L) 5 t. EpA MethodzozGravimetric Anarysis Log
Project Code:PROJ-052980
t
I
TUnit lD:Huntington Unit 2
Back-Half Organic Partlculate Matter Catch
Run #1
8884
Weisht (s)
Run fl2
8895
Run #3
8896
Blank
8900
I
I
I
I
Tin #
Final Weight fl (g)
Final Weight #2 (g)
Tare Weight #1 (g)
Tare Weight #2 (g)
Organic CPM Catch (g)
Back-Half lnorganic Particulate Matter Catch
Date WeiSht (8) Date Date
4l8l2s 6.3258 4/8/25 6.4471 4l8l2s 6.4887 4/8/2s 5.4205
4/9/25 5.3255 4le/2s 6.4469 4/e125 6.4885 4/sl2s 6.4203
3lL7l2s 6.3223 3lt7lzs 6.4418 3h7/25 6.4827 3/t7lzs 6.417
3178/25 6.3225 3lt8l2s 6.4420 3/18125 6.4820 3lt8l2s 6.4168
0.0033 0.0051 0.0065 0.0035
Teflon Baggie #
FinalWeight f1 (g)
FinalWeight f2 (g)
Tare Weight fl (g)
Tare Weight #2 (g)
lnorganic CPM Catch (g)
Condensable Particulate Catch
Run #1
2024
Date weiSht (g)
Run f2
2026
Date weiSht (8)
Run #3
2039
oate weight (8)
Blank
2022
oate weiSht (g)I
I
I
I
4/?l?s
4/t0l2s
3.722
3.72t7
418l2s
4/sl2s
3.911
3.9109
!18/25
4/e/2s
3.7346
3.734L
4lel2s
4ltol2s
3.716
3.7158
3174/2s 3.718 3lt4l3s 3.8998 3l26l2s 3.7254 3/t4/2s 3.7156
3lt7/2s 3.7177 3lt7l2s 3.8994 3l2sl3s 3.7265 3lt7lzs 3.7Lsz
0.0040 0.0114 0.0079 0.000s
Organic CPM Catch (g)
+ lnorganic CPM Catch (B)
- CPM Blank (g)
Run #1
0.0033
0.0040
0.0020
Run f2
0.0051
0.0114
0.0020
Run fl3
0.0065
0.0079
0.0020 I
t
I
I
I
I
I
I
0.0124Total cPM (s)
GP043AS-052980-RT- 188 1 Page 59 of 91
I
I
T
I
I
I
I
t
I
I
Ir
I
I
I
t
I
I
6rrr MONTROSE
I Laboratory Chain of Custody Record
Project Code:P'z o) ' o 5 2 1 t a
Client:Pn., ct ( c'Q P
Faclllty:t_/ ,tri I vt, Tp )
Unlt:t,II ,JL
Sample Date(s):gbf/t; '\/tt/tr-
Project Manager:('rl tt ,5 Ly'n c e
Sample lD / Run #Filter lD
FronlYz
Acetone Back % Hexane Back thV,later
Tin lD Volume(N,?Tin lD Volume(*1,
Baggl
e
ID
Volumg
1ngtf.,
t/\ lz t 22 )L )tjLtl qvL fs,icB l?v-\?oz)s)\ 1
ui t AZ 22+ I *,1 qYi gric i 112 7 hz',?/8 '(
,,1 ln3 ).75L ?1r\cis.c Blc'i i,4V u '.ct LIO s'7 lu
t,) Z 1Q I Ttsq ?qc'tl e9)if'.&'//rl,{2eZLl 353 L
U Z ttL ) I tt,qs.\t 7]1 1r.t;,1 /r,5 lrttti ,3.;'? t
ftt n ]zzt ?.q\0 qt ,I s:'iG t?6 {7$t 3rr ?
Btntr<2zvr q. ?,"\2-vir
L.l>LaP,{jic0 l31 1 /oLL )L3 L
Relinouished bv:(^ /-{,) , s. tv| L/-Date: S/tY/zs-
Received bv:
'g/rnr?Date z/E, /t,
,
t
GP043AS-0s2e80-Rr-1881 Page 70 of 91
Appendix D
Qual ity Assurance/Qual ity Control
Appendix D.1
Units and Abbreviations
64\ lt?,N,r+gp.E
@Xo/o 02
lccl
ldloc
oF
oR
" HzO
13.6
AH
AP
e
ug
Pa
P*
acfm
An
As
Btu
B*"
c"
Cars
Co',
cf or ft3
cfrn
Co",
cM
cm or m3
Cuo
co
cp
cs
CS
CS
cv
D
dcf
dcm
Dn
Ds
dscf
dsctn
dscm
Fd
fpm
fps
ft
e
s
gal
gr
gr/dscf
hr
UNITS AND ABBREVIATIONS
corrected to X% oxygen (corrected for dilution air)
absolute value of the confidence coefficient
absolute value of the mean differences
degrees Celsius
degrees Fahrenheit
degrees Rankine
inches of water column
specific gravity of mercury
pressure drop across orifice meter, inches H2O
velocity head of stack gas, inches HrO
total sampling time, minutes
microgram
density of acetone, mg/ml
density of water, 0.9982 g/mlor 0.002201 lb/ml
actual cubic feet of gas per minute at stack conditions
cross-sectional area of nozzle, ft'
cross-sectional area of stack, square feet (ft')
British thermal unit
proportion by volume of water vapor in gas stream
particulate matter concentration in stack gas, grlacf
average unadjusted gas concentration, ppmv
measured concentration of calibration gas, ppmv
cubic feet
cubic feet per minute
average gas concentration adjusted for bias, ppmv
average of initial and final system bias check responses from upscale calibration gas, ppmv
cubic meters
actual concentration of the upscale calibration gas, ppmv
average of initial and final system bias check responses from low-level calibration gas, ppmv
pitot tube coefficient
particulate matter concentration in stack gas, gr/dscf
calibration span, % or ppmv
measured concentration of calibration gas, ppmv
manufactured certified concentration of calibration gas, ppmv
drift assessment, % of span
dry cubic feet
dry cubic meters
diameter of nozzle, inches
diameter of stack, inches
dry standard cubic feet
dry standard cubic feet per minute
dry standard cubic meters
F-factor, dscf/MMBtu of heat input
feet per minute
feet per second
feet
square feet
gram
gallons
grains (7000 grains per pound)
grains per dry standard cubic feet
hour
I
I
I
I
t
I
I
I
I
I
I
I
I
I
I
I
I
I
tGP043AS-052980-RT-188 1 Page 73 of 91
I
I 6 IY"{?.N,T+P.p.H
I
in
k
K
K3
rq
kg
'6kwscftr
I
lb/hr
lb/MMBtu
lpm
m
M
m'
ma
Md
meq
mg
Mg
min
ml or mL
mm
MM
MMBtu/hr
mn
mol
mol. wt. or MW
Ms
MW
n
ng
nm
oI bar
ps
P^
Pm
ppb
ppbv
ppbvd
ppm
ppmv
ppmvd
ppmvw
Ps
psi
psia
psig
Psto
Q"
Q.
Qsto
R
I
UNITS AND ABBREVIATIONS
percent of isokinetic sampling
inch
kilo or thousand (metric units, multiply by 10s)
kelvin (temperature)
conversion factor 0.0154 gr/mg
conversion factor 0.002668 ((in. Hg)(ft'))/((mlX'R))
kilogram
pitot tube constant (85.49 fUsec)
thousand wet standard cubic feet per hour
liters
pounds per hour
pounds per million Btu
liters per minute
meter or milli
thousand (English units) or mega (million, metric units)
cubic meters
mass of residue of acetone after evaporation, mg
molecular weight of stack gas; dry basis, lb/lb-mole
milliequivalent
milligram
megagram (106 grams)
minute
milliliter
millimeter
million (English units)
million Btu per hour
total amount of particulate matter collected, mg
mole
molecular weight
molecular weight of stack gas; wet basis, lb/lb-mole
molecular weight or megawatt
number of data points
nanogram
nanometer
barometric pressure, inches Hg
picogram
stack static pressure, inches H2O
barometric pressure of dry gas meter, inches Hg
parts per billion
parts per billion, by volume
parts per billion by volume, dry basis
parts per million
parts per million, by volume
parts per million by volume, dry basis
parts per million by volume, wet basis
absolute stack gas pressure, inches Hg
pounds per square inch
pounds per square inch absolute
pounds per square inch gauge
standard absolute pressure, 29.92 inches Hg
volumetric flow rate, actual conditions, acfrn
volumetric flow rate, standard conditions, scfin
volumetric flow rate, dry standard conditions, dscfnr
ideal gas constant 21.85 ((in. Hg) (ft3)y(("R) (lbmole))
I
I
I
T
I
I
I
t
t
I
I
I
I
I GP043AS-052980-RT-1881 Page 74 of 91
64t l'l?.N,I+gP.I
SBnnat
SBi
scf
scfh
scftn
scm
scmh
sec
sf, sq. ft., or f
std
t
T o.szs
Ta
Tm
ton or t
tph or tons/hr
tpy or tons/yr
Ts
Tsto
va
Vt"
vm
Vmlstoy
vm
vs
Vwclstol
Vwilsto;
Vwsg(sto)
W
wa
W,p
Ws9
Y
UNITS AND ABBREVIATIONS
post-run system bias check, % of span
pre-run system bias check, % of span
standard cubic feet
standard cubic feet per hour
standard cubic feet per minute
standard cubic meters
standard cubic meters per hour
second
square feet
standard
metric ton (1000 kg)
t-value
absolute average ambient temperature, oR (+459.67 for English)
absolute average dry gas meter temperature, oR (+459.67 for English)
ton = 2000 pounds
tons per hour
tons per year
absolute average stack gas meter temperature, oR (+459.67 for English)
absolute temperature at standard conditions
volt
volume of acetone blank, ml
volume of acetone used in wash, ml
total volume H2O collected in impingers and silica gel, grams
volume of gas sampled through dry gas meter, ft'
volume of gas measured by the dry gas meter, corrected to standard conditions, dscf
stack gas volume sampled, acf
volume collected at stack conditions through nozzle, acl
average stack gas velocity, feet per second
volume of water vapor condensed, corrected to standard conditions, scf
volume of water vapor in gas sampled from impingers, scf
volume of water vapor in gas sampled from silica gel, scf
watt
weight of residue in acetone wash, mg
total weight of impingers, grams
total weight of silica gel, grams
dry gas meter calibration factor, dimensionless
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
t
I
IGP043AS-052980-RT- 188 1 Page 75 of 91
I
I
I
I
I
I
t
I
t
I
I
I
I
I
t
I
T
I
I
6n lt?,N,T+gp.I
AAS
ACDP
ACE
AD
ADL
AETB
AS
ASTI\4
BACT
BDL
BHP
BIF
BLS
CC
CD
CE
CEM
CEMS
CERMS
CET
CFR
CGA
CHNOS
CNCG
co
coc
COMS
CPM
CPMS
CT
CTM
cTo
CVAAS
D6
DE
Dioxins
DLL
DNCG
ECD
EIT
ELCD
EMPC
EPA
EPRI
ES
ESP
EU
FCCU
FGD
FI
FIA
FID
FPD
FPM
FTIR
FTPB
FTRB
Furans
GC
ACRONYMS
atomic absorption spectroscopy
air contaminant discharge permit
analyzer calibration error, percent of span
absolute difference
above detection limit
Air Emissions Testing Body
applicable standard (emission limit)
American Society For Testing And Materials
best achievable control technology
below detection limit
brake horsepower
boiler and industrial furnace
black liquor solids
confidence coefficient
calibration drift
calibration error
continuous emissions monitor
continuous em issions monitoring system
continuous emissions rate monitoring system
calibration error test
Code of Federal Regulations
cylinder gas audit
elemental analysis for determination of C, H, N, O, and S content in fuels
concentrated non-condensable gas
catalytic oxidizer
chain of custody
continuous opacity monitoring system
condensible particulate matter
continuous parameter monitoring system
combustion turbine
conditional test method
catalytic thermal oxidizer
cold vapor atomic absorption spectroscopy
equivalent diameter
destruction efficiency
polychlorinated dibenzo-p{ioxins (pcdd's)
detection level limited
dilute non-condensable gas
electron capture detector
Engineer ln Training
electoconductivity detector (hall detector)
estimated maximum possible concentration
US Environmental Protection Agency
Electric Power Research lnstitute
emission standard (applicable limit)
electrostatic precipitator
emission unit
fluid catalytic cracking unit
fl ue gas desulfurization
flame ionization
flame ionization analyzer
fl ame ionization detector
flame photometric detector
filterable particu late matter
Fourier-transform i nfrared spectroscopy
field train proof blank
field train recovery blank
polychlorinated dibenzofurans (pcdfs)
gas chromatography
GP043AS-052980-RT- 188 1 Page 76 of 91
6.i\ l,l?N,T+gp.H
GC/MS
GFAAS
GFC
GHG
HAP
HC
HHV
HPLC
HRGC/HRMS
HRSG
IC
ICAP
ICPCR
ICP-MS
IR
tso
KW
LFG
LHV
LPG
MACT
MDI
MDL
MNOC
MRL
MS
NA
NCASI
NCG
ND
NDIR
NESHAP
NG
NIOSH
NIST
NMC
NMOC
NMVOC
NPD
NSPS
OSHA
PAH
PCB
PCWP
PE
PFAS
PI
PID
PM
PMro
PMz.s
POM
PS
PSD
PSEL
PST
PTE
PTM
ACRONYMS
gas chromatography/mass spectroscopy
graph ite fu rnace atom ic absorption spectroscopy
gas filter correlation
greenhouse gas
hazardous air pollutant
hydrocarbons
higher heating value
high performance liquid chromatography
high-resolution gas chromatography/high-resolution mass spectroscopy
heat recovery steam generator
ion chromatography
inductively-coupled argon plasmography
ion chromatography with a post-column reactor
inductively coupled plasma-mass spectroscopy
infrared radiation
lnternational Standards Organization
kilowatts
landfill gas
lower heating value
liquified petroleum gas
maximum achievable control technology
methylene diphyenyl diisocyanate
method detection limit
maximum normal operating conditions
method reporting limit
mass spectrometry
not applicable or not available
National Council For Air And Steam lmprovement
non-condensable gases
not detected
non{ispersive infrared
National Emissions Standards For Hazardous Air Pollutants
natural gas
National lnstitute For Occupational Safeg And Health
National lnstitute Of Standards And Technology
non-methane cutter
non-methane organic compounds
non-methane volatile organic compounds
nitrogen phosphorus detector
New Source Performance Standards
Occupational Safety And Health Administration
polycyclic aromatic hydrocarbons
polychlorinated biphenyl compounds
plywood and composite wood products
Professional Engineer
per- and polyfluoroalkyl substances (PFAS)
photoionization
photoionization detector
particulate matter
particulate matter less than 10 microns in aerodynamic diameter
particulate matter less than 2.5 microns in aerodynamic diameter
polycyclic organic matter
performance specifi cation
particle size distribution
plant site emission limits
performance specifi cation test
permanent total enclosure
performance test method
t
I
I
I
I
I
I
I
t
T
I
I
I
I
I
t
I
I
IGP043AS-052980-RT- 188 1 Page77 of 9L
I
t
I
I
I
I
I
I
I
I
I
I
t
I
I
t
I
I
I
64\ lt?,N,I+gp.I
QA/QC
QI
OSTI
RA
RAA
RACT
RATA
RCTO
RICE
RM
RTO
SAM
SCD
SCR
SD
Semi-VOST
SRM
TAP
TBD
TCA
TCD
TGNENMOC
TGNMOC
TGOC
THC
Trc
TO
TO
TPM
TSP
TTE
ULSD
UV
VE
voc
VOST
WC
\A^/1/TP
ACRONYMS
quality assurance and quality control
Qualified lndividual
Qualifi ed Source Testing lndividual
relative accuracy
relative accuracy audit
reasonably available control technology
relative accuracy test audit
rotary concentrator thermal oxidizer
stationary reciprocating internal combustion engine
reference method
regenerative thermal oxidizer
sulfuric acid mist
sulfur chemiluminescent detector
selective catalytic reduction system
standard deviation
semivolatile organic compounds sample train
standard reference material
toxic air pollutant
to be determined
thermal cond uctivity analyzer
thermal cond uctivity detector
total gaseous non-ethane non-methane organic compounds
total gaseous non-methane organic compounds
total gaseous organic compounds
total hydrocarbons
tentatively identified compound
thermal oxidizer
toxic organic (as in EPA Method TO-15)
total particulate matter
total suspended particulate mafter
temporary total enclosure
ultra-low sulfur diesel
ultraviolet radiation range
visible emissions
volatile organic compounds
volatile organic sample train
water column
waste water treatment plant
GP043AS-052980-RT- 1881 Page 78 of 91
Ag silverAs arsenic
Ba barium
Be beryllium
C carbon
6 l,l?N,I+gp.E
Cd cadmiumCdS cadmium sulfideCH2O formaldehyde
CH3CHO acetaldehyde
CH3OH methanol
CHo
C2H4O ethylene oxide
CzHe ethane
CaH4O acrolein
CaH6O propionaldehyde
C.Hu propane
C6H5OH phenol
Clz chlorine
ClO2 chlorine dioxide
CO carbon monoxide
Co cobalt
COr carbon dioxide
Cr chromiumCu copperEtO ethylene oxideEIOH ethyl alcohol (ethanol)
hydrogen
water
HzOz hydrogen peroxide
HrS hydrogen sulfide
H2SO4 sulfuric acidHCI hydrogen chlorideHg mercuryIPA isopropyl alcoholMDI methylene diphyenyl diisocyanateMeCl2 methylene chloride
MEK methyl ethyl ketoneMeOH methanolMn manganese
nitrogen
ammonia
nickelNO nitric oxideNOz nitrogen dioxide
NO, nitrogen oxides
Oz orygen
P phosphorusPb leadPCDD polychlorinated dibenzo-pdioxinsPCDF polychlorinated dibenzofurans
CHEMICAL NOMENCLATURE
Se seleniumSOe sulfur dioxide
SOg sulfur trioxide
SO, sulfur oxides
TCDD tetrachlorodibenzodioxinTCDF tetrachlorodibenzofuranTGOC total gaseous organic concentrationTHC total hydrocarbons
Tl thallium
TRS total reduced sulfur compounds
I
I
I
t
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
H2
Hzo
N2
NHs
Ni
GP043AS-052980-RT- 188 1 Page 79 of 91
I
I
I
I
I
I
I
I
I
I
I
I
I
t
I
t
I
I
I
Appendix D.2
Manual Test Method QA/QC Data
IBIEt
il
o,lIIIIIIIIIIIIII
€(nc,olo
eoq6)
,s
f
r
60
E
sE
,
F
;E
,
E
v
v:
-
C
E
(E
.
U
)
.*
?
-
e
'
E
E
E_
r
r
J
#s

Ec
=e
E
r
*c
b
d
E
O-
c
r
Y
1
lI
'
E
r
-
-
#e
!
Ov

-
E8
-
=
b-
u
gg
:Z:
'd\sS
g+
.-
g
o
E,

oo
.
$.
P
t
r€
r
90
6"
.
i

cE
:3

0;
.g
+

aE
Eo

U.
=
€
o
aP
ER

ri
eI

Et
E;

EE
95

t
5
=E

!t

e
oE

€o
E;

bE
;;

@8
.I
E!
i
6
It

*e
t;

e
,E
.
E
,f

E
g3
E€

FR
Er

;E
€f
,

3
0
OE
i

Oo
b8

b9
oCFc
6a
La
,t
ttUOF<UU27ao<Eok>tdoo='o
J
IPHq
tOU>
io=E66
l6
z
3t!EaA6t
sEE
EOe?qg
tl
rE1EsBgq:
,E
EN99Eqi
3E
c
iL
o
ie
'E

9.
e
G
:.
8
E
ET
=
li
o
aE
:
!
t
o
6E
o
;o
.9

:8
L
YO
O
;P
x
*F
oai
>
L
<<
6t

tr
=
EP
F
.
==
!oofEIoE@!oage
'
6ofEE
;9g€
o;ec"e
69b3eE-
S
oRo,o>
EEE+I*
OE
:E
,A
g
qR
Ioga6'
Joo!o.Ya!oE:(,(!xoooo=!oo!o!ooooooo-xooo0,-
NonPPIo
oooPE8.Eo6o6co!octooEoFooogsulE'tEoEo€oG
t.9I
@
;oJo>EL,-ZC<aF
o
o
5sgc
cF
cN
!oo!oco.EsGo,ot,Got-9EL=oooEo.cxoooo=
oEEEa353E.A3oo=
o)
(Dg)o?o
t\6
,s
f
r
A6

5
es
E
;E
,
E
v
V.-
-zr
(
U
O
.f
;
?
:
p
E
E
AU
J
#5

Ec
=h
E
f
Sc
b
5
il
e
f
o
s;

b
-o
c
x
E
o=
o+
(
-
c
HS
-
*
b
-y

Lr
J
gs
oC6o
o\
(I
t!o=oc,
ECc(c(
o.Eo.EoEfao6
oEtro(
'6ENciei
9+
-9

*o
E
=E
B
3e
t
rs
E
69
e
€I
6.
i

cE
:c
,

EE
EI

TE
EE

si
oo
.
:
:d

;E
a3

E
$
iE

3e
3E

E*
;6

3E
:E

=
e
,E
i

98
"
gE

<9
EE

€;
Ir

:C
E
q
r=
.
:
,[
E

*s
5€

iR
En

x,
6a

o
t
,q
-
a

FL
;$

;q
!(ap{1i
!D
:
egi,!
.nro
ttUOhs
-7oo<Eok>ddoo=r$
J
tfu
1-
k<daU>
Jo=s
ff
5
l6
z
3o5caiEEE;o5E;
EOqEEgbg
og.c
.Eef
i
Fg38Pb8E
c
lr
o
5,
E
XE
E
iE
=
la
o
a!
:
R
o
pE
o
Eo
,J

g!
{
L
PO
o
6e
x
tF
ooi
i
G,

Et
r
80
0
.
=E
o-Pcod
,
Ei
,
6u
lt8r
oo
!I:
rid!B:
dE3i
-ttr
-t
qd@od
s1o!
-a.9
t
ci6:Za
@o
c-i-
aE.
oo
ai=t
o
c.g
Eo.:o!,E.eeoogIa:9E-
E
qIc4gEatE€9E
=ogE
'
EN
.r

cB
I
Ee
5f
i
i
-r
l
l
l
I
l*
l
"
l
El
l
l
=l
-
-
-
H
=l
l
l
ol
r
l

I
s
li
l
-
l
5
l;
l
g
l
E
l3
l
r
l
b
lg
l
€
l
6
lE
l
E
l
=
l*
l
'
l
efE:Eoio
OEcra9cS
i.
eo26>
.t(,oo!a!oo)oahoo-xoooo=
jo8otoFa8.c3ogtFEE!E;o,tEoEo5oeEsq,-
c5IItEo!IEGou
o!).Et,ooE9
3aE
coi;oJ
FEl
rl
.(
oN
!ooEocoo€a!o,o!t(!otgEL=o(,oELo.cxoooo.
oI.iq
IIIIIIIIIIIIIIItIII
I
EE
9d
rqd9
ir
Q

E:
de

9o
'
qq

Ea
oo
o
o
FF
h
F
3?
i9
5,
1
opl
€DI€f
f
EI
f
i
E,
!
TJ
f
T
.E
=
?E
€
EE
E

F
Ei
E

E
Ig
E
E
E
s"

it
i.
r
E
t
I
::
E
I
H
I
I
E
:
I
E
H
ts
G
o
r-
r
-
r

o
Fl
:
l
=
l
F
gl

I
lk
g*
g
"
IJ
J
'
tr
l
H
IIIIIII
EI
E!;l
f,sl
;?l
to$H
I
ll
Ftd;H
I
69gH
r
.l
Ia,oF.Jfi(9
t5ofi.I
$
,IE
66F'dd
CE;t;cGaqE
F;t".ia;daao
q.
tEI
oa
qaa
{€Ia
a:a1
n!
.i!
r.
:o
oc
t?
O
O
?
6
--
6
t
66
a
6
a
O
-o
6
-
l
-
ff
i
f
f
i
f
f
i
f
f
i
Eit$I5
I,
iI
il
i:t
rEi
3iiiTT
;l
rEI
-,
otr
r
lt
rii
r
Ii
i
!t

I
Ei

sl
tE
l
I:

I
t!

I
Ei
i
iI
I
E
E
E
ff
E
OO
ts
l
i
l
ff
i
Eff
i
f
f
i
H
f
f
i
f
f
i
{oEHt2I
aooaE
I
F
ts
aCIcICF
FaLacF
!
i
FGF
OoF
!G
oE
od
odFt€Fqa
!otsoo
66ER
aiFGF
EoFel,o!ots
Ch
dF
C
oFo
Et
r
t
r
E
E
riE*CIEcEoU.+eg3UT
,i
[
$
l
q
il
T
i
8,
1
i
rJll
|:!,lr
lot!!lILeoJ(,Ec.o
-ol-trEoIUIILGoJoFdO'

!
lloo-FUI-
Appendix D.3
Instrumental Test Method QA/QC Data
Prolcct llumbcr
Cllcm,lFlclllty
Soutrc/Locrtbn
O.tc
Opcretor
Anelyrcr lD
5lz+lzs
. -. -'ln{.- -..
-, 6,Trrbaq' :?J-lt oL- o I
qC.lbredon CtllodrrlD 6uVrlur Xopome * Crtot lt
2ero Flf.t'+ au A.b h.o
Mid Artorqrqt I b-t{L lo-ue '/SDrn i(ol[ zl oL L\.o?7t.oU /
CQCrlSrrdon CylladrrlD 6rrYrltto irr?onr f Erro,lt?rSl
Zero 0L-(.t\?mt-o.o o
Mid Au\orr{-t\(il,9+1 .Yl
Sprn FnorsLSoL t+- b7 l?- I.,fl t/
mbSles-mrrttM
I
I
I
I
I
I
T
I
I
I
I
I
I
I
I
I
I
t
I
Airgas
an Atr Liqui(b conpeny
Airgas Specialty Gases
Airgas USA LLC
Sz5 North Industrial l,oop Road
Tooele, LIT 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STAMARI)
Part Number: E03N180E15A0015
CylinderNumber: 4LM024748Laboratory: 124 - Tooele (SAP) - UT
PGVP Number: 872024
Gas Code: CO2,O2,BALN
Reference Number: 15340299207 5-1
Cylinder Volume: 150.0 CF
Cylinder Pressure: 2015 PSIG
Valve Outlet: 590
Certification Date: Mar 19,2024
Expiration Date: Mar {9, 2032
Certification performed in accordanco with "EPA Tracoability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)'document EPA
600/R-12/531, using the assay procodures listed. Analytical Methodology does not requirE conBcdion for analytical interferenc,e. This cylinder has a total analytical
uncrrtsinty as stated below with a confidence level of 95%. There are no significent impurities which affect ths use of this calibration mixture. All concrntrations are on a
mole/mole basis unless otheMise notod. The results relate only to the items tosted. Tho report shall not be reproducod except in full without approval of the laboratory. Do
Triad Data Available Upon Request
Slonature on file
Approved for Release
GP043AS-052980-RT- 188 1
Page I of 'l
Page 86 of 91
Not Use This b€low 100 osio. i.e. 0.7
Component Requested
Concentration
ANALYTICAL R.ESULTSActual Protoco!Concentration Method
TotalRelative
Uncertainty
Assay
Datee
CARBON DIOXIDE
OXYGEN
NITROGEN
9.000 o/o
10.50 o/o
Balance
8.979 o/o
10.42 o/o
G1
G1
+l- 1.0o/o NIST Traceable
+l- 0.5o/o NIST Traceable
03t19t2024
03t1912024
CALIBRATION STANDARDS
Type Lot lD Cylinder No Concentration Uncortainty Expiration Date
NTRM
NTRM
1 306041 I
I 1060604
cc413537
cc3381 73
7 .489 o/o CARBON DIOXIDE/NITROGEN
1 4.93 O/O OXYGEN/NITROGEN
0.6olo
0.2o/o
May 14,2025
Nov 02, 2028
lnstrumenUMake/Model
ANALITICAL EQUIPMENT
Analytical Principle Last Multipoint Callbration
Horiba VIA-S10 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
CO2 NDIR (Dixon)
02 Paramaqnetic (DIXON)
Mat 06,2024
Mat 06.2024
CERTIFICATE OF AI\ALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
E03N161El540287
E80162302
124 - Tooele (SAP) - UT
872023
co2,02,BALN
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Nov 14.2031
Airuas
an Ar Liquido corpany
Airgas Specialty Gases
Airgas USA LLC
SzS North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
I
I
I
I
I
I
I
I
T
I
I
I
I
I
I
t
I
t
I
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
153402892897-1
158.0 CF
2015 PSIG
590
Nov 14, 2023
Certification performed in accordanco with "EPA Traceability Protocol fior Assey and Certification of Gaseous Calibration Standards (May 2012)'document EPA
6OO/R-1 2/531 , using the assay procodures listed. Analytical Methodology does not require conection for analytical interference. This cylindcr has a total analytical
uncsrtainty as stated below with a confidence l6vel of 950/0. There arc no significant impurities which affect ths use of this calibration minure. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the itoms tosted. The report shall not bo raproduced except in full without approvel of the laboratory. Do
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-052980-RT- 1 88 1
Page 1 of 'l
Page 87 of 91
Not Us6 Thig below 100 psis, i.e. 0.7
Component Requested
Concentration
ANALYTICAL RESULTS
Actual ProtocolConcentration Method
Tota! Relative
Uncertainty
Assay
Dates
CARBON DIOXIDE
OXYGEN
NITROGEN
18.00 %
21.00 o/o
Balance
17.69 0/o
21.07 o/o
G1
G1
+l- 0.60/o NIST Traceable
+l- 0.9o/o NIST Traceable
11t14t2023
11t14t2023
CALIBRATION STANDARDS
Type Lot tD Cylinder No Concentratlon Uncertainty Expiration Date
NTRM 1 3060802
09061434
cc415397
cc282492
24.M o/o CARBON DIOXIDE/NITROGEN
22.53 o/o OXYG EN/N ITROG EN
0.6%
0.4o/o
Oec 11,2025
May 13,2025NTRM
lnstrumenUMako/Model
ANALYTICAL EQUIPMENT
Analytlca! Principle Last Multipoint Calibration
Horiba VIA-s10 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
CO2 NDIR (Dixon)
02 Paramaqnetic (DIXON)
od 17,2023
od 17,2023
Appendix D.4
Accreditation Information I Certifications
GP043AS-052980-RT- 1881
I3l
oelI
oFcr
)_-
c
PEBg
;
OE
.
E
c.
9

!
.a

a:
E5
P
'
!U
EHs
S
U
6'
.
<=

o
o.
>
'
E
.=
o
t
r
E
3=
.
:z
.
E
{
o;
=
oo
u
6:

ft
!r
EkB

a
iH
&
Na
t
<;

o
=o
O
EP

a
PE

Fi
r
al
.
=
b9
U
_v
(
J
[-
o
^
L
o.
-

u
E
BE
=
o'
1
5
ox
o
oE
a
C€
+
6+
8
qn
s
^P

3X
Ea
=
-.
E
U
)
:o
<
'F
o8d
oIc
arqUl-
{fr
rqaF{
lr
{F]
-d&lr
{rqac&F<zc
oo=ooOooo.C)N
tomh0
-Lop
)
+)
ca
.q
DHrtLoop
)
caaop
)dLFXLoF
)
\3q)
+)
ol
)
\3pLq)q)
Co*ot!oooo+ooooJorLC.e{-
.9oo.4anCo(-
)0)E
IIIIIIIIII
q)qJaPqooa(tto{L)6.tq)L$iq)to(aoLb!oLqq)Lc)(aFi
o)
.oa0)a/)!o.S
2
c
-
E
A3
x
T9
S
R
lu

L-

(r
)
-
o
-@
U=

QN
<:
J
l
>
.f
r

t
o
-4
\
)
)
s
86
i
6<
E
:
i
o.
9
:
A\
s
-
V
YL
:
.9
X
o
o
>l
.
i
U
>
EI
fd.fr
T
?a$l
(,
I
gan
I
$NoN-ol.oou-oooEF.N.2.CErq)co0)o-
dorooologr
(oo-
JFzIJ
J
IzZo;ztr
J
€tJ
.
l
C,
)c&Fzo=
@(\oNNozoLdExul
l!oI.J
J
l-6
IE@oa3G=aIo-f@Eao.a
uF
(f
)No(\
tNNoLJfo9,
l!ouJko
\{s
.eS
(E
E
e6

E
tr
E

U)
.!
2
2
;
EE

E
LLGL

€
F(
J
r
(
r
o.
=

o
EB

F
EE

;
l€

s
a$

F
eB

t
OG
t

S
ut
gT

I
E
I3
i
E
f
:
E
s
EE

tS
{-

lh
i
.Z

.=

rl
J

H
EE

ro
-
LA
ai.
-
E
.=
|
t
s
{E+
g
$
|
EE

?
E
+.
.
2

O
=
Ez
t

E
-
gE

E
Z
EE

E
E
;
g
el

F
Ed

s
b
Fe
o
o
:(o=t-o.Co.o+,al--o
zo-FUJJo-=oolloII
JFolJ
.FuUJo
IIIIIIIIIIIIIITIIII
H@@HIFdIo6orNtr
loIa(v
)too-(9
This is the Last Page of This Document
If you have any questions, please contact one of the following
individuals by email or phone.
Name: Craig Kormylo
Title: District Manager
Region: USA - Stack - Great Plains - Operations
Emai! : [e-mail]
Phone: [phone]
Name: Glen Capra
Title: Vice President
Region: USA - Stack
Emai! : [e-mail]
Phone: (5L2) 772-6450
-*-_D,vtsloN OF AtR o,.,At_tTY
GP043AS-052980-RT- 1881 Page 91 of 91
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name PacifiCorp Huntington - Unit No. 1
Company Contact:Tom Wiscomb
Contact Phone No.801-220-2373
Source Designation:Unit No. 1
Test & Review Dates
Test Date: 3/25/2025
Review Date: 5/2/2025 Tabs Are Shown
Observer:3/25/2025
Reviewer:Paul Morris
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
0.030 74.000
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0052 25.0095 0.0024
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
323.30 570.08 0.9970 1.8 0.84 23.75 -4.2 0.234
Contractor Information
Contracting Company: Montrose Air Quality Services, LLC
Contact: Cheyney Guymon
Phone No.: 801-794-2950
Project No.:
1840
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
PacifiCorp Huntington - Unit No. 1
Testing Results Lab Data - grams collected
Test Date 3/25/2025 3/25/2025 3/25/2025 3/25/2025 Lab Data Probe Filter Back
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.0154 0.0001 0.0171
As ft^2 570.08 570.08 570.08 Run 2 0.0099 0 0.0109
Pbar 23.75 23.75 23.75 Run 3 0.0096 0 0.011
Pq (static)-4.20 -4.20 -4.20 Run 4
Ps 23.44 23.44 23.44
Avg. Ts F 110.75 112.17 112.83 Front Half Emissions Summary
CO2 - FCO2 12.00 12.20 12.10 Run 1 Run 2 Run 3 Run 4 Avg.
O2 7.10 6.90 7.10 gr./dscf 0.0032 0.0020 0.0020 0.0024
N2+C 80.90 80.90 80.80 lbs/hr 33.7368 20.7839 20.5079 25.0095
Md 30.20 30.23 30.22 lbs/MMBtu 7.060E-03 4.268E-03 4.272E-03 0.0052
Ms 28.91 28.78 28.76
Y 1.00 1.00 1.00
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 92.81 96.33 94.65 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 186.40 219.80 217.80 gr./dscf 0.0068 0.0042 0.0042 0.0051
AVG. Tm F 65.08 64.67 67.75 lbs/hr 70.9560 43.6671 44.0065 52.8766
Vm std 74.22 77.12 75.33 lbs/MMBtu 1.485E-02 8.968E-03 9.168E-03 0.0110
Vw std 8.77 10.35 10.25
Bws 0.11 0.12 0.12
S Bws 0.11 0.12 0.12
Avg. Sqrt Dlp 0.84 0.85 0.85
Vs 55.07 56.12 55.94 F factor used
scfm wet 1365323.74 1387814.69 1381880.40 1840
acfm 1883774.05 1919558.19 1913577.19
Qsd dscfh 73258717.62 73424765.98 72980683.53
# Sample
Points 12.00 12.00 12.00
Dn 0.234 0.234 0.234
An 2.99E-04 2.99E-04 2.99E-04
Start Time 0:00 0:00 0:00
End Time 0:00 0:00 0:00Total Test
time 120.00 120.00 120.00
Time @ point 10.00 10.00 10.00
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
PacifiCorp Huntington - Unit No. 1 Flow & Moisture Test Date 3/25/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
570.08 23.75 -4.20 23.44 111 12.00 7.10 80.90 30.20 28.91
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1135
0.9970 0.84 92.806 186.40 65.08 74.216 8.774 0.1057 0.1135 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.836 55.07 1,365,324 1,883,774 7.33E+07 12 0.234 120 10.00 1.708333
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 111.442 Wt. (Final) Wt. (Initial) lc
2 118.320 0.54 1.30 110 64 64 454.10 349.80 104.3
3 125.520 0.66 1.60 110 64 64 683.90 654.00 29.9
4 133.159 0.74 1.80 110 64 64 757.80 731.10 26.7
5 140.560 0.59 1.50 110 65 65 894.30 868.80 25.5
6 148.490 0.75 1.80 111 65 65 0.0
7 156.541 0.79 1.90 111 65 65
8 164.220 0.64 1.60 111 66 66 Isokinetics
9 172.540 0.78 1.90 111 66 66 Test Date 3/25/2025
10 180.649 0.79 1.90 111 66 66 Start Time enter
11 188.170 0.64 1.60 111 66 66 End Time
12 196.190 0.74 1.80 112 65 65 Run 1
13 204.248 0.75 1.80 111 65 65
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1
Run 2
PacifiCorp Huntington - Unit No. 1 Flow & Moisture Test Date 3/25/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
570.08 23.75 -4.20 23.44 112 12.20 6.90 80.90 30.23 28.78
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1182
0.9970 0.84 96.325 219.80 65 77.119 10.346 0.1183 0.1182 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.849 56.12 1,387,815 1,919,558 7.34E+07 12 0.234 120 10.00 1.83
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 204.685 Wt. (Final) Wt. (Initial) lc
2 212.450 0.66 1.60 111.0 63.0 63.0 594.30 494.10 100.2
3 220.510 0.78 1.90 111.0 63.0 63.0 726.70 674.90 51.8
4 228.830 0.79 1.90 112.0 63.0 63.0 808.10 771.60 36.5
5 236.670 0.65 1.70 113.0 64.0 64.0 955.60 924.30 31.3
6 245.120 0.77 2.00 112.0 64.0 64.0 0.0
7 253.420 0.79 2.00 113.0 65.0 65.0
8 260.910 0.62 1.60 113.0 65.0 65.0 Isokinetics
9 268.980 0.74 1.90 113.0 65.0 65.0 Test Date 3/25/2025
10 277.295 0.78 2.00 112.0 66.0 66.0 Start Time
11 284.760 0.61 1.60 112.0 66.0 66.0 End Time
12 292.720 0.72 1.80 112.0 66.0 66.0 Run 2
13 301.010 0.75 1.90 112.0 66.0 66.0
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1
Run 3
PacifiCorp Huntington - Unit No. 1 Flow & Moisture Test Date 3/25/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
570.08 23.75 -4.20 23.44 113 12.10 7.10 80.80 30.22 28.76
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1205
0.9970 0.84 94.646 217.80 68 75.330 10.252 0.1198 0.1205 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.845 55.94 1,381,880 1,913,577 7.30E+07 12 0.234 120 10.00 1.82
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 302.792 Wt. (Final) Wt. (Initial) lc
2 310.130 0.59 1.50 113.0 66.0 66.0 468.6 349.2 119.4
3 318.130 0.72 1.80 112.0 66.0 66.0 686.7 655.3 31.4
4 326.228 0.77 2.00 113.0 67.0 67.0 753.5 719.7 33.8
5 334.050 0.69 1.80 113.0 67.0 67.0 932.1 898.9 33.2
6 342.180 0.79 1.90 113.0 67.0 67.0 0.0
7 350.114 0.76 1.90 113.0 68.0 68.0
8 357.550 0.60 1.50 113.0 68.0 68.0 Isokinetics
9 365.680 0.71 1.80 112.0 69.0 69.0 Test Date 3/25/2025
10 373.575 0.74 1.90 113.0 69.0 69.0 Start Time
11 381.300 0.65 1.70 113.0 66.0 66.0 End Time
12 389.460 0.78 2.00 113.0 70.0 70.0 Run 3
13 397.438 0.79 2.00 113.0 70.0 70.0
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name PacifiCorp Huntington - Unit No. 2
Company Contact:Richard Neilsen
Contact Phone No.435-687-4334
Source Designation:Unit No. 2
Test & Review Dates
Test Date: 3/27/2025
Review Date: 5/2/2025 Tabs Are Shown
Observer:
Reviewer:Paul Morris
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
70.000
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0032 14.6607 0.0016
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
322.54 567.39 0.9900 0.7662 0.84 23.7 -4.2 0.245
Contractor Information
Contracting Company: Montrose Air Quality Services, LLC
Contact: Cheyney Guymon
Phone No.: 801-794-2950
Project No.:
1840
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
PacifiCorp Huntington - Unit No. 2
Testing Results Lab Data - grams collected
Test Date 3/27/2025 3/27/2025 3/27/2025 3/27/2025 Lab Data Probe Filter Back
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.0105 0.0001 0.0053
As ft^2 567.39 567.39 567.39 Run 2 0.0069 0.0001 0.0145
Pbar 23.70 23.70 23.70 Run 3 0.0063 0.0124
Pq (static)-4.20 -4.20 -4.20 Run 4
Ps 23.39 23.39 23.39
Avg. Ts F 113.58 114.67 115.50 Front Half Emissions Summary
CO2 - FCO2 12.90 12.80 12.80 Run 1 Run 2 Run 3 Run 4 Avg.
O2 6.50 6.60 6.50 gr./dscf 0.0021 0.0014 0.0012 0.0016
N2+C 80.60 80.60 80.70 lbs/hr 19.7950 13.0324 11.1547 14.6607
Md 30.32 30.31 30.31 lbs/MMBtu 4.253E-03 2.939E-03 2.534E-03 0.0032
Ms 28.90 28.79 28.76
Y 0.99 0.99 0.99
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 100.74 98.83 103.33 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 218.00 226.90 241.60 gr./dscf 0.0031 0.0044 0.0037 0.0037
AVG. Tm F 74.96 84.67 86.00 lbs/hr 29.6925 40.0282 33.1098 34.2768
Vm std 78.38 75.49 78.78 lbs/MMBtu 6.379E-03 9.026E-03 7.523E-03 0.0076
Vw std 10.26 10.68 11.37
Bws 0.12 0.12 0.13
S Bws 0.12 0.13 0.13
Avg. Sqrt Dlp 0.77 0.75 0.74
Vs 51.07 49.59 49.41 F factor used
scfm wet 1251152.40 1212640.19 1206493.39 1840
acfm 1738526.54 1688194.78 1682073.08
Qsd dscfh 66378705.30 63740670.95 63257979.42
# Sample
Points 12.00 12.00 12.00
Dn 0.245 0.245 0.245
An 3.27E-04 3.27E-04 3.27E-04
Start Time 0:00 0:00 0:00
End Time 0:00 0:00 0:00Total Test
time 120.00 120.00 120.00
Time @ point 10.00 10.00 10.00
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
PacifiCorp Huntington - Unit No. 2 Flow & Moisture Test Date 3/27/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
567.39 23.70 -4.20 23.39 114 12.90 6.50 80.60 30.32 28.90
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1234
0.9900 0.84 100.736 218.00 74.96 78.377 10.261 0.1158 0.1234 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.772 51.07 1,251,152 1,738,527 6.64E+07 12 0.245 120 10.00 1.816667
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 444.290 Wt. (Final) Wt. (Initial) lc
2 452.000 0.44 1.40 113 67 67 580.10 494.80 85.3
3 460.510 0.62 1.90 113 71 68 741.70 676.40 65.3
4 469.062 0.62 1.90 114 74 68 795.60 761.10 34.5
5 476.930 0.51 1.60 115 74 70 981.80 948.90 32.9
6 485.380 0.63 1.90 113 77 69 0.0
7 493.782 0.62 1.80 114 80 70
8 501.880 0.53 1.60 115 77 72 Isokinetics
9 510.570 0.65 2.00 113 81 74 Test Date 3/27/2025
10 519.680 0.69 2.10 113 84 75 Start Time enter
11 527.450 0.54 1.60 113 83 75 End Time
12 535.960 0.64 1.90 113 84 76 Run 1
13 545.026 0.69 2.10 114 86 77
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1
Run 2
PacifiCorp Huntington - Unit No. 2 Flow & Moisture Test Date 3/27/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
567.39 23.70 -4.20 23.39 115 12.80 6.60 80.60 30.31 28.79
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1272
0.9900 0.84 98.834 226.90 85 75.491 10.680 0.1239 0.1272 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.747 49.59 1,212,640 1,688,195 6.37E+07 12 0.245 120 10.00 1.67
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 550.095 Wt. (Final) Wt. (Initial) lc
2 557.990 0.50 1.00 113.0 78.0 76.0 473.50 348.40 125.1
3 566.040 0.57 1.70 115.0 85.0 77.0 681.00 650.80 30.2
4 575.104 0.70 2.10 115.0 89.0 78.0 793.70 754.10 39.6
5 582.960 0.49 1.50 114.0 86.0 79.0 997.00 965.00 32.0
6 591.060 0.56 1.70 115.0 89.0 81.0 0.0
7 599.965 0.65 2.00 115.0 92.0 81.0
8 608.000 0.52 1.60 113.0 89.0 82.0 Isokinetics
9 616.330 0.55 1.70 116.0 91.0 83.0 Test Date 3/27/2025
10 624.392 0.52 1.60 116.0 93.0 83.0 Start Time
11 631.920 0.45 1.40 114.0 85.0 83.0 End Time
12 640.230 0.59 1.80 114.0 91.0 84.0 Run 2
13 648.929 0.63 1.90 116.0 93.0 84.0
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1
Run 3
PacifiCorp Huntington - Unit No. 2 Flow & Moisture Test Date 3/27/2025
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
567.39 23.70 -4.20 23.39 116 12.80 6.50 80.70 30.31 28.76
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1302
0.9900 0.84 103.329 241.60 86 78.779 11.372 0.1261 0.1302 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.744 49.41 1,206,493 1,682,073 6.33E+07 12 0.245 120 10.00 1.86
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 649.225 Wt. (Final) Wt. (Initial) lc
2 657.280 0.52 1.60 115.0 84.0 83.0 645.6 494.8 150.8
3 666.080 0.67 2.00 116.0 87.0 84.0 704.1 676.0 28.1
4 674.828 0.67 2.00 116.0 89.0 84.0 784.9 753.5 31.4
5 682.610 0.49 1.50 114.0 85.0 83.0 974.9 943.6 31.3
6 691.570 0.65 2.00 116.0 88.0 83.0 0.0
7 701.101 0.73 2.20 116.0 92.0 83.0
8 709.740 0.56 1.70 116.0 87.0 83.0 Isokinetics
9 718.880 0.68 2.10 114.0 90.0 83.0 Test Date 3/27/2025
10 727.920 0.17 2.10 117.0 91.0 84.0 Start Time
11 735.150 0.43 1.30 116.0 88.0 84.0 End Time
12 743.330 0.55 1.70 115.0 90.0 84.0 Run 3
13 752.554 0.68 2.10 115.0 91.0 84.0
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Page 1