DAQ-2024-010467

1

DAQC-956-24
Site ID 10884 (B4)

MEMORANDUM

TO: STACK TEST FILE – HEBER LIGHT AND POWER

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Robert Sirrine, Environmental Scientist

DATE: September 23, 2024

SUBJECT: Contact: Jason Norlen – 435-654-2913
Tester: Montrose Air Quality Services
Source: Engine Unit #2.
FRS ID#: UT0000004905100006
Permit# AO DAQE-AN108840013-24 dated January 29, 2024
Action Code: Tr
Subject: Review of Stack Test Report Received August 20, 2024
On August 20, 2024, the Utah Division of Air Quality (DAQ) received an emissions test report for the
Heber Light and Power engine unit #2, located in Heber, Utah. Testing was performed on July 17, 2024,
to determine compliance with emission limits for NOX and CO found in Condition 1I.B.2.a of their AO.
The DAQ-calculated test results are:

Source Test Date RM/Pollutant DAQ Result Test Result Limit

Unit #2 7/17/24 7/NOX 2.44 lb/hr 2.4 lb/hr 4.06 lb/hr
10/CO 0.07 lb/hr 0.068 lb/hr 1.0 lb/hr

DEVIATIONS: None noted.

CONCLUSION: The stack emissions test reports appear to be acceptable.

RECOMMENDATION: The tested emissions appear to be acceptable and in compliance with the
applicable emission limits at the time of testing. The source used
incorrect significant figures which are correct in the DAQ results. No
further action is recommended.

HPV: No.

ATTACHMENT: Stack test reports received August 20, 2024.
DAQ generated excel spreadsheets.

6fi}}qNIHIT
Source Test Report
2024 Compliance Emissions Testing
Unit 2 Natural Gas-Fired Generator Engine
Heber Light and Power
Heber, Utah
Test Date: July 17,2024
Document #: GP08{AS-0401 28-RT-1 672
UTAH DEPAHTMENT OF
ENVIRONMENTAL OUATJTY
Alc '2 , !it!,l
DIVISION OF AIR OUAUTY
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Source Test Repoft
2024 Compliance Emissions Testing
Unit 2 Natural Gas-Fired Generator Engine
Heber Light and Power
Heber, Utah
Prepared For:
Heber Llght and Power
300 South 735 West
Heber, Utah 84032
Prepared By:
Montrose Air Quallty Services, LLC
6823 South 3600 West
Spanish Fork, Utah 84650
For Submlsslon To:
State of Utah Depaftment of Environmental Quality (UDEQ),
Dlvislon of Alr Quallty
195 Nofth 1950 West
Salt Lake City, Utah 84116
Document Number: GPO81AS-O4O128-RT-1672
Test Dats: luly L7r 2lJ24
Submittal Date: August L5r 2024
UTAH DEPARTMENT OF
ENVIRONMENTAL QUAUTY
DIVISION OF AtR QUALITV
Page # 1
Document #: GP081AS-0401 28-RT-1 672
Review and Certlficatlon
All work, calculatlons, and other adlvltles and tasks performed and presented in thls
document were carrled out by me or under my direction and supervlslon. I hereby certify
that, to the best of my knowledge, Montrose operated in conformance wlth the
requlrements of the Montrose Quality Management System and ASTM D7036-04 durlng thls
test project.
Slgnature:
Name:
August L2,2024
Cheyney Guymon Tltlc:Fleld ProJect Manager
I have revlewed, technlcally and edltorlattyf Oetalls, calculadons, results, concluslons, and
other approprlate wrltten materials contalqed hereln. I hereby certlfy that, to the best of my
knowledge, the presented materlal ls authtntlc, accurate, and confiorms to the requlrements
of the Montrose Quallty Management SystCm and ASTM D7036-04.
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TlUe:
slgnaturett -.l*^ lL-u;rP Date:
Beckle Hawkins
August L2,2024
Dlstrict Manager
Document #: GP08 1 AS-O+O r rtlffi 3i, ;
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Table of Contents
Section
1.0 Introductlon......... ...............s
1.1 Summary of Test Program .............5
1.2 Key Personnel............. .................7
2.0 Plant and Sampling Location Descrlptions.............. ..................9
2.L Process Descrlptlon, Operation, and Control Equipment............... ......9
2.2 Flue Gas Sampllng Locations... .......9
2,3 Operatlng Condltions and Process Data ......... ............,.....9
3.0 Sampllng and Analytlcal Prccedures .....10
3.1 Test Methods............ ,................10
3.1.1 EPA Method 1.............. ......10
3.1.2 EPA Method 2.............. ......10
3.1.3 EPA Method 4.............. ......11
3.1.4 EPA Methods 3A, 7E,, and 10...... .......... 133.2 Process Test Methods............. .....!4
4.0 Test Dlscusslon and Results .................154.t Fleld Test Devlatlons and Exceptlons.......... ...................154.2 Presentatlon of Results ................15
5.0 Intemal QA/QC Activitles ....1S5.1 QA/QC Audlts....... ......15
5.2 QA/QC Dlscusslon. ......155.3 Quallty Statement ......15
List of Appendices
Appendlx A Field Data and Calculations ......16A.1 Sampling Location ....,.L2A.2 Emissions Test Results ................19
A.3 Field Data.. ..............,.194,4 Example Calctlations ..................20
Appendlx B Faclllty Process Data......... .,.,..,21
Appendlx C Quality Assurance/Quallty Control ...,.........22C.l Unlts and Abbrevlatlons ............ ..................23
C.2 InstrumentalTest Method QA/QC Data......... .................24
C.3 Callbration Records..... ................2S
C.4 Accredltation Informatlon/Certlflcatlons......... ................ 26
Page # 3
Document #: GP081AS-040 128-RT-1672
List of Tables
Table 1-1 Summary of Test Program """""'5
Tabfe 1-2 Summary of Emlsslons Resutts - Generator Englne Unlt #2, )uly L7, 2024 ........6
Table 1-3 Test Personnel and Observers............ """"""7
Table 2-1 Control Device """"""8
Table 2-2 Sampllng Locatlon """'8
List of Figures
3-1 EPA Methods 2 and 4 Sampllng Tra1n......... """"" 12
3-2 EPA Methods3A,7E, and 10 Sampllng Traln ........ """""""" 14
Document #: GPo81AS-OOOr rtlffi 8fl
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1.O fntroduction
1.1 Summary of Test Program
Heber Ught and Power contracted Montrose Alr Quality Services, LLC (Montrose) to perform
a compllance emisslons test program on the sources llsted ln Table 1-1 at thelrfaclllty
located ln Heber, Utah.
The tests are conducted to determlne compllance wlth the appllcabte emtsslon llmits llsted
ln Sectlon II.B. of the Utah Department of Envlronmental Quallty (UDEQ Approval Order
(AO) (DAQE-AN 108840 OL3-24) dated January 29, ZOZ4,
The speclflc obJectlves are to:
. Determlne the concentrations and mass rates of nltrogen oxldes (NOx) and
carbon monoxlde (CO) ln emlsslons from the exhaust of one (1) natural gas
flred Caterplllar 3516H generator englne (#2, 1,350 kW rating).
. Conduct the test program with a focus on safety.
Montrose performed the tests to measure the emlsslon parameters llsted ln Table 1-1.
Table 1-1
Summary of Test Plogram
To slmplify thls report, a llst of Unlts and Abbrevlatlons ls lncluded ln Appendtx C.1.
Throughout this report, chemlcal nomenclature, acronyms, and rreportlng unlts are not
deflned. Please refer to the llst for specific detalls.
Thls report presents the test results and supportlng data, descrlptlons of the tesgng
procedures, descrlptlons of the facllity and sampllng locations, and a summary of the quality
assurance procedures used by Montrose. The average emission test results are summarlzed
and compared to thelr respectlve emlsslons standards ln Table 1-2. Detalled results for
indlvldual test runs and all supportlng data can be found ln the appendlces.
The testing was conducted by the Montrose personnet llsted ln Table 1-3. The tests were
conducted according to the test plan (protocol) that was submltted to and approved by the
UDEQ.
Document #: cP081 AS-O4Or rtlffi trs,
Table 1-2
summala of Emlaelone Rerulte - Generator Englne unlt #& Tuly LTr 2024
l{ltrogen Oxldcc (llox ar NOz)
II.B.2.a of AO DAQE-
Carbon lrlonoxlde (Go)
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L.2 Key Personnel
A llst of project particlpants ls included below:
Faclllty Informatlon
Source Locatlon: Heber Llght and Power
Bay #2
300 South 735 West
Heber, Utah 84032
ProJect Contact: Jason Norlen
Company: Heber Llght and Power
Role: General Manager
Telephone: [phone]
Emall: [e-mail]
Agency fnformatlon
Regulatory Utah Department of Environmental Quality (UDEQ)
Agency: Dlvlslon of Air QualltyAgenry Contact: Chad Gllgen, Minor Source Compllance
Telephone: [phone]
Email: [e-mail]
Teetlng Company Informatlon
Testlng Flrm: Montrose Air Quality Servlces, LLC (Montrose)
Contact: Beckle Hawkins Cheyney GuymonTitle: DisHct Manager Fleld proJect Manager
Telephone: 8OL-372-7O49 801-794-2950Emall: [e-mail] [e-mail]
Test personnel and obseryers are summarlzed ln Table t-3.
Tablc 1-3
Test Penconnel and Obaeryerc
Cheyney Guymon
ProJect Manager
Quallfied Indlvldual (QI)
Trailer operator
Joe Avila i Montrose Field Technldan
Sample Traln operator
Joby Dunmlre i Montrose
Page#7
Document #: GP08 1 AS-040 1 28-Kt -1 67 2
2.O Plant and sampling Location Descriptions
2.1 Process Description, Operation, and Control
Equipment
Heber Light and Power ope6tes the power generatlon faclllty in Heber, Utah. The natural
gas flred generator engine #2 ls lnstalled to generate power for the facility.
The control device lnformagon for the control of pollutants for thls source ls llsted below and
included on page 6, Sectlon II.A.3 of the AO.
Table 2-1
Control Devlce
2.2 Flue Gas SamPling Locations
Informatlon regarding the sampllng locatlons ls presented ln Table 2-2 below'
Table 2-2
Sampllng Locatlon
All sample locatlon were verlfied ln the fleld to conform to EPA Method 1. See Appendlx A.1
for more lnformation.
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Document #: cPo81 AS-040, *l'ifiti ;
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2.3 Operating Conditions and Process Data
Heber Llght and Power operates the power generatlng facltlty ln Heber, Utah. The power ls
generated uslng both natural gas fired and dleselflred lntemal combustlon englne
generators, whlch in turn emit pollutants into the atmosphere. This faclllty can generate
power for lts own customer use or for use by other members of the Utah Assoclation of
Municipal Power Systems (UAMPS). The generator englnes were fired on natural gas for the
testlng perlods.
Plant personnel were responslble for establlshlng the test condltlons and collectlng all
appllcable unit-operatlng data. The process data that was provided ls presented in Appendtx
B. Data collected includes the followlng parameters: .
. Englne Operating Data, lncludlng:
. Engine Power, Unit 2 - 1,350 kW
Document #: GP081 AS-OrOr rr:ffi 8792
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
informatlon regardlng specific appllcatlons or modlficatlons to standard procedures is
presented below.
3.1.1 EPA Method 1, Sample and Vetocity Traverses for Stationary
Sources
EpA Method 1 is used to assure that representative samples or measurements of volumetrlc
flow rate are obtalned by dividlng the cross-section of the stack or duct into equal areas,
and then locatlng a traverse point wlthln each of the equal areas' Acceptable sample
locations must be located at least two stack or duct equivalent diameters downstream from
a flow dlsturbance and one-half equivalent diameter upstream from a flow dlsturbance'
Each sampllng locatlon met these criterla'
3.L.2 EPA Meth od 2, Determination of stack Gas veloctty and
Volumetric Flow Rate (Type S Pitot Tube)
EpA Method 2 ls used to measure the gas veloclty using an S-type pitot tube connected to a
pressure measurement devlce, and to measure the gas temperature uslng a callbrated
thermocouple connected to a thermocouple lndlcator. Typlcally, Type s (stausschelbe) pltot
tubes conformlng to the geometrlc speclficatlons in the test method are used' along wlth an
lncllned manometer. The measurements are made at traverse points specified by EPA
Method 1. The molecular welght of the gas stream ls determlned from independent
measunements of Oz, COz, and moisture. The stack gas vOlumetric flow rate is calculated
uslng the measured average veloclty head, the area of the duct at the measurement plane'
the measured average temperature, the measured duct statlc pressure, the molecular
welght of the gas stream, and the measured molsture'
Pertinent lnformatlon regardlng the performance of the method is presented below:
r Method OPtlons:o S-type pltot tube coefficient is 0'84
o Method ExcePtlons:
o Flow traverses were conducted twlce during each test run to represent the
flow rate for the entire test run. The first traverse was done prior to the
beglnning of each run, and the second traverse was done at the conclusion of
the run.
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Document #: GPo81 AS-*r't rEHi-TJr', ;
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3.1.3 EPA Method 4, Determination of Moisture Content in Stack
Gas
EPA Method 4 is used to measure the molsture content of gas streams. Gas ls sampled at a
constant sampllng rate through a probe and implnger traln. Molsture is removed uslng a
serles of pre-weighed implngers contalnlng methodology-specific liqulds and silica gel
lmmersed ln an lce water bath. The lmpingers are welghed after each run to determlne the
percent molsture.
Pertlnent lnformatlon regardlng the performance of the method ls presented below:
. Mlnimum Requlred Sample Volume: 21 scf
. Method Optlons:
o Alt-009 was used for post-test meter callbratlon.
The typlcal Methods 2 and 4 sampling system ls detalled ln Ftgure 3-1.
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Document #: GP08 1 AS-040 128-RT -1 6Z 2
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Document #: GP081 AS-ooo,r r!-Hf-tu'i ;
Flgure 3-1
EPA Mgthoda 2 and 4 Sampllng Traln
IHERilOCOT,PLE/ PROBE
/SAMPLE LINE
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TYPE'S'
PITOT
TIANOMETER +- VACUUM
- LINE(ffiadb)
BY.PASS VALVE
@r*f,)
ERM
J
OCOUPLES
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3.L"4 EPA Methods 3,A, 7E, and 1O, Determination of Oxyg€tr, Carbon
Dioxide, Nitrogen Oxides, and Carbon Monoxide
Concentrations in Emissions from Stationary Sources
(Instrumental Analyzer Procedures)
Concentratlons of Oz, COz, NOx, and CO are measured simultaneously uslng EPA Methods
3A,7E, and 10, whlch are instrumental test methods. Conditioned gas ls sent to a series of
analyzers to measure the gaseous emlsslon concentratlons. The performance requlrements
of the method must be met to valldate the data.
Peftlnent lnformation regarding the performance of the method ls presented below:
o A dry extractive sampllng system is used to report emissions on a dry
basls.
o A paramagnetlc analyzer is used to measure Oz.
o A nondlspersive lnfrared analyzer is used to measure COz
o A chemllumlnescent analyzer ls used to measure NOx.
o A gas fllter correlatlon nondlspersive infrared analyzer ls used to
measure CO.
o NO and NOz are measured separately and summed to report NOx
emlssions.
o Gas stratlflcation testlng was performed across a grld of 3 points
located L6,7o/o, 5O.Oo/o, and 83.3olo of each traverse line determined
uslng EPA Method 1 tn accordance wlth 40 CFR part 60, Appendlx B.
Stratlffcation testlng was performed for three mlnutes per tmverse
polnt. As dlluent and pollutant concentratlons were withln 5olo of thelr
mean concentratlons, subsequent testlng was performed at a slngle
polnt at the centroidal area of the stack exhaust.
The typical sampling system ls detailed in Figure 3-2.
Page # '13
Document #: GP08 1 AS-04O128-RT -1 612
Flgurc 3-2
EPA t{ethodi3Ar7E, and 1O Sampllng Train
3.2 Process Test Methods
The test plan dld not require that process samples be collected durlng this test program;
therefore, no process sample data are presented ln thls test report.
' rultdRgilGrli,WIAF.oWOOIB
VAVE
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Document #: GP081 AS-ooor rBffi-tJ/,
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4.O Test Discussion and Results
4.1 Field Test Deviations and Exceptions
No field devlatlons or exceptions from the test plan or test methods were idengfied by the
project manager durlng thls test program.
4.2 Presentation of Results
The average results are compared to the permlt llmlts ln Table 1-2. Emlsslons are reported
in unlts conslstent with the emissions limlts llsted in Section II.B.2.a of UDEQ Approval
Order DAQE-AN108840013-24. Addltlonal lnformatlon ls lncluded ln the appendlces as
presented In the Table of Contents.
5.O fnternal QA/QC Activities
5.1 QA/QC Audits
EPA Methods 3A, 7E and 10 callbratlon audlts were all wlthin the measurement system
performance speclftcations for the calibration drlft checks, system calibrafion blas checks,
and callbratlon error checks, except where noted ln Secflon 5.2.
The NOz to NO converter efflclenry check of the analyzer was conducted per the procedures
ln EPA Method 7E. Sectlon 8,2.4. The conversion efflclenry met the criterla, except where
noted ln Section 5.2.
5.2 QA/QC Discussion
All QA/QC crlteria were met durlng thls test program.
5.3 Quality Statement
Montrose is quallfled to conduct thls test program and has establlshed a quallty
management system that led to accredltatlon wlth ASTM Standard D7036-04 (Standard
Practlce for Competence of Alr Emlsslon Testlng Bodles). Montrose partlclpates in annuat
functlonal assessments for conformance wlth D7036-04 whlch are conducted by the
Amerlcan Assoclatlon for Laboratory Accredltatlon (A2lA). Al! testlng performed by Montrose
ls supervised on slte by at least one Quallfled Indlvldual (QI) as deflned tn D7036-04
Section 8.3.2. Data quality objectives for estlmatlng measurement uncertalnty wlthln the
documented llmlts in the test methods are met by uslng approved test protocots for each
proJect as defined ln D7036-04 Sections 7.2.L and 12.10. Addltlonal quatity assurance
lnformation ls lncluded ln the report appendices. The content of thls report ls modeled after
the EPA Emlsslon Measurement Center Guideline Document (GD-043).
Page # 15
Document #: GP081 AS-0401 2g-RI -1 67 2
Appendix A
Field Data and Calculations
Document #: ePo81AS-Mol rBHi-tJi ;
Appendix A.1
Sampling Location
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I Document #: G P08 1 AS- *o. rl?&l I ll,
t nlttz
Stack Or.wlng E Trrvarac Polnt Locatbn
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Caent Hrb.tl-b!llPoE
Ciry / Stsl: H.b.r. UT
Sqrco: Ufln *l
Jobi\b.0
DEb:7l11NU
lrpdBy: ChoynsyOuYrm
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Document #: GPO81 As-o4or r!f;i-tJi ;
orTnrl!.: vaoctY ff Prltlodrt.:Port l\rp.
$rd(Aru, Ff:
Xurbar otPort:
L.ndh dPoG klctE:
Tolrl Nunt- of TnYrm Polrtt:
a
LCtl
2
to
te
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PohNo. hdl- hdr6
liollt{cHE8
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tC7 t&7
17.6 20.5
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' AtFra.d pohlf dhnrt r S 24' no Poft Glo..rlhm 0.5 hcn
St ct Omdtr bd![al lAZ hchi ]ilrmm pohtr ln E i
a pohtt p.t poil fth! E , 2 .lrrrtrt dos'natram.td
updl.Ir ctttrh lr rrt
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MONTROSE AIR QUALITY SERVICES, LLC.
6823 South 3600 West
Spanish Fork, UT 84660
Cvelonic FIow Detormination
rr.r, Hfrsar- L-/ P pro 11o. P*4,J
rmnm U^'tl 4 ?-* Vnfzq
Ber.Prcra (W L4-L8
Pftotrubc(Ci Z'A (0,84\StackDimcnclo* 14'S o
Average Angle
Pitot Tubcr Initi ^1, lr- -
/s---
,/PttotTubcrPort:A- ' .R=7-
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Atb.T.tp.'rZ5o F
'b*/[0.<bi
Page # 19
Document #: GP081AS-0401 28-RT-1 672
Appendix A.2
Emissions Test Results
Document #: GP081 AS{mr r[Hf-tfr%
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Montnse Alr Quallty Services, LLC.
6823 S. 3600 W. 801-79+2950
Spanish Fork, Utah 84660
TABLE 4.I.3
(FTELD AND I-ABORATORY DATA SUMMARY)
Plant: Heber Light & Power
Source: Unit 2
Method: EPAlt4
Date:711712024
Symbol Description Test#l Test#2 Test #3
dcf
"Hg
"Hzo
t
I
Vm Volume Dry gas
Sampled @ Meter
ConditionsPu", Barometric Pressure
AH Average Pressure
Drop Across the
Oriflce Meter
h Ave.Gas Meter Temp.
Tm Ave.Gas Meter Temp.
Y Meter CoefficlentVw TotalH20 Collected,
lmpingers & Silica GelCOz Orsat Analysis
02 Orsat Analysis
Nz + CO Orsat Analysis
t Stack Temperature
T" Stack Temperature
Sqrt AP Vebcity Head of
Stack Gas
Pltot Tube Coefficient
Static Pressure
Absolute Pressure
Stack Area
Stack diameter
Net Time of Test
6.6
9.8
83.6
801
1,261
0.7765
0.84
-0.22
24.66
2.07
19.5
60
41.858
24.68
1.3
80
540
1.016
104.0
5.9
10.9
83.2
798
1,258
0.7808
0.84
-0.22
24.66
2.07
41.051
24.68
1.3
81
541
1.016
97.6
6,3
10.4
83.3
800
'1,260
0.7n1
0.84
-0.22
24.66
2.07
19.5
60
42.365
24.68
1.3
Average
41.758
24.68
1.3
83
543
1.016
101.0
6.3
10.4
83.4
799
1,259
0.7781
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F
"R
dimensionless
g
o/o
oh
olo
OF
OR
"Hzo
dimensionless
"Hzo
"Hg
F(
inches
minute
87
547
1.016
101.5
0.84
4.22
24.86
2.O7
19.5
60.0
19.5
60
cP
Pe
P!
Ar
0
Tr
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-6-
Page#21
Document #: GP081AS-0401 28-RT-1 672
Montrose Alr Quality Servlces, LLC.
6823 S. 3600 W. 801-794-2950
Spanlsh Fork, Utah 84660
TABLE 4.I.4
(CALCU!-ATED COMPLIANGE CRITERIA)
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Plant: Heber Lisht & Power
Source: Unit 2
Method: EPA #4
Dale:711712024
Descriotion Test#1 Test#2 Test #3
V,r Volume of Gas Per dscf/min
Minute @ Dry Condtions
Vmrro Volume of Dry Gas dscf
Sampled @ Standard
Conditions
V, co Volume of Water Vapor scf
in Gas SampleB- Proportion by Volume of
Water Vapor in Gas Stream
Dry Molecular Weight lbflb mole
Wet Molecular Weight lb/lb mole
Stack Gas Velocity ll/sec
Volumetric Flow Rate dscf/h
Dry Basis @ Standard dscf/min
Conditions
Alt 009 Post Meter Cal, yqa
% DlffiErcnce, Callbratlon must be within 5% of
orylnal Y Factor
1.0357 1.0562
-2,370/o
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M6
M!
%
Q.a
0.574
34.419
4.895
0.125
29.38
27.9e
75.7
171,196
2,853
0.562
33.693
4.594
0.120
29.42
28.05
75.3
170,889
2,848
0.573
34.409
4.778
o.122
29.45
28.05
75.2
170,328
2,839
1.0284
Average
0.570
34.174
4.756
0.122
29.42
28f2
75.4
1701804
2,U7
Average:
1.0401
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Docu ment #: c Po8 1 AS-o4o "lfl? i:i' I
-7-
Appendix A.3
Field Data
Page#23
Document #: GP08'l AS-04O128-RT -'1672
NOx
N()r
Gurour Eml!8lona SummerY
Gomprny : Hcber Ught & Porer
DtG..:. 711712021
Soutcc: Unltf2
Slb R.tlng: 1,350 kW
Flow Rete Datr
Runtt 1.7'llf+O5 DSCFH
Runt2 1.7098+05 D8CFH
Run lil 1.703E+05 DSCFH
Gusour Ernlslonr
Run *l
113.3 ppmrrd (uncomdcd) CO
't14.1 ppmvd (ddft coredcd)
2.333 lbs/hr
EtlllS
118.2 ppmvd (unconadcd) CO
118.7 ppnvd (dttlt corccicd)
2.122 |Diolhr
Run 13
125.9 ppmvd (unconcc{cd) CO
126.4 ppmvd (drilt coredcd)
2.57'1 lbCtrl
1,226 kW
8.0 ppmvd (uncornrcted)
7.9 ppmt d (ddft consctcd)
O.(DE lba/hr
1,228 kW
5.3 ppmvd (uncorcd)
5.1 ppmvd (drlt concded)
0.0&{ lb6/hr
1,222 kW
3.5 ppmrd (unconcded)
3.3 ppmvd (drlft corscfed)
0.(X1 lbdhr
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6.1
6.1
O2
&I
NOx
(opml
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Plant
Source
Date
Run
TONTROSE AIR QUALIW SERVICES, LLC.
6823 South 3600 West 801-266-7111
Spanish Fork, Utah 84660
Heber Light & Power
Unit#2
07n7n4
Run #1
Dato and
Tlme
71171247:47
71171247:48
71171247:49
7117D47:5O
71171247:51
71171247:52
7117D47:53
711711247:il
71171247:55
7117fi247:66
7l'171247:57
71171247:58
71171247:59
7117124 8:0O
7117124 8:O1
7117P4 8:O2
7117124 8:,03
71171248:M
7117fi24 8:O5
71171248:.6
71171i24 8:O7
7117124 8:OB
71171i248:09
7117124 8:'lO
7117124 8:11
7117D4 8:12
7117fi24 8:13
71171124 8:14
7117fi24 8:15
7117D48:16
7117124 8:17
7117f24 8:18
71171248:19
7117124 8:2O
7117124 8:21
7117D4 8:22
7117124 8:23
7117t24 8:24
115.8
116.5
112.3
110.5
111.6
112.4
113.0
112.7
110.6
113.2
1't3.5
113.6
107.7
114.1
111.9
109.8
109.2
110.0
109.9
111.2
110.0
108.2
113.3
108.3
105.4
1cp..7
99.8
97.9
105.4
118.8
119.9
114.0
114.3
115.0
115.5
115.4
117.2
116.3
co
lopm)
7.8
7.8
7.8
7.7
7.8
7.7
7.9
8.3
9.0
9.0
8.9
8.9
8.9
8.8
8.8
8.8
8.8
8.7
8.7
8.7
E.7
8.7
8.6
8.5
8.4
8.3
8.2
8.1
8.2
8.2
8.0
7.9
7.8
7.8
7.9
7.9
7.8
7.8
13.0
13.0
13.0
13.0
13.0
13.0
12.9
11.6
10.7
10.7
10.7
10.7
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.6
10.7
10.6
10.7
10.6
10.6
10.6
10.6
10.7
Goz
CIt)
4.7
4.8
4.8
4.8
4.8
4.8
4.8
5.6
8.1
6.1
6.1
6.'l
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
Page#25
Document #: GP081 AS-0401 28-RT-1 672
7117fi24 8:25
71171248:26
71171248:27
7117124 8:28
7n7n48'.29
7117124 E:3O
7117D48:31
7l'17D48:32
7117248:33
7117D48:34
7117124 8:35
71171248:36
71171724 8:37
7117fi24 8:38
7n7n48'.39
7117fr24 8:40
7l'17824 8:41
71171248:42
7117f248:43
71171248:4
71171248:45
7l'17f24 8:46
115.3
115.9
'115.4
117.',|
115.3
116.0
116.0
114.5
115.3
115.6
117.4
116.3
116.9
116.1,'1a.7
117.2
116.5
117.7
'l'17.0
117.4
116.1
118.0
113.3
7.8
7.7
7.7
7.7
7.7
7.6
7.5
7.4
7.4
7.5
7.4
7.3
7.3
7.3
7.2
7.2
7.2
7.1
7.1
7.1
7.1
7.O
8.0
10.7
10.7
10.7
10.7
10.7
'10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.7
10.6
10.6
10.6
'10.7
10.7
10.9
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.0
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
6.1
5.9
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Docu ment #: G P08 1 AS-oool rB-Tf-tfru, ;
NOr
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UONTROSE AIR QUALITY SERVICES, LLC.
6823 South 3600 West 801-266-711'l
Spanish Fork, Utah 84660
Plant: Heber Light & Power
Source: Unit#2
Date: 07nln4
Run: #2
Date and
Tlme
7117124 9:O7
71171249:08
7117124 9:O9
7117tr49:'10
7117124 9:11
71171249:12
7117124 9:13
71171i249:14
7l'17D4 9:15
7117fi24 9:16
7117fi24 9:17
7117124 9:18
7117D49:19
7117124 9:2O
71171249:21
71171249:22
7117D49.,23
71171249:24
711711249.,25
7117P.49:26
71171124 9:27
7117D49.,28
71172.49:29
7117D49:30
71171124 9:31
71171249:32
7117fi24 9:33
71171249:*
7117124 9:35
71171249:36
71171249:37
71171249:38
7117l/249:39
71171249:40
7117D49:41
71171124 9:42
7117f24 9:43
7117124 9:44
'l13.7
115.6
115.2
116.0
116.8
115.9
115.7
116.1
115.9
116.3
118.3
118.2
118.0
118.3
116.8
115.9
117.6
116.6
118.0
118.1
119.4
115.2
115.3
117.8
119.'t
117.8
120.2
120.5
118.5
115.4
1',17.3
121.3
120.6
117.7
120.9
121.4
121.3
121.2
co
(onml
6.4
6.3
6.3
6.3
6.2
6.2
6.2
8.2
4.2
6.2
6.1
6.1
6.0
6.0
5.9
5.9
5.9
5.8
5.8
5.7
5.7
5.6
5.6
5.6
5.6
5.5
5.4
5.4
5.3
5.2
5.2
5.2
5.2
5.1
5.1
5.1
5.0
5.0
10.4
10.4
10.4
10.4
'10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.5
10.5
10.5
10.4
10.5
10.5
10.5
10.5
10.5
'10.5
10.4
10.4
10.4
10.5
10.4
10.4
10.4
10.4
10.4
10.5
10.5
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
02 coz
IE} O6T
6.3
6.3
Document #: G P08 1 AS- OOO,| rrl?&i I 31,
71171249:45
71171249:46
71171249:47
7l'17D49:48
7117f249:49
7117D49:5O
7117124 9:51
71171249:.52
7117D49:53
71171249:il
71171249:.55
71171i249:56
7117D49:57
71171249:58
7117fi249:59
7117D4'lO:00
7l,1712410:01
7l'1712410:02
7117112410:O3
7117f2410:M
7117D41O:O5
7t't7D410:6
Average:
119.4
117.5
118.9
120.1
119.8
119.4
121.9
118.6
119.3
121.5
116.5
117.8
116.7
116.5
117.4
118.7
120.1
119.2
119.2
120.4
120.4
118.9
118.2
4.9
4.8
4.8
4.8
10.5
10.5
10.5
10.5
10.4
10.5
10.4
't0.5
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.4
10.5
10.5
10.5
10.5
10.5
10.4
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6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.3
6.2
6.2
6.2
6.2
6.2
6.3
4.8
4.7
4.7
4.6
4.6
4.5
4.5
4.5
4.4
4.5
4.4
4.4
4.4
4.4
4.3
4.3
4.3
4.2
5.3
Document #: GP08 1 AS-OOO',t rB-Hf-tfrt,
;
NOx CO 02(ooml (oom) (!(t
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6.6
6.6
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MONTROSE AIR QUALITY SERVIGES, LLC.
6823 South 3600 West 801-266-7111
Spanish Fork, Utah 84660
Plant : Heber Llght & Power
Source: Unit#2
Date: 07117n4
Run: #3
Date and
Tlme
7117D410:19
711712410:20
7117t2410:21
711712410:22
711712410:23
71171241O:24
711712410:25
7117D410:26
711712410:27
7117112410:28
711712410:29
711782410:30
7117112410:31
711712410:32
7117124'10:33
7117fi2410:il
7117D41O:35
7117D41O:36
7l'l7D410:37
711712410:38
711712410:39
7l'17112410:40
711712410:41
711712410:42
711712410:43
71171i241O:4
711712410:45
711712410:46
7117D410:47
7117D410:48
7117D410:49
7117112410:50
71171241O:51
7117D410:52
711712410:53
711712410:il
711712410:55
71171241O:56
125.3
126.6
127.3
126.7
127.0
128.8
129.5
122.9
128.5
124.2
122.0
126.1
128.4
124.9
125.6
127.9
127.O
126.7
128.1
126.2
128.3
126.2
127.6
128.2
127.4
126.4
126.7
127.2
127.6
126.0
128.0
129.0
124.9
125.9
124.2
124.4
125.1
126.O
4.O
4.0
3.9
3.9
3.9
3.9
3.9
3.8
3.E
3.8
3.7
3.7
3.8
3.7
3.7
3.7
3.7
3.7
3.7
3.7
3.6
3.6
3.6
3.5
3.5
3.5
3.5
3.5
3.5
3.5
3.5
3.5
3.4
3.4
3.4
3.4
3.4
3.3
9.8
9.8
9.8
9.9
9.9
9.8
9.8
9.9
9.8
9.9
9.8
9.8
9.8
9.E
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.9
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
Coz
&l
o.o
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
Page # 29
Document #: GP081 AS-040128-RT -1612
7117D4 10.57 127.2
7117f2410:58 127.0
711712410:59 126.6
7117D411:00 126.1
7117f2411:01 128.0
711712411:02 126.4
711712411:03 126.6
711712411:04 124.2
711712411:05 127.1
7117t2411:06 122.6
7117/2411:07 123.8
711712411:OB 124.9
711712411:O9 125.8
7117112411:10 '125.1
7117fi2411:11 123.6
711712411:'12 124.4
711712411:13 122.7
7117D411:'14 122.8
7117124'11:15 123.9
711712411:16 123.5
7117112411:17 122.3
7117f2411:18 122.0
Average: 125.9
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6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
6.6
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
9.8
3.4
3.4
3.4
3.4
3.3
3.4
3.4
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.2
3.2
3.2
3.2
3.2
3.1
3.1
3.1
3.5
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Document #: Gp08 1 AS-ooo't r!-Hi-tfr% I
Stop
Start
Rate
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Montrose Air Quality Servic€s, LLC.
6823 South 3600 West
Spanish Fork, Utah 84660
801-794-2950
FIELD DATA
1 Plant
2 City
3 Stack Name
4 Operator
5 Date
6 Reference Method
7 Run#
8 Stack Diameter - $
9 Stack Area - A"
10 Sample Box Number
11 Meter Box Number
12 MeterAH@
13 Meter Calibration - Y
14 PitotTube -Co
15 Probe Length
16 Probe Liner Material
17 Probe Heater Setting
18 Ambient Temperature
19 Barometric Pressure - P6",
20 Stack Gas Pressure - P,
21 Static Pressure - Po
22 CFador
23 Reference ^P
24 Thermometer Number
25 Pretest Leak Rate
26 LeakCheckVacuum
27 Gas Analysls
28 lnitial Leak Check good
Heber Light & Power
Heber, Utah
Unit 2
Joe Avila
7t't7t2024
EPA #4
1
19.5 inches
2.07 square feel
APEX
xc-522t10
1.708
1.016
0.84
z',-A
Stainless Steel
248
65
24.68
24.66
-0.22
0
0.63
#2-A
0.000
19
feet
OF
OF
inches Hg
inches Hg
inches H20
inches H20
cfm
inches H20
Pitot Tubes1007.87 A= OK1007.87 B= OK
Vac= 19
Pm 24.78
EPA Method 4 RUN #1 Pagelof 5
Page # 31
Document #: cP08 1 AS-040 128-Rf 4 67 2
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0.77
o.74
0.69
0.65
0.59
0.65
0.67
0.73
0.89
0.89
0.81
0.73
0.71
0.88
0.99
1.05
0.78
0.59
0.55
0.48
0.42
0.35
0.42
0.45
0.53
0.8
0.79
0.66
0.54
0.5
0.78
0.98
1.1
o.62
0.78
0.77
0.66
0.66
0.62
0.63
0.65
o.74
0.90
0.87
0.81
0.71
0.69
0.90
1.05
1.10
0.78
Point #
1 0.61
2 0.59
3 0.44
4 0.43
5 0.386 0.4
7 0.42
8 0.55
I 0.81
10 0.76
11 0.65
12 0.51
13 0.48
14 0.81
15 1.1
16 1.2
Pre-Teet and Post-Test Velocitiee
Post-Test #'l
Time:850
Stack Temp : 800
Post-test AP Sq, Root APSq. Root AP
Pre-Test #l
Time: 735
Stack Temp : 796
Pretest aP
Average =
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Docu menr #. c Po8 1 AS-*r r rB-Hf-f .ti,
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EPAMethod4RUN#1 Page2of5
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Outlet
fF)
67
69
69
71
74
77
80
82
84
84
83
82
lnlet
cF)
68
72
75
78
82
86
88
89
89
90
90
91
t,
fF)
798
797
799
800
800
799
799
799
795
799
799
800
Sample
Point
Starting
,|
2
3
4
5
6
7
8
I
't0
11
12
vm
scf
1008.28
101 1 .76
1015.25
1018.75
1022.25
1025.76
1029.26
1032.76
1036.25
1039.75
1043.26
1046.75
1050.138
Gas
Volume
difference
scf
3.48
3.49
3.50
3.50
3.51
3.50
3.50
3.49
3.s0
3.51
3.49
3.39
Moter Meter Stack Meter Gas
Temperature Temperature Temperature Volume
avg "F
avg'R
total =
average = 76.83
Meter
80.00 798.67540.00 1258.67
83.17 798.67Meter Stack
Temperature Temperature Temp ('F)
Outlet ("F) lntlet ("F) ts
41.86
Gas
Volumev.
41.86
Gas
Volume
vm
EPA Method 4 RUN #1 Page3of 5
Page # 33
Document #: GP081AS-040128-RT-1612
Pressure
Difference
AH
(inches H20)
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
Sampling
Time
(min)
5
5
5
5
5
5
5
5
5
5
5
5
(24 hrs)
747
752
757
802
807
812
817
822
827
832
837
u2
847
Clock
Time
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fF)
66
&t
63
63
64
61
61
60
63
il
64
65
fF)
251
256
252
258
25',1
253
253
253
zil
2il
253
254
248
249
251
252
251
252
253
250
252
251
250
252
4
4
4
4
4
4
4
4
4.5
4.5
4.5
4
Probe Filter lmpinger
Temperature Temperature Temperature
Exit OutletExii
(inches Hg) fF)
1.30
Pressure
Diff
AH
60
5
Sampling
Time
4.13
Vacuum
2s0.92
Probe Exit
60
Clock
Time
253.50 63.17Filter Outlet lmPinger
Temperature Temperature Temperature
("F) CF) fF)
Document #: cPo8lAs-040rz!ffi-t#'
;
EPAMethod4 RUN#1 Page4of 5
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Svmbol
vm
Vmrto
Vme
V,.!aa
vw
Bws
Md
M!
co
Coe
O2
N2
AH
T.
Tr #1
Sqrt AP"* #1
vr#1
Q"
Qro #1
Qsw
Final Leak Check
TEST RESULTS
Descriotion
Volume of Gas Sampled by Dry Gas Meter
Dry Gas Volume at Standard Conditions
Volume of Gas per Minute @ Dry Condtions
Volume of Water Vapor in the Gas Sample
Total Moisture Collecled in lmpingers and Silica Gel.
Water Vapor in the Gas Stream, Proportion by Volume
Dry Molecular Weight
Wet Molecular Weight
Carbon Monoxide Concentration in Stack
Carbon Dioxide Concentration in Stack
Oxygen Concentration in Stack
Nitrogen Concentration in Stack
Average Pressure Dlfferential Across Meter O rifi ce
Average Meter Temperature
Stack Temperature:Pretest - Run #1
Average sqn AP: Pretest - Run #1
Stack Velocity:Pretest - Run #1
Actual volumetric flow rate
Stack Flow Rate: Pretest - Run #1
Wet Gas Volume at Standard Conditions
Stop 1050.185Start 1050.185Rate 0
Vac =
Pitot Tubes
A= OK
B= OK
I
Units Value
1
2
3
4
5
6
7
8
I
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
dcf 41.858
dscf 34.419
dscf/min 0.574
scf 4.895
s 104.0
0.125
lb/lb mole 29.38
lbflb mole 27.96
o/o 0
o/o 5.9
% 10.9o/o 83.2
inches H2O 1.3oR 540
"F 7gg
0.7808
75.7
ft"/hr 5.6519E+0s
dscf/hr 1.7120E+05
wscf/hr 1.9554E+05
Alt 009 Post Mebr Gal,
Run #l : 1.0357
Average: 1.0401
olo Dlfi: -2.37o/o
Page # 35
Document #: GP081AS-040128-RI-1672
EPA Mathod 4 RUN #1 Page5of 5
Montrose Air Quality Seruices, LLG.
6823 S. 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Molsture Data
EPA Method 4
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Com pany: He!et!E!!4!qwgt Run Number: 1
Sampling Location:Unit 2
lnitialWeight
686.9
618.2
783.4
Moisture Collected
FinalWeight
674.2
747.1
655.7
807.5
Dale:711712024
Weight Gain
-12.7lmpinger 1
lmpinger 2
lmpinger 3
lmpinger 4
55.1
37.5
TotalGain (V*) =104
24.1
Docu ment #: G P08 1 AS-*r't rB-Hi-Tfri
;
Company: Heber Light & Power
Montrose Air Quality Services, LLC.
6823 S. 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Run Number: 1
Date:711712024
Gas Analysis
(Average of 3 analyses each)
Sampling Location: Unit 2
Volume Percent - Dry Basis
CEM Run
#1 N2 o2 Coz CO
1 83.2 10.9 5.9 < 0.01
2 83.2 10.9 5.9 < 0.01
3 83.2 10.9 5.9 < 0.01
Average 83.20 10.90 5.90 < 0.01
o2
34.3o/o when 02 24.0o/o
<0.2o/o when 02 <4.0%
Coz
30.3o/o when CO2 s15.0%
30.2o/o when CO2 215.0o/o
co
< 0.3%
Page # 37
Document #: GP081AS-040128-RT-'1672
Montrose Arr Quality Services, LLC.
6823 South 3600 West
Spanish Fork, Utah 84660
801-794-2950
FIELD DATA
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Stop
Start
Rate
1 Plant
2 City
3 Stack Name
4 Operator
5 Date
6 Reference Method
7 Run#
8 Stack Diameter - $
9 Stack Area - &
10 Sample Box Number
11 Meter Box Number
12 MeterAH@
13 Meter Calibration - Y
14 PitotTube - Co
15 Probe Length
16 Probe Liner Material
17 Probe Heater Setting
18 AmbientTemperature
19 Barometric Pressure - P5",
20 Stack Gas Pressure - P"
21 Static Pressure - Pn
22 C Factor
23 Reference ^P
24 Thermometer Number
25 Pretest Leak Rate
26 LeakCheckVacuum
27 Gas Analysis
28 lnitial Leak Check
Heber Light & Power
Heber, Utah
Unit 2
Joe Avila
7t17t2024
EPA#4
2
19.5
2.07
APEX
xc-5221'lo
1.708
1.016
0.84
2',-A
Stainless Steel
248
73
24.68
24.66
-0.22
0
0.62
f2-A
0.001
18
50.375
50.374
0.001
Vac =
Pm
inches
square feet
feet
OF
OF
inches Hg
inches Hg
inches H20
inches H20
cfm
inches H20
Pitot Tubes
A= OK
B= OK
18
24.78
Docu ment #: GPos 1 AS-ooo r rtt-Hi-tfrt,
;
EPA Method 4 RUN tt2Page 1 ot 5
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Pre-Test and Post-Test Velocltles
Pre-Test #2
Time: 850
Stack Temp: 800
Tmverse Pretest AP
Point#
Poet-Teet #2
Time: 1012
Stack Temp: 799
PosttestAP Sq. RootaP
0.75 0.87
0.65 0.81
0.56 0.75
0.52 0.72
o.72 0.85
0.85 0.921.1 1.05
1
2
3
4
5
6
7
I
I
10
11
12
13
14
15
16
Average =
0.59
0.55
0.48
0.42
0.35
0.42
0.45
0.53
0.8
0.79
0.66
0.54
0.5
0.78
0.98
'1,1
0.62
Sq. RootAP
0.77
0.74
0.69
0.65
0.59
0.65
0.67
0.73
0.89
0.89
0,81
0.73
0.71
0.88
0.99
1.05
0.78
0.77
0.75
0.70
0.67
0.61
0.62
0.69
0.71
0.92
0.6
0.57
0.49
0.45
0.37
0.39
0.48
0.51
0.84
Average =
Page # 39
Document #: GP081 AS-040 128-Rf -1 67 2
0.78
EPA Method 4 RUN tf2Page2ol S
Sample Meter Meter Stack Meter Gas
Point Temperature Temperature Temperature Volume
Outlet lnlet t6 V,
("F) ('F) ("F) scf
Starting 50.445
1 76 77 800 53.84
2 77 80 801 57.24
3 76 84 799 60.64
4 75 87 800 63.99
5 74 88 799 67.38
6 72 89 799 70.75
7 72 89 798 74.08
8 71 90 797 77.42
9 72 91 797 80.93
10 73 92 797 84.34
11 75 93 798 87.93
12 76 95 798 91.496
Gas
Volume
difference
scf
3.40
3.40
3.40
3.35
3.39
3.37
3.33
3.34
3.51
3.41
3.59
3.57
avg "F 81.00
avg'R 541.00
74.08
Meter
41.05
87.92 798.58Meter Stack Gas
798.58
1258.58
total
aveEge =
41.05
Temperature Temperature Temp ("F) Volume
Outlet ("F) lntlet ("F) t Vm
EPA Method 4 RUN f2 Page 3 of 5
Gas
Volume
V,
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Pressure SamplingDifference Time
AH
(inches H20) (min)
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
601.30 5Pressure SamplingDiff Time
AH
Clock
Time
Probe Filter lmprnger
Temperature Temperature TemperatureExit Exit Outlet
(24 hrs) (inches Hg)
907
912
917
922
927
932
937
942
947
952
957
1002
1007
3.2
3.2
3.2
3.2
3,5
3.5
3.5
3.5
3.5
3.5
3.5
4
('F)
251
249
248
250
251
252
251
250
250
251
251
250
('F)
252
252
251
252
252
2il
252
252
252
254
253
251
('F)
59
55
56
56
57
59
59
59
60
60
62
63
60
Clock
Time
3.44 250.33 252.25 58.75Vacuum Probe Exit Filter Ouflet lmpinger
Temperature Temperature Temperature(.F) ("F) ("F)
EPA Method 4 RUN #2 Page 4 ot S
Document #: cPo81 AS-O4or rEffi-f#
Symbol
1V,
2 Vmeta
3 Vmo
4 V.rgac
5V*
6 Bws
7Mo
8M'
9CO10 coz
11 Oz
12 N2
13 AH
14 Tm
15 T"ffi
16
17 Sqrt AP"," #2
18
19 v,#
20
21 Qa
22
23 Q,a #2
2425 Qsw
26
27 FinalLeakCheck
TEST RESULTS
DescriPtion
Volume of Gas Sampled by Dry Gas Meter
Dry Gas Volume at Standard Conditions
Volume of Gas per Minute @ Dry Condtions
Volume of Water Vapor in the Gas Sample
TotalMoisture Collected in lmpingers and Silica Gel.
Water Vapor in the Gas Stream, Proportion by Volume
Dry MolecularWeight
Wet Molecular Weight
Carbon Monoxide Concentration in Stack
Carbon Dioxide Concentration in Stack
Oxygen Concentration in Stack
Nitrogen Concentration in Stack
Average Pressure Differential Across Meter Orifice
Average Meter Tem Perature
Stack Temperature: Run #2
Average sqrt AP: Run #2
Stack Velocity: Run #2
Actual volumetric flow rate
Stack Flow Rate: Run #2
Wet Gas Volume at Standard Conditions
91.596
91.596
0
Vac =
Pitot Tubes
A= OK
B= OK
9
Units
dcf
dscf
dscf/min
scf
g
lb/lb mole
lb/lb mole
o/o
o/o
o/o
o/o
inches H2O
OR
OF
fUsec
ft'/hr
dscf/hr
wscf/hr
Value
41.051
33.693
0.562
4.594
97.6
0.120
29.42
28.05
0
6.3
10.4
83.3
1.3
541
799.5
0.7771
75.3
U.61949+05
1.7089E+05
1.9419E+05
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Alt-009 Post Meter Cal.
Run #2: 1.0562
Average: {.0401
% Dlff: -2.37oh
EPA Method 4 RUN #2 Page 5 of 5
Document #: GPoslAS-o4ol 2B-ffi-f f,
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Company: Heber Light & Power
Montrose Air Quality Services, LLC.
6823 S. 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Molsture Data
EPA MEthOd 4
Run Number: 2
Sampling Location:Unit 2 Dale:711712024
lmpinger 1
lmpinger 2
lmpinger 3
lmpinger4
lnitialWeight
709.2
690.8
591.2
818.7
Moisture Collected
FinalWeight
765.1
719.5
Weight Gain
55.9 I
g
g
g
g
28.7
8.1
596.1
826.8
TotalGain (V*) =97.6
Document #: G po8 1 AS- o+o t zEHl I a9z
(Average of 3 analYses each)
Company:Heber Liqht & Power
Montrose Air QualitY Services, LLC.
6823 S. 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Run Number: 2
Dale:711712024
Gas Analysis
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Sampling Location:Unit 2 I
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o2
< 0.3% when 02 24.0o/o
<0.2% when 02 34.0o/o
Coz
s 0.30/o when CO2 315.Oo/o
30.2o/o when CO2 >15'0%
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Document #: GP081 AS-O.t',t ZBf;i-t#'
;
Stop
Start
Rate
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Montrose Air Quality Servrces, LLC.
6823 South 3600 West
Spanish Fork, Utah 84660
801-794-2950
FIELD DATA
1 Plant
2 City
3 Stack Name
4 Operator
5 Date
6 Reference Method
7 Run#
g Stack Diameter - Q
9 Stack Area -,\
10 Sample Box Number
11 Meter Box Number
12 MeterAH@
13 Meter Calibration - Y
14 Pitot Tube - Co
15 Probe Length
16 Probe Liner Material
17 Probe Heater Setting
18 Ambient Temperature
19 Barometric Pressure - P5",
20 Stack Gas Pressure - P.
21 Static Pressure - Pn
22 C Factor
23 Reference ^P
24 Thermometer Number
25 Pretest Leak Rate
26 Leak Check Vacuum
27 GasAnalysis
28 lnitial Leak Check
Heber Light & Power
Heber, Utah
Unit 2
Joe Avila
7t17t2024
EPA#4
3
19.5
2.07
APEX
xc-522t10
1.708
1.016
0.84
z',-A
Stainless Steel
248
77
24.68
24.66
-0.22
0
0.62
#2-A
0.001
17
91.771
91.77
0.001
Vac =
Pm
inches
square feet
feet
OF
OF
inches Hg
inches Hg
inches H20
inches H20
cfm
inches H20
Pitot Tubes
A= OK
B= OK
17
24.78
Docu ment #: G P08 1 AS-ooo r rBfff-tfru,
EPA Method 4 RUN #3 Page 1 of 5
II
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t
0.76
0.74
0.72
0.69
0.64
0.60
0.69
0.73
0.92
0.89
0.82
0.74
o.72
0.82
0.94
1.00
0.78
0.58
0.55
0.52
0.48
0.41
0.36
0.47
0.53
0.85
0.79
0.67
0.55
0.52
0.68
0.89
1
1 0.6
2 0.57
3 0.49
4 0.45
5 0,37
6 0.39
7 0.48
8 0.51
I 0.84
Pre-Test and Post-Test Velocities
Pre-Test #3
Time: 1012
Stack Temp : 799
Traverse Pretest AP
Point #
Post-Test #3
Time: 1118
Stack Temp : 802
PosttestAP Sq. RootAP
10
11
12
13
14
15
16
Average =
Sq. RootAP
0.77
0.75
0.70
0.67
0.61
0.62
0.69
0.7'l
0.92
0.87
0.81
0.75
0.72
0.85
0.92
1.05
0.78
0.75
0.65
0.56
0.52
a.72
0.85
1.1
0.62 Average = 0.62
EPA Method 4 RUN #3 Page 2 of 5 Document #: cPo81 AS-o40r rBf;f-TJri
1
3.52
3.51
3.49
3.48
3.47
3.55
3.55
3.58
3.55
3.55
3.56
3.56
42.37
Gas
Volume
v.
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Sample Meter Meter Stack Meter GasPoint Temperature Temperature Temperature Volume
Gas
Volume
ditference
scf
Starting
1
2
3
4
5
6
7
I
I
10
11
12
total
average =
Outlet
('F)
79
79
79
80
80
81
82
82
82
83
83
84
lnlet
("F)
81
85
89
92
94
94
94
95
95
96
96
96
t
("F)
799
800
800
801
801
800
800
801
801
802
802
800
v,,,,
scf
91.82
95.34
98.85
102.34
105.82
109.29
112.U
116.39
119.97
123.52
127.07
130.63
134.185
avg oF 86.71 800,58avg'R 546.71 1260.58
42.3781.17 92.25 800.58Meter Meter Stack Gas
Temperature Temperature Temp ("F) Volume
Outlet ('F) lntlet ('F) t
EPA Method 4 RUN #3 Page 3 of 5
vm
Page#47
Document #: GP081AS-0401 28-RT-1 672
Pressure Sampling
Difference Time
AH
(inches H20) (min)
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
1.3
601.30 5Pressure SamplingDiff Time
AH
Clock
Time
Probe Filter lmPtnger
Temperature Temperature Temperature
t
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t
(24 hrs) (inches Hg)
1019
1024
1029
1034
1039
1044
1049
1054
1059
1104
1 109
1114
1119
Exit Outlet
('F) ("F)
3.9
3.9
3.9
4.2
4.2
4.5
4.5
4.5
4.5
4.5
4.5
4.5
Exit
('F)
249
251
251
250
251
250
251
251
250
250
251
249
67
63
58
59
59
60
60
60
62
63
65
66
251
252
252
253
254
252
252
252
252
254
254
252
60
Clock
Time
4.30 250.33 252.50 61.83
Vacuum Probe Exit Filter Outlet lmpinger
Temperature Temperature Temperature
("F) ('F) ('F)
EPA Method 4 RUN #3 Page 4 of 5
Docu ment #: G P08 1 AS-ooo r r!f;i-tJrt, I
Stop
Start
Rate
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1
2
3
4
5
6
7
8
9
10
1'.|
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
Svmbol
V,
Vrro
Vme
Vvpas
vw
Bws
M6
M"
co
Coz
o2
N2
AH
T,
T" #3
Sqrt APrr" #3
v"#3
Q"
Q'3d #3
Qsw
Final Leak Check
Units
dcf
dscf
dscf/min
scf
g
lb/lb mole
lb/lb mole
o/o
o/o
o/o
o/o
inches H2O
OR
OF
fto/hr
Value
42.365
34.409
0.573
4.778
101.5
0.122
29.45
28.05
0
o.o
9.8
83.6
1.3
547
800.5
0.7765
75.2
5.6178E+05
1.7033E+05
1.9398E+05
TEST RESULTS
Description
Volume of Gas Sampled by Dry Gas Meter
Dry Gas Volume at Standard Conditions
Volume of Gas per Minute @ Dry Condtions
Volume of Water Vapor in the Gas Sample
TotalMoisture Collected in lmpingers and Silica Gel.
Water Vapor in the Gas Stream, Proportion by Volume
Dry MolecularWeight
Wet MolecularWeight
Carbon Monoxide Concentration in Stack
Carbon Dioxide Concentration in Stack
Oxygen Concentration in Stack
Nitrogen Concentration in Stack
Average P ressu re Differential Across Meter Orifi ce
Average Meter Temperature
Stack Temperature: Run #3
Average sqrt AP: Run #3
Stack Velocity: Run #3
Actual volumetric flow rate
Stack Flow Rate: Run #3
Wet Gas Volume at Standard Conditions
134.239
1U.238
0.001
Vac =
Pitot Tubes
A= OK
B= OK
10
Page # 49
Document #: GP081 AS-0401 28-RT-1 672
Alt-009 Poet Meter Cal.
Run #3: 1.0284
Average: 1.0401o/oDlfi: -2.37%
EPA Method 4 RUN #3 Page 5 of 5
Montrose Air Quality Services, LLC.
6823 S. 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Molsture Data
EPA Method 4
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Company: Heber Light & Power Run Number: 3
Sampling Location:Unit 2 Date:711712024
lmpinger 1
lmpinger 2
lmpinger 3
lmpinger 4
lnitialWeight
695.3
693.8
620.3
789.1
Moisture Collected
FinalWeight
721.8
743.6
633.9
800.7
Weight Gain
26.5
49.8
13.6
11.6
TotalGain (V*) =101.5
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Document #: Gpo81 AS-o4o, rB-ffi-f.t% t
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Company: Heber Light & Power
Montrose Air Quality Services, LLC.
6823 S 3600 W.
Spanish Fork, Utah 84660
801-794-2950
Run Number: 3
Dale:711712024
Gas Analysis
(Average of 3 analyses each)
Sampling Location: Unit 2
o2
s0.3% when 02 24.0o/o
<0.2% when 02 34.0o/o
Coz
30.3o/o when CO2 s15.0%
s0.2o/o when CO2 >15.0%
co
< 0.3%
Volume Percent - Dry Basis
Cem Run
#3 N2 o2 Coz CO
1 83.6 9.8 6.6 s 0.01
2 83.6 9.8 6.6 < 0.01
3 83.6 9.8 6.6 s 0.01
Average 83.60 9.80 6.60 < 0.01
Document #: G p08 1 AS-ooo,' rE-Hf-tu9/,
Appendix A.4
Example Calculations
Document #: cPoslAs-o4or r!ffi-t.te I
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SAilPLE CALCUT.ATIOT{S
Clty of tlaber Powur Plant Unlt #2 Generrtor Englna Erhrurt, Run #l
July lf ,2OA
AVERAGE STACK GAS CALGULATIOilS CORRECTED FOR SYsTEf, BIAS VIA U8EPA 7E
Averaoc Gag Effruent CalqJlaton Conccted for S\lsbm Blag Gheck. C .-.: USEPA 7E
Gu Component 02
%vd
Gor
%vd
Nor
nornud
GO
DDTTI'd
C.w 10.9 5.9 t't3.3 8.0
zcro lnltal (Zl)0.1 0.0 0.3 0.3
zcro final (20 0.1 0.2 0.1 0.3
0.1 0.1 0.2 0.3
rDscalc lnltal (Sl)10.2 8.1 101.0 11.9
uplcalc llnal (Sf)10.2 6.1 101.4 12.0
cm 10.2 6.1 101.2 12.0
upscale value (SV)10.07 6.04 101.9 r2.0
Eull
Cg., ' (C.,s ' C") x [G'o f (G'' Gjl
O"Goncerhdon ln Steck Go (oercentl
Cgn D . (10.9-0.1)x110.1 /(10.2-0.1)l
Cro = 10.8 %
GO'Conccntrr0on ln Stack Gas loercentl
Cs-o . (5.9-0.1)x[6.O4l(6.1 -0.1)l
Cs.ns = 5.9 %
ilO- Conccntrrtlon ln 8bck Gu loerte ocr mllllon h volums. dll
Gs-o . (113.3-0.2)x[101.9 l(101.2-0-211
Cgo = 114.1 ppmvd
CO ConcentraUon ln Steck Gm (oailr oer mllllon bu volume. drvl
Css6 I (8.0-0.3)x112l(12.0-0.3)l
Symbol Ilefnltlon
eaYg Average gaE concentreflon from analyzcr, parts par mllllon by volume or pcnrant volumc
Crm Actral concent'aton of the upscale callbration gae (SV), partr psr mllllon by voluma or percent
volume
Average of the inital (Zl) and frnal (Zf) callbration blas ched( resulb for tfie zero gas, parts per
mllllon by volume or percant volumg
cm Average of thc lnltal (Sl) and finel (Sf) callbration blas cfisd( r€sulb furthe upacale calibration
gas, parts per mllllon by volume or percent voluma
Ce-o Averago gas effiuent concentration oorBcfod for aystem blas cficck, partB por mllllon by
volume or percent volume
Csrw Average gas efiuent concantatlon conEcted for aystem blas cfieck, part8 per mlllion by
rrolumc or percent volume
Docu ment #: G P08 1 AS-o4fi 23-Hf-f fz1
Cg-o =7.9
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Docu ment #: G Po8 1 AS-o4o 1 rPe-ffi-t#, I
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SATPLE CALCULAToilE
Clty of Heber Powor Phnt, Unlt#ll Generetor Englne Exhaurt, Run *1
July'17,2021
REAL NTE CONCEilTRATION
'
ETISSION
'
DESTRUCTION EFFICIENCY CALCULANOilS
frrn t
Uelm mbol Deflnlton
5.9 CgrrO COZ Average gas effruent concantaton of CO2, conoc'tcd for ayttem blas cfied<, pcrcent,
dry basis
f4.01 MWcoz Molecrlar rruelght of carbon dioxlde, pounds per pound-mole
111.1 CgrrOHO,Average gae effluent concenfa0on of NO<, corcctad for system biao cfieck, pattr pel
mllllon by volume, dry basls, qJblc fiEst per 106 ctblc fuet of strack gas
46.01 MWrc'Molecular wrlght of nltogcn oxideg, pounda per pound-mole
7.9 CgrrO CO Avcrage gas efiuent concantsaton of CO, conecilad br syttsm blaa dted(, patb per
mllllon by volume, dry baslc, cublc faat per 100 cublc tbet of rteck gae
28.01 MWco Moleanlar uolght ol ca6on monoldde, pounds per poun&mole
0.125 ar.Average Stad< Gas Molature, Percent
20.s 20.9 Percant oxvoen ln amblent air at stendard conditions
10.8 Oe Stack Gas Oxygen, Percent by volume
5.9 Coz Stad< Gaa Carbon Dlodde, Percant, by volume
1.0E6 1.0E6 Parts pcr mlllion, 1 part parametar pcrLOEO partB stad( gas; Cublc fact pcr mllllon
:ublc iect
2853 Q.a Average standard stad( gas f,ow rata conec'ted for molsfure, dry ctandard cubic fr6t
per mlnute
,0 60 Mlnutea oer hour
3Es.3 V Cublc faet of pollutrant per pound-mole ol ideal Ses @ 68 dcgraes Fahrenhclt and
29.92lncfies Mercury
t.1948-07 Qxo,Converslon fador, convertlng parta per mllllon NOx b pounda per atandard cubic fmt
1.660E-07 Qeoz Converglon tEctor, converfing parts per million SOz to pounds per standard cublc fuot
Hr Total sample time, hours (Hr e minutes / 60)
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Poundr oer hour flb/hr)
lMrr r
lMrr =
lMtr =
CO ConcenEr0onr md Eqhdom
Poundr ocr hour (lbfltrl
lblJrr r
lMrr =
lb/lrr =
G!..D lor, l.0EG x Q.6x 60 / V r tWm,
1 14.100 / 1.0E0 x2653 x 60 / 385.3 x46.012.332 lMrr
GgrDco, 1.0EG x Q.6x 60 / V x tW66
7.900 I 1.0E8 x 2E53 x 60 / 385.3 x 28.01
0.09E lb/}tr
Page # 55
Document #: GP081AS-040'128-RT-1672
Urlt 2
HlbGr Uiht & Pow.t
tlrbcr, t t h
tltt Lr,m2t
Rur ll Srmph Crls{tllont
EPA MGthodr l4: Ir.tilmlnrtton of Strct Gc Volumddc flow nna lnd Molrt{ra Contatrt
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Docu ment #: G p08 1 AS-o+o r zB-Hf-f o5zoz I
vtrhbL vrlu.).llnldotr lJnlt o{ MeBolhant
D.'t0.6 !tad( OlamEt r lnchca
2.O7 'n.r-SdMd AM dh Str*fti
P.4.22 itrck St8ilc PDstm ln. HrO
Pr 4.@.;t d( Stetc PBsua ln. H0
%co,5.0 lon@ntrton ol Csrbon Obndo Ory Volum Prcant (%vd)
%o,10.9 loncant afm of O)rygs|Dry Volume Porcant (%vd)
Md 29.3E )ry Mddltr W.lght of th6 Sbck Gar (dcfarlt)lb/lb-rnolr
24.64 lmmtlcPrsm in. Ho
AH 1.30 ,0$m Dlltmndal amrt Of,'fiG in. HrO
P-21.78 dbshr. PEsm et Gs Metar in.Ho
80 TmpcrluG Et Gas Mottr 'F
r.540 \bloMa Tmprillw at Ga! M€ts .R
K1 0.O'17(E lsvaBion Fac'tor ftlmL
1(x.0 y'olumo o, W!16 CmdmEod t
4.89 /dum otWrtuCmdmsad 8C,
rt 17.U londsrn 'R n.Hs
1.0160 l,lrbr CsllbElion Faclot Unruest
,11.858 Volurn of Sbckcsco{.ci.d dcf
3,t..ltg Smpl! GBVolum drd
B.-o.1 25 Stlck O[ Mdltm Content %/too
M.27.8 qcnJal irlol6alar Weloht od th. Stsck Gag lMUmls
P.21.@ qbtolub Strck PE$uF in. Hq
T.798.67 \vm9c Stacl Tomporaturo .F
f 1259 AvrEoc Abroluis Steck T€mmtum
Kp 85.49 ;m6fdon Factor (fusE) x v{(0brEmoloxin.Hg)xf RXln.Hro)))
q 0.8.1 Pilot Cosrncbnt OlmanConlcE!
AwVAP 0.7808 \vcraso Squaro Rot of Vclocity Hud Rrtdhgs In. HrO
15.70 Avmqc Sirck Gs Velodly ll/sc
,160 R itandsd Abrolr.t8 Tmp€Ettm .R
29_t2 itendsrd Ablomo PEsm in. Ho
o 171 18 Vdmeulc Flil Relg Corelgd to .is.l,/ir
K5 0.09,a8 :m3tant (ln.H8.min) /('R tF)
e 60 ;mglr Tlmr m&lut€a
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Unlt 2
Hcbat Ulnt & Poru
H.bd, Ut h
,lrly rr,202a
Rm ll SlrmL Cdol.tlor
EPA IurtM t4r Drt mh.Uotr o, St d G.r Volun.trlc flow i.t and Molttun Contaot
A. dD,Pllr
d19.s/24)^2.2.07tt^2
Pr'P/13'8
- 4.D,113.4
' O.olla.lt
rr.. (0.a4 x %cq) + (o.sa x rq) r 0.28(10o-%cor-9aq)
' (0.44 r 5.9) + (0.32 x 1o.9) r 0.28(lo0 - 5.9 - 10.9)
.29,!tblb-mol.
Pi. Pr r (AtU13.8)
. 2a.68+ (1.3/.t3.6)
r 2a,7t ln Ht
T.. 460 + t-
.480+80
'StOR
Vtt'KtxVt
. O.O47(E x lO4
. alg rc, Ea, +r)
lq xYx V-x P.
T.
. 6 x 4 1.867990090099o x 24.78
540
E:l+4l9dsct (Eq.+:tt
l-. Vs*c
V,461 + V414
t AAI
4.89 + 3i1.42
. 0.125 E/r001 (Ec,.H)
n4' Mcr (l-Bt ) + (18.0x B$)
t (0.44 x 6.9) + (0.32 x 10.9) + 0.26(100 - 5.9 - 10.9) r (l - 0.125) r (18.0 x 0.125). ?.lrlbflt-ml. (Eq.2a)
Pr. PE + P.
= 24.68 r ({.02)
r 2456|n. Ht
T{-tr480+T.
. '160 + 798.666086E66067r 1.iIl9 R
Page # 57
Document #: GP08 1 AS-O40128-RT -1 67 2
Unn 2
Hrbfr tlght & Powrt
H.b.r, Ut h
tr'rytT,Du
Run llsmd. C.kuhdor
€PA ttiiropdr 14. Datrml[Uon ot Strd( 6at volumatrlc f]il n t lnd MoBtura Cantonl
v.. lqrcrxAvgvap x
.85.49x0.44x0.7808x (24.@x27.941-
= 7s.7W* lEq.2-l
q. ?rmox(t.qJxMlx(A)x (I"ixPJ
Ol.u x Por)
= 36@ r (1 - 0. 126) x (76.7) r (2.07) x (460 x 24.88)
. t7,.,r$d!d,lhr
(1259 x 2e.92)
(Eq.2€/
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Document #: GP081 AS-ooOrzEf;i-T*
I
Appendix B
Facility Process Data
IIIIIIItIItIIIIIII
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Appendix C
Quality Assu ra nce I Quality Contro!
Document #: GP08'IAS-*OI r!-Hi-f *
|
Appendix C,1
Units and Abbreviations
Page # 65
Document #: GP081 AS-04O128-RT -1672
66AtgN,I*?p"H
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lccl
tdt
oF
oR
" Hro
13.0
AH
AP
e
us
Pr
fir
actrn
&
&
Bfuq-
c.
CAo
cDr
c{ord
Gfin
cc..
Gx
qll ormt
cu,r
%
cp
c.
cs
Cg
c"/
D
dcf
dcrn
Dn
Dr
dscf
dscfrn
dgcnr
F6
0m
Fs
ftf
s
98lgr
grldsd
hr
UNITS AND ABBREI'IATIONS
oon€dEd to X% oxygen (coneded fordlluton alr)
abaolub value ofthe confidcnca coeffident
absoluts yelue of the mssn dlfrrsncsg
degree Celslus
degrcea Fahrcnhelt
degrce Ranklne
inchea of wgter column
spedficgravlty of morcury
pr€88ur3 dmp acrocs odflca meter, inches H2O
velodty haad of cbclt gas, lndles H2O
btal gampling flme, mlnutee
mlcrognam
denelty of acatone, mg/ml
denelty of wabr, 0.9982 g/ml or 0.002201 lUml
ac,hral anblc bet of gas Per mlnute at stack condlllons
ctoss-secflonel arsa of nozzl€, f
cross€acflonalarea of stach 8qu8rB ftet (ff)
Brithh thermal unit
proporton by volum€ of water vapor ln gae stream
paroouhe matbr conccntratlon ln sbck gaE, grlad
everegs unadjuabd gee concenttaton. ppmv
measured concenEetion of callbration gss, ppmv
cublc lbet
anblc fuet permlnute
avarago gas concntratlon adlusEd for blag, ppmv
svgrale of lnltal snd flnal system bhs ched( r3sponseE fiom upscale calhratlon ga8' pPmv
(rlblc mEter8
actral concenbaton of the upacale callbmUon gas, ppmv
ayorEgs of lnlflal and final system blas dred< rssponses ftom lowlerral callbraffon 988' ppmv
pltotfuba coefic;lent
partarlate metbr concontraUon ln ataok gas, Srldscf
callbratlon epan, % gr ppmv
rneasured concenhUon of calibratlon gas, ppmv
manufacturcd certfled conenbatlon of callbratlon gae, ppmv
drlfr assessmsnt, Yo of sPan
dry cublc ftet
dry cublc mebrs
dlametsr of no:zlo, lndtee
dlarnetEr of silack, lnches
dry standad cublofeet
dry standad anbicftet Per minub
dry stardad cublc mobrs
F-tactor, dscilfintMBtu of heat lnPut
Eetpermlnub
Eet per second
Est
eguanEet
9namgallons
grelns 00m grains perpound)
gralns por dry Etandad G1lblo tuet
hour
T
Docu ment #: c Po8 1 AS-040 rzB-Hii.ti
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A/1\ MONTROSEt!'Jr Atn qrlLtrY s!RvtcEs
I
ln
k
K
G
rt
kSq
l$,scfi
I
lb/hr
lb/MMBtu
lPm
m
M
m3
m.
luld
meq
ms
Mg
mln
ml ormL
mm
MM
MMBMIT
mn
mol
rnol. ut or iilrVtt
lvTW
n
ng
nm
Pla'
ps
Pe
Etrm
ppb
ppbv
ppbrd
Ppmppmv
pPmtd
ppmvw
Pr
psi
psla
PslS
P6
a.
o.
Q6
R
UNITS AND ABBREVIATIONS
porceril of leokinetic sampllng
lnctr
kllo orthousand (metrlc unlts, multlply by tOrl
kelvln (bmperaturE)
oonveslon fador 0.0154 grtng
converelon fador 0.002688 ((ln. Hgxfl1y((mlX'R))
kllogram
pltottrbe constant (85.49 ft/sec)
thousand upt standad oublc het per hour
Ittera
pounds per hour
pounde per mllllon Btu
litens per mlnub
metarormllli
thousand (Engllsh unlts) or mega (mllllon, mefic unlta)
cublc mebm
mass of rpsldue of accbnE after evaporatlon, mg
motecularrrclght of stack gas; dry basla, lb/lhmole
mllllequivalent
mlll[ram
megagram ('l0t grama)
mlnuE
mllllllbr
mllllmeter
mllllon (Engllah unlts)
mllllon Btu per hour
bhl amount of partlorlate matter collec{ed, mg
mole
moleanlar*elght
moleolaruelght of ctad< gas; nsl baala, lMb-mole
molecular nolght or megawatt
numberofdata polnte
nsnoglem
nanometer
bammefic progsurc, lndtee Hg
plcogram
stad< staUc pressure, lnchee H2O
barometlcpnesure of dry gas metor, lnches Hg
parts per bllllon
parb p6r bllllon, by volume
parts per bllllon by volume, dry basls
parb per mllllon
parts per mllllon, by volume
parts per mlllion by volume, dry basle
parta per mllllon by volume, wet bagls
absolub abd< gas pr€Gaulo, lncfiee Hg
pounds persguaro lnctr
pounds perlquaro lndr absolute
pounds persquam lnch gauge
stardard abgolute pr€ssula, 29.92 lnfies Hg
rolumetic Eow rab, actual condltons, acfui
nolumetrio f,or rata, etandard condltlonr, ecfrn
volumetlo fiow rata, dry standard ondlUonc, daofrn
ldeal gas congbnt 21.8ti ((ln. Hg) (frtly('R) (lbmole))
Page # 67
Document #: GP08 1 AS-040128-RT -1 672
66 +*g"p"H
sBh.t
sq
scf
scffi
scfrn
gcrn
sCmh
seo
gf, eq. fr., ord
std
t
Tooc
T.
Tm
bn ort
tsh ortonsrhr
$y ortons/yr
T.
T6
v
v.
vd
Vro
vm
V,rrul
vm
%
v.
V.nOst
Vq.st
Vt of-tww.
w|@
w{
Y
UNITS AND ABBREVIATIONS
post{un sysbm biag check, % of sPan
prHun system biae check, % of span
standad oublcbst
standald cublcfest Psr houl
standad anblc fuet per mlnub
stardad cublcmeters
stBrdard cttblc mdera Por hour
socond
square bet
standard
npticton (1000l€)
tryalue
abaolutE averago amblent bmperaturc' cR (+459'67 br Engllsh)
absolub averege dry gas mebrbmperatum, oR (+459.67 fur Engllsh)
bn = 2(XX) pounds
tons per hour
tons peryear
absoluto averagg stad< gas matortomporetuE, oR ({'459'67 fur English)
absolute bmperatrre at standard condltons
t olt
volumE of acebre blank, ml
volumc of acobnc used ln wash, ml
total votume tluO colbcbd ln lmplngers and glllca gel, grame
rolume of gae samplod through (ry geg meter, flf
volume of gas measured by he dry gae meter, corectsd to standard conditons, d8d
stack gas volumc samplod, acf
volums colb&d at stack condltons through nozzle, acf
averagg atrack gae rralodty, fuet per aecond
rolume of wabr vapor condensed, oonsded to etandad condiUong' sc'f
nolume of wabr vapor ln gas aampled ftom lmplngers' ecf
volumo of wabr vapor ln gas aampled ftrom elllca gel, scf
wat
$eEht of rBsldue ln acetone rvash, mg
total rnight of lmplngars, grams
totalwefiht of sllica gel, grame
dry gas meter callbratlon fador, dknEnslonl€gs
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60 a*Q}l,r+gp"H
AAS
ACDP
ACE
AD
ADL
AETB
AS
ASTM
BACT
BDL
BHP
BIF
BLScc
CD
CE
CEM
CEII,IS
GERII/IS
CET
CFR
CGA
CHNOS
CNCG
GOcoc
coMs
CPM
CPltlS
CT
CTM
cTo
CVAAS
D.
DE
Dloadns
DLL
DNCG
ECD
EIT
ELCD
EMPC
EPA
EPRI
ES
ESP
EU
FCCU
FGD
FI
F!A
FID
FPD
FPM
FnR
FTPB
FTRE
Furans
GC
ACRONYMS
atomic absorptlon speotoeoPY
alr contaminant dlscftarge Permh
analyzer calibrston snor, percant of span
absolute dlfrrence
abow detec*lon llmit
Alr Emlsslons Tesflng BodY
appllcable atandad (erdsslon llmlt)
A'merlcan Soclety ForTestlng And Materlals
best achl€vable contol technology
belorvdstecfron limlt
brake horaeporver
boller and lndugtrlal fumace
blaok llquorsollda
conffdence coeffdent
calibraton drift
callbra0on enor
contnuous emietlons monltor
contnuoue emlsslons monltorlng sysbm
contnuoug emigslone rab monltorlng eystem
callbratlon Ermrbst
Code of Federal Regulatona
cyllnder gas audlt
iienrendt analysls for detctmlnagon of C, H, N, o, and s contcnt ln fircls
concentrated non-condenaable gas
oablytc oxldlzer
cfialn of oustody
conllnuoue opadty monltorlng system
condenchle partladab matter
contnuoug paramelor montbrlng eysbm
combustion furblne
condlflonalbst method
catalytlo thermal olddlzer .
cold vapor abmlc absorptlon apec'troecopy
equlvalent dlameter
deetruc,tion effcleno1
polyclrlorlnatcd dlbeuofdlo:dns (pcdd's)
dstecffon level llmlted
dllub nonondensable gae
elec'tro n capfu m debclor
Englneer ln Tralnlng
elcctoconductMty debctor (hall debc{or)
estmabd madmum posslble concentrailon
US Envlronmental Protecflon Agsncy
Electlc Povv€r Re8€ercfi lnstltub
emlsslon standard (appllcable llmlt)
elecbosta0c preclpltator
emlssion unlt
iuld catalytc cracklng unlt
llue gas deeulturlzallon
flame lonlzaton
flamE lonlza0on analyzer
f, ame lonization debcdor
fl ame photometlc deteclor
fr ltarablE pardculab matter
Fourler-tansform lnfiamd specffoacopy
freld taln proof blank
fldd fah tocot/ory blank
polycfilorlnated dlbcrzoturans (podfg)
gae chmmatographY
Page # 69
Document #: GP081AS-0401 28-RT-1 672
6,0 **gN,T+g[I
GC/l,lS
GIFAAS
GFC
GHG
HAP
HC
HHV
HPLC
HR@/HRMS
HRSG
IG
ICAP
ICPCR
lcP-Mti
IR
rso
kw
LFG
LHV
TPG
MAGT
MDI
MDL
MNOC
MRL
MS
t{A
NCASI
NCG
ND
NDIR
NESHAF
NG
NIOSH
NIST
NMC
NMOC
NI,IVOC
NPD
NSPS
OSHA
PAH
PCB
PCWP
PE
PFAS
PI
PID
PM
PMro
P[tt'
POM
PS
PSD
PSEL
PST
PTE
PTM
ACRONYMS
gas chromatography/mass specfr,oscopy
graphite fumace atomlc abeorpdon speotroscopy
gas f,lter conelaUon
greenhouee gas
hazardoue alr pollutant
hydrocarbons
hlgher heatlng value
hlgh perbrmance llquld cfi romatograPhy
highrasolu[on gas chromatography/hlgh-rcaoluton maeB spec{roscopy
heat rBcovery steam generator
ion chromabgraphy
inducdrrely-coupled argon plasmognaphy
ion cfrromabgraphy with a post-column rcac*or
lnducdvely coupM plasrna-+naes spectroscopy
infrared radiatlon
lnbmaff onel Standards Organlzatlon
kllowatts
landfrllgas
lower heatng value
liqulfred p€hdeum gas
maldmum achlevable contnol teohnology
rnethybne dlphyenyl diisocyanate
mothod dsteoton llmlt
maimum normal operatlng condiilons
method rEportng llmlt
masr spectometry
not appllcable or not available
Natonal Coundl ForAlrAnd Steam lmprovement
non-condensable gaees
not deteded
nondisperslve infared
Natlonal Emissione Standards For Hazadous Alr Poltutants
natural gaa
Natlonal lnetltub For Occupatlonal Safety And Health
NaUonal lngt'hrb Of Stendads And Tecfinology
nonflEthang cuttar
non-msthan€ organic compounds
non-nplhane volatlle organlc compounds
nltogen phosphorus debc{or
New Source Porformance Standards
Occupatlonal SaHy And Heslth Admlnlstretlon
polycycllc aromatc hydrocabons
polycfrlodnated blphenyl compounds
plywood and composib wood produde
Probsslonal Englneer
per- and polyfluoroalkyl subetsncas (PFAS)
photolonlzaton
photolonlzaton detedor
parfrculate matbr
partculate matter less than 10 microna in aerodynamic dlamebr
partarlate matter less than 2.5 mlcrons ln aerodynamlc dlameter
polycycllc organic matter
perbrmance spedficaUon
partde stse dFHbutlon
plant stte emlselon llmltg
perbrmance speclficaUon test
permanont totsl enclosur€
perfurmance test method
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QA/QC
ot
QSTI
RA
RAA
RACT
RATA
RCTO
RICE
RM
RTO
SAM
scD
scR
SD
SemI-'VOST
SRM
TAP
TBD
TCA
TCD
TGNENIiDC
TONMOC
TGOC
THC
Tlc
TO
TO
TPM
TSiP
TTE
ULSDW
VEvoc
vosTwc
WWTP
AGRONYMS
quallty assurance and quallty contsol
Qualtfied lndivldual
Quallfied Source Teatng lndlvldual
rehtve aocuracy
rplatvr accuracy audit
reasonably avallable contol technology
relatve acanracy bst audlt
ro0ary concanbator thermal o$dlzer
statlonary raclprocdng lntemal ombustlon englne
raftrcnca method
mgenera0ve thermal o:ddlzer
sulfurlc acld mlst
sulfu r dlernllumlnegenl dsbdor
sslscilve catal$lc reduc{on syst€m
stardad devlatlon
semlvolatlle organlc compounds sample taln
etandad rcbrcnce material
to:do alr pollutant
to be debmlned
therma I conduc'tivlty analyzer
ft ermal conducdvlty detedor
btal gaaeoug non+thane non-melhane oganlc compounds
total gaEeou8 non-mcthanc olganlc compound!
bhl gaseous oryanlc oompounds
bEl hydmcarbono
bntatvely ldentlficd compound
thermal o$dtser
to{c organlc (as ln EPA Method TG15)
bbl parllanlate matter
total suapended partiorlab matter
bmporary total cnclosurc
ultra-low gulfur dlascl
ultravlolet radlatlon range
vlelble emlsslons
volafl le organlc compounds
vohtle organlc aample Ealn
rvater column
waste rrater treatnent plant
Page#71
Document #: GP08 1 AS-040'l 28-RT -1 67 2
60$qxJI+gp"I
A9 . arsenlc
Ba badum
Bc berylllumC ca6onCd cadmlumCdS cadmlum sullldeCllrO fornaldeffie
Cll.CHO aoeEldehyde
CHsOH rnothenol
CtL rpthanc
CrltO dhylene oldde
Crlb etraneCltl.O acrolelnqthO prcplonatsehyde
qHa propens
CltlrOH phenol
Ch chlorhe
ClOz chlorlne dlodde
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Ag
Cr
Cu
CHEMICAL NOMENCLATURE
so selenlumS0z eulturdlodde
Sq eulturtdodde
S0, sulfuro)ddes
TCDD t€tradllorodlbenzodlodnTCDF btradllorodlbenzofuranTGOC totBl gas€ou8 organlc concentaton
THC total hYdrocatuons
Tl thdllum
TRS bbl leducsd sulfur comPounds
Zn zlnc
cerbon rnono)ddrCo cobaltCOr carDon dlo:dde
chpmium
copperEtO cthylenc olddeEIC)H etry'alcohol(efignol)H2 hydrcgen
tlrO webr
HzQ hydrogonpero:dde
HrS hydrogen eulfdc
HZSO. rutfurlc add
HCI hydrogcn chlorldsHg mcrctttylPA lroproryl alcoholMDI mcthybncdlphyon$dlltocyanaleMeCh mcthy4cnc dtbddeMEK methyl ettry' kotonoMoOH msthanolMn rnanganssgNz nllrogen
Nru arnmonlaNl nlckslNO nltrlo olddeNO, ntrogen dlocldc
NOr nltrogen olddes
02 o(ygcnP phosphorusPb b8dPCDD polyehlorinated dhenzopdloldnsPCDF polyctrlorlneted dbcnzofurans
Docu ment #: GP08 1 AS- Ooo',t r,l?&i x{l' I
Appendix C.2
Instrumental Test Method QA/QC Data
Page # 73
Document #: GP081 AS-040 1 28-RT -1 67 2
Gompontl : Hcbcr Ltght & Porurr
Sourcc: Unitfz
Wt 07n7ru
SanrpleGll: 02
sp.n : 20.45
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Anr@Cdl!tr0e!
CyllndcrValuc
(%)
0
10.07
20.45
hNdglu
Analyzcr Rarponr
(%)
0
10.2
Ectlfir!..Elu
Analyzcr R$ponsc
(%)
0
10.2
Eel&d-a.ElI
Analyzcr Rclponsc
(%)
0
10.2
Ecdrecf.r;l.Ehl
Analyzer Rcrponrc
(%)
0
10.2
Analyzs Rctponlc
(%)
0
10.2
20.5
Syrilcm Reeponsc
(%)
0.1
1o.2
Syatcm Rcsponlo
(%)
0.1
10.2
Syrtem Rcsponcc
(%)
0.1
10.1
Syobm Rccponre
(%)
0.1
10.2
Abloluh DifrIgnco
(%)
0.0
0.1
0.1
Syricm Blas
(% ofspan)
0.49
o-00
Sycbm Blas
(% ofspan)
0.49
0.00
S),!Em Blag
(% ofrpan)
0.49
0.49
Sysbm Blaa
(% ofspan)
0.49
0.00
Dlfielencs
(% ofopan)
0.00
0.64
o.24
Drilt
(% ol epan)
0.00
0.00
Ddft
(% ofspan)
0.00
0.zlS
Ddft
(% ofspan)
0.(x)
0.49
Document #: GP081 AS-o+or zBffi-fo?z
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MONTROSE AIR QUALITY SERVICES, LLC.
6823 South 3600 West 801-266-7111
Spanish Fork, Utah 84660
Plant : Heber Light & Power
Source : Unit #2
Date'.07117124
Run : Post NO2 Conversion, EPA Method 7E, Section 8.2.4
ctual Concentration : 51.4 ppm NOa (as NO,)
Date and NOxTime (ppm)
711712411;31:57 19.2
7117124 11:32:57 47.8
711712411:33:57 47.8
7117124'11:34:57 47.9
7117124'11:35:57 47.8
71171241'l:36:57 47.7
711712411:37:57 29.7
Average 47.8
Minimum 47.7
Maximum 47.9
7o Difference 0.31olo
Conv Efficiency
93.0%
Page # 75
Document #: GP081 AS-040 128-RT -1 67 2
MONTROSE AIR QUALITY SERVICES, LLC.
6823 South 3600 West 801-266-7111
Spanish Fork, Utah 84660
Plant: Heber Light & Power
Source : Unit #2
Date : July 17,2024
Run : Stratification Test
Total NOx Average
114.7
Stack l.D. Date and NO. COo/o Time (ppm) (ppm)
16.7 71171247:35 116.3 8.3
71171247:36 112.3 8.1 0 0
71171247:37 115.4 8.1 0 0
50.0 7117124 7:38 116.9 8.0
71171247:39'114.3 7.9 0 0
71171247:40 11'1.3 8.0 0 083.3 71171247:41 119.4 7.9
71171247:42 114.3 7.9 0 0
71171247:43 112.5 7.8 0 0
0 0 't2.2 5.2 114.7 99.9
13.'.t 4.7
13.1 4.70 0 13.'l 4.7 114.2 99.5
13.1 4.7
13.1 4.70 0 13.1 4.7 11s.4 100.6't3.0 4.7't3.0 4.7
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(Y"l (%) Average diff
Page # 76
Document #: GP081AS-040 128-Rf -1672
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Coilp.tty : Hobcr Llght & Power
8outtc : Unlt #2
Orflal O7A7n1
Semplc Gr : CO2
Sp.n: 11.97
AnelnzerCrllbldon
Cy'indcrValuc
(%)
0
6.(X
11.97
hITltEE
Analy:er Rceponrc
(%)
0
6
Ec$:fd-fi-E}g
Analyzar Rcrponsc
(%)
0
6
Pctncrtfil Elas
Analyzcr Rerponrc
(%)
0
6
Pot'bctlil Blr
Analyzcr Responrc
(%)
0
6
Analyzer R$ponse
(%)
0.0
6.0
12.O
Syrtum Rcrponsc
(%)
0.0
6.1
Sysbm Recponrc
(%)
o.2
6.1
Systam Rcsponse
(%)
o.2
8.1
Syetcm Responrc
(%)
0.2
6.1
Abeolut Dlficlsncc
(%)
0.0
0.0
0.0
Syltcm Bles
(% ofrpen)
0.00
0.8.f
Spbm Blar
(% ofspan)
't.67
0,84
Systcm Blas
(% of cpan)
1.47
0.84
Syrtcm Blac
(% ofgpan)
1.47
0.84
Difr]lncc
(% ofrpan)
0.00
0.33
0.25
Drlt
(% ofgpan)
1,07
0.00
Drtlt
(% otgpen)
0.00
0.00
Drift
(% ofrpan)
0.00
0.00
Page#77
Document #: GP081AS-040128-RT-1 672
Gornpcny: HGbor Light & Porvor
Eouruc : Unlt fil
Dl,bz Oll17frl4
Semplc Gar : NO,
Sp.n: 247
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Anelvan Grllbreilon
CyllndcrVsluc
(ppm)
0
101.9
217
lllgitEllr
Analy!.r Rctponlc
(ppm)
o.2
99.9
Pod-bctll Blrr
Analyzcr Rctpons.
(ppm)
o.2
99.9
Port-brt12 Blr.
fuialyzcr Responea
(ppm)
o.2
s8.9
Pct-tatlil Bla
Analyzcr Rcsponsc
(ppn)
o.2
99.9
Analyzer Rcrponsc
(ppm)
0.2
99.9
216,.8
Systam Rcsponsc
(ppm)
0.3
101.0
Syrtcm RclponEc
(ppm)
0.1
't01.4
Syrtcm Rclponsc
(ppm)
0.4
101.6
Systcm Re.ponsc
(ppm)
0.a
101.5
AbEolutc Dlfietcne
(ppm)
0.2
2.0
o.2
Syrtam Biaa
(% ofspan)
0.04
0.45
SyBtcm BlaS
(% ol rpan)
0.(x
0.61
Syrtcm Blar
(% ofapan)
0.08
0.69
Syatcm Blar
(% ofepan)
0.08
0.65
Dillbrsncc
(% ofepan)
0.0E
0.81
0.08
Drtlt
(% ofspan)
0.08
0.16
Drtfr
(% ofspan)
o.12
0.08
Drlll
(% ofspan)
0.00
0.04
Document #: G p08 1 AS-oao r zB-Hi-foTz8z
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Conplny: Hcbcr Light & Pomr
Soutcc: Unltt2
Drtlc z 07117124
SmplcGlc: CO
Sprn : 25.3
Amlvar Callbrrtlon
CyllnthrValuc
(ppm)
0
12
25.3
tnltd Blt
Anelyzcr Rcrponr
(ppm)
0.'l
12
fsHsrilLEls
Analyrcr RcEponlc
(ppm)
0.1
12
Pct-brtlil Bla
Analyzcr Rclponsc
(ppm)
0.1
12
Pot-bdfil Bh.
Anatyzcr Rcrponse
(ppm)
0.1
12
Analyzcr Recponsc
(ppm)
0.1
12.0
25.4
Systcm Rcrponm
(ppm)
0.3
11.0
SyrEm Rcrponsc
(ppm)
0.3
12.0
Sydcrn Rcsponsc
(ppm)
0.4
11.9
SysEn Responrc
(ppm)
0.3
11.9
Abaolub Dlfrtgncc
(ppm)
0.1
0.0
0,'l
SyBtdYr Blss
(% ofrpan)
0.79
0.40
Syrtam Blas
(% ofrpan)
0.79
0.00
Spbm Blar
(% ofcpan)
1.1S
0.40
Syttcm Blae
(% ofepan)
0.79
0.40
Ditrcpncc
(% ofspen)
0.40
0.00
0.40
Drifl
(% ofepan)
0.00
0.40
Drlt
(% ofrpan)
0.40
0.40
odtt
(% of $an)
0.,t0
0.00
Page # 79
Document #: GP081AS-040128-RT-1 672
,.. v I ,, C.. -r(rl I
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Page # 80
Document #: GP081AS'040128-RT-1672
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Page # 81
Document #: GP08 1 AS-0401 28-Rf -1 67 2
ProSyccBZ Cca
ClldcrNunber Afil{574CS Er.pardodt ncorhhty
?fi Wn lllt lE orrd. t l ppm
Ealrncr }{I0!g.o
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Page # 83
Document #: GP081 AS-040 128-RT -1 67 2
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CTNTTTrcETE OF ANALYSIS / EPA PROTOCOL GAS
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Page # 85
Document #: GP08 1 AS-040128-RT -1 67 2
W
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Document #: GP081 AS-ooor rB-Hi-futu,
;
Siff Eg&rdooDrI OlAtAE,
Appendix C.3
Calibration Records
Page # 87
Document #: GP081AS-040 128-Rf -1672
Montrose Arr Quality Services
6823 South 3600 West Spanish Fork, Utah 84660
(801) 7e4-2950 [phone]
Meter Box Calibration Data Form
(English Units)
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Date
7t3t2024
Average Yi
1.016
Orfice Manometer
Setting aH
0.50
1.00
1.50
2.00
3.00
4.00
Barometric Pressure
25.55
Average AH Calibrated By Std Meter Yi1.708 0.99497
Meter Box Number
APEX XC-522-10
DGM No.351501
lnlet
(Td i)'F
67
75
75
82
82
88
88
92
92
95
95
97
Std Test Meter
(Vs) Ft3
4.999
4.999
9.998
9.999
9.999
10.002
Dry Gas Meter
Outlet
(Td o) "F
67
68
68
70
70
73
73
76
76
79
79
81
Dry Gas Meter
(vd) Ft3
4.904
4.911
9.845
9.888
9.9
9.92
Average
(Td)'F
69.25
73.75
78.25
82.25
85.50
88.00
Std Test Meter
(Ts)'F
71
71
71
71
71
73
73
73
73
75
75
75
Time @
Minutes
11.67
8.13
13.20
11.42
9.25
7.97
AH/13.6
0.04
0.07
0.11
0.15
0.22
0.29
Std Test Meter
Average Temp.
71.00
71.00
72.00
73.00
74.00
75.00
AH
1.800
1.735
1.706
1.695
1.665
1.645
Average AH
1.708
Yi
1.009
1.015
1.018
1.018
1.018
1.0't6
Average Yi
1.016
Documenr #: GPO81AS-ooorrBffi-f# I
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Montrose Air Quality Services
6823 South 3600 West Spanish Fork, Utah 84660
(801 ) 794-2950 (801) 26U.^7 111
Sample Box Temperature Sensor Calibration Form
Sample Box Number: lmpinger Boxes (Cal)
Date:71212024
Calibrated By: CG
Barometric Pressure: 25.57
Reference: Digi-Sense 20250-92 SN:210429562
Reference Point Source a Reference ThermocoupleNumber (specify) Thermometer Potentiometer
Temperature "F Temperature oF
Temperature
Difference b
o/o
0.14
-0.19
0.00
0.'19
0.14
-0.20
-0.19
0.00
0,00
-0.19
-0.19
-4.14
0.00
0.19
-0.14
0.19
0.19
0.19
-0.14
0.00
0.19
-0.14
0.19
-0.19
0.00
0.14
0.00
-0.19
1APEX 1#14(XC522) 3
4
4
5
5
1APEX 1#24(XC522-10) 3
4
4
5
5
1APEX 1#34(XC522-14) 3
4
4
5
5
1ES1
#1A (C-5000) 3
4
4
5
5
a Type of calibration system used.
Probe on 249 248
Probe off 74 75cPM 75 75
Oven on 249 248
Oven off 76 75
lmpinger ice 33 34
lmpinger amb. 76 77
Probeon 242 242
Probe off 75 75cPM 74 75
Oven on 251 252
Oven off 73 74
lmpinger ice 33 33
lmpinger amb. 75 74
Probe on 246 247
Probe off 76 75cPM 75 74
Oven on 241 242
Oven off 72 71
lmpinger ice 34 34
lmpinger amb. 77 76
Probeon 239 240
Probe off 75 74cPM 74 75
Oven on 242 241
Oven off 74 74
lmpinger ice 33 33
f mpinger amb. 75 76
I b (rererencer"rno ;ilr::ll,jliil,,ffl["["j".iJ;,0 ", + 460) * 1oo< 1.5%
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Document #: GP081 AS-04O128-RT -'l 612
Montrose Air Quality Services
6823 South 3600 West Spanish Fork, Utah 84660
(801) 794-2e50 [phone]
Sample Box Temperature Sensor Calibration Form
Sample Box Number: Probes (Cal)
Date:71212024
Calibrated By: CG
Barometric Pressure: 25.57
Reference: Digi-Sense 20250-92 SN:210429562
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36
181
228
247
353
458
36
179
228
245
354
456
35
175
227
246
352
454
35
180
229
247
355
457
36
177
228
247
353
455
36
177
226
245
353
455
a)z',-A b)
c)
d)
e)
0
a)z'.-B b)
c)
d)
e)
f)
a)3'-C b)
c)
d)
e)
0
a)
3'- D b)
c)
d)
e)
0
lce Water
Hot Water
Boiling Water
Warm Oil
Hot Oil
Boiling Oil
lce Water
Hot Water
Boiling Water
Warm Oil
Hot Oil
Boiling Oil
lce Water
HotWater
Boiling Water
Warm Oil
Hot Oil
Boiling Oil
lce Water
Hot Water
Boiling Water
Warm Oil
Hot Oil
Boiling Oil
Reference Point Source aNumber (specify)
Reference ThermocouPle
Thermometer Potentiometer
Temperature'F Temperature "F36 35181 182231 233248 249355 354458 457
Temperature
Difference b
o/o
0.20
-0.16
-0.29
-0.14
0.12
0.11
-0.20
-0.16
0.15
0.00
0.25
-0.11
0.00
-0.31
0.00
0.28
-0.12
-0.11
0.20
0.31
-0.15
-0.14
0.12
0.11
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;
a Type of calibration system used.
b (reference temp. oF + 460) - (test thermometer temp. 'F + 460) ' 100< 1.5%
reference temPerature 'F + 460
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thvr\
ur.)N il(()\l
C.llbnr.d Pllot fub.;
Pltot Tube Callbratlon Data Sheet
PmbdPltol lD No:2'A-SP-2'
Prolncior d DEiirl Anglo Flndor lol
libsuino Tap.lO:
C.up.r lD
Cdbntbn p.dbmrd usho thr prccodmr ol EPA M.lhod 2. Src0il I 0. 1
-99:-REF-EEI_(Et.REF€PR.I
f: H#'"""ndrubrns'''*'-i
Pa$
PeG
Pts
Pas
PasE
P6!s
Pass
P8!!
Pu
ParE
D.aG Ldkafne tvtl pothlon fo. d.l.mlrln! q rnd q.
ffi
d.Lmlnlrg 0.
-{il!
i
D.gn l.rdlalitC lnd po.ltlon fo. dd.mlnlng t $o qlculdtrC Z.
Alrombly lntoi4omponent Splclng Roqulromont
Oftol TC only
S.tb.ck TC only
Pas
Fsil
Pas Off!.l TC only
Podormad 8t{ _ J& Avit.
ApprovadBy _chcynryouymm
SiCnatuG:
Signaturo:
Daie: _ oltu2tita
Drto: _ o7&tna
a, (-10'<q,< +l0P)4.3
( -10'<6< +loPl 3.3
B. 1-5'< B. < +5'l o.5
6r (-t" <Ur<+5"1 2.3
2.4
A t6
A o.sa30
z'AtanY (t 0.0428Abne a+ OO3l25"l o o?41q (0.1875" < D,< 0.375")0.3730
P. lt osn. < p. < I srl.l 0.r1450
Pr (l.o5Dr < Pr < l.sDr)0.4950
IPr-P. Is0.(E25 4.05mD.!@ lndlc.ltrg lml pdud tor
Page # 91
Document #: GP081 AS-0401 28-RT -167 2
Runl Run2 Run3 Average:
APEX
xc-522t10
Heber Light & Power
Heber, Utah
Unit 2
711712024
Run 1
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
Run 2
1.140175
1.140175
1.',140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
'1.140175
1.140175
Run 3
1j40175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140175
1.140',175
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Alt-009 Post Meter Cal.
% Dlfference, Callbratlon must be
wlthln 5% of orginal Y Factor
-2.37%
1140175 1.140175 1.140175
Document #: GP081AS-ooor rB-Hi-fun"
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Address:
City/State/zlp:
Manufacturer:
Model:
Serlal Number:
ldentlflcatlon:
Locatlon:
Montrose Air Quality Services
Certlflcate of Balance Calabratlon
6823 South 3600 West
Spanlsh Fork, Utah 84550
Sartarius
Analytical
Ba110530706871
AET#1
SmallTrailer
CertlflcateNo.: 712-202&!
Callb. Date: 71212024
Technlclan: Cheyney Guymon
Next Callbratlon:
Refercnce Welghts Cal ld:
Nomlnal Mass
1
20
50
100
2A0
Comments:
lndlcatlon
1
20.0ooo
50
99.9999
200.0001
tl212O2s
Error
0.0000
0.0000
0
-0.0001
0.0001
Nomlnal Mass
1
20
50
100
2@
lndlcatlon Error
1 0.0@0
200
500
99.9998 -0.0002
200 0
Pertinent lnformatlon:
The artifact descrlbed hereln has been callbrated using standards traceble to NIST. This is
to certlry the data reported herein is true and correct as the date calibrated. The
procedure used to callbrate the artifact meets the requirements to meet MAes standards.
Authorlzed Slgnature:
Page # 93
Document #: GP081AS-0401 28-RT-1 672
Montrose Air Quality Services
Certiflcate of Balance Calabration
Address: 6823 South 3600 West
Clty/State/Zlp: Spanlsh Fork, Utah 84660
Manufacturer:
Model:
SerlalNumber:
ldentlflcatlon:
Location:
Shimadzu
Top Loader
D446711AET #2439
AET#2
SmallTrailer
CertiflcateNo.: 712-2024*2
callb. Date: 71212024
Technician: CheYneY GuYmon
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Next Callbratlon:
Reference Welghts Ca! ld:
Nomlnal Mass
1
20
50
1@
200
Comments:
lndlcatlon
1.00
20
49.99
99.98
200.01
tl212O2s
Error
0.00
0
-0.01
-0.02
0.01
Nominal Mass
L
20
50
100
200
lndlcatlon Error
1.00 0
19.99 -0.01
49.98 -0.02
99.98 -0.02
200.00 0
Pertinent lnformatlon:
The artifact descrlbed herein has been callbrated using standards traceble to NlsT. This is
to certify the data reported herein is true and correct as the date calibrated. The
Authorlzed Slgnature:
procedure used to calibrate the artifact meets the requirements to meet MAQS Standards.
Document #: Gp08 1 AS-ooo't rB-Hf-f u?0,
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Model:
SerlalNumber:
ldenUflcatlon:
Locatlon:
Next calibratlon:
Reference Welghts Cal ld:
Nomlnal Mass
1
20
50
100
200
Comments:
u212025
Error
0
0
0
0.01
{.1
Nomlnal Mass
7
20
50
100
200
Montrose Air Quality Services
Certificate of Balance Calabration
Address: 5823 South 3500 West
Ctty/Stats/zlp: Spanish Fork, Utah 84660
OHAUS
Top Loader
8350103094
AET#5
Gooseneck
lndlcatlon
1
20
50
100.01
199.9
Pertlnent lnformatlon:
The artlfact described hereln has been callbrated uslng standards traceble to NIST. This is
to certifu the data reported herein is true and correct as the date calibrated. The
procedure used to calibrate the artlfact meets the requirements to meet MAQS Standards.
Authorlzed Slgnature:
Certlficate No.: 712-2024*5
Callb. Date: 71212024
Technlclan: Cheyney Guymon
lndlcatlon Error
10
200
500100 0
200 0
Page # 95
Document #: GP08 1 AS-040 128-RT -1 67 2
Next Callbration:
Reference Welghts Cal ld:
Nomlnal Mass
t
20
50
100
zoo
Comments:
Nomlnal Mass
7
20
50
100
200
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Pertinent lnformatlon:
The artlfact described herein has been calibrated using standards traceble to Nl5T. This is
to certify the data reported herein ls true and correct as the date calibrated. The
procedure used to calibrate the artlfact meets the requirements to meet MAQS Standards.
Authorized Slgnature:
Montrose Air Quality Services
Certlficate of Balance Calabratlon
Address: 6E23 South 3500 West
Clty/State/ap: Spanish Fork, Utah 84660
Manufasturer:
Model:
SerlalNumber:
ldentiflcaUon:
Location:
OHAUS
Analytical
8329582368
AET#6
Gooseneck
Indicatlon
1
20
50
99.9999
199.9998
tl212O2s
Errpr
0.0000
0
0
-0.0001
-0.0002
Certificate No.: 712-2024#6
callb. Date: 71212024
Technician: Cheyney Guymon
lndlcation Error
1 0.0000
200
49.9998 -0.0002
100 0
199.9999 -0.0001
Docu ment #: G Po8 1 AS-ooo r rtt-Hi-ffru,
;
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Montrose Air Quality Services
Certlflcate of Balance Calabratlon
Address: 6823 South 3600 West
clty/State/zlp: Spanish Fork, Utah 84650
Manufasturer:
Model:
SerlalNumber:
Identlficatlon:
Locatlon:
Flrstaden
HC21404N
947
MAqS-1
Laboratory
lndlcatlon
1
20
49.9999
100
200
Certiflcate No.: 712-2024*8
callb. Date: u2l2o24
Technlclan: Cheyney Guymon
Next callbration:
Reference Welghts Cal ld:
Nomlnal Mass
1
20
50
100
200
Comments:
tl212O2s
Error
0.0000
o.0000
-0.0001
0
o
Nomlnal Mass
1,
20
50
100
200
lndlcatlon Error
1 0.0000
20 0.0000
49.9999 -0.0001
99.9999 -0.0001
200 0
Pertlnent I nformatlon :
The artifact descrlbed hereln has been calibrated using standards traceble to NIST. Thls is
to certifo the data reported herein ls true and correct as the date calibrated. The
procedure used to calibrate the artifact meets the requirements to meet MAQS Standards.
Authorlzed Slgnature:
Page # 97
Document #: GP08 1 AS-040 128-Rf -167 2
Appendix C.4
Accreditation Informatio n I Certifications
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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: Beckie Hawkins
Title: District Manager
Region: Great Plains Region, Utah Office
Email: [e-mail]
Phone: 8OL-794-2950
Name:
Title:
Region:
Email:
Phone:
Cheyney Guymon
Client Project Manager
Great Plains Region, Utah Office
CG uymon @montrose-env. com
801-362 -4978
AUG 2 0 2024
DIVISION OF AIR OUALITY
Heber Unit 2 2024 NOx and CO rev
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name Heber Light & Power
Company Contact:Jason Norlen
Contact Phone No.435-654-2913
Stack Designation:Engine #2
Test & Review Dates
Test Date:7/17/2024
Review Date: 9/20/2024
Observer:None
Reviewer:Robert Sirrine
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./kW-hr
lbs./hr. 4.06 1.00 2.44 0.07
ppm 150.0 10.00 119.750 5.440
Percent
%O2 Correction as a whole #
Test Information Heat Input
Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static)
fuel flow rate
(Btu/hr.)
Heat Input
(Btu/hr.)
19.50 2.074 1.0160 1.708 0.84 24.68 -0.22
Contractor Information
Contact: Cheyney Guymon
Contracting Company: Montrose Air Quality Services
Address: 6823 S 3600 W Spanish Fork, Utah
Phone No.:
Project No.:
8710

Round
Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
Diluent
F factor used
O2
CO2Anthrocite 2
Bituminous
Lignite
Natural
Propane
Butane
10100
COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Wet CEM
Correct For O2
CO2 Interference w/CO
Yes
Yes
Yes
Heber Unit 2 2024 NOx and CO rev
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Heber Light & Power
Engine #2
Average Emission
Dry SO2 NOX CO
g/KW-hr 0.445 0.012 Average % concentration
lbs./hr.2.442 0.068 CO2 O2
ppm or % 119.75 5.44 6.57 9.57
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 CO2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)1.83E+00 7.73E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 1.363E-05 5.767E-07
lbs./hr.2.331 0.099 6.50 9.50
ppm or %114.11 7.93 5.90 10.90
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)1.87E+00 4.91E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 1.418E-05 3.723E-07
lbs./hr.2.424 0.064 6.60 9.60
ppm or %118.71 5.12 5.90 10.40 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)1.99E+00 3.14E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 1.510E-05 2.380E-07
lbs./hr.2.572 0.041 6.60 9.60
ppm or %126.43 3.27 6.60 9.80 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Heber Unit 2 2024 NOx and CO rev
Calibration Error Test
Test Date July 17, 2024 O2
CS - Cal. Span 20.45
Units %
Cylinder No. Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.00% Passed Cal.
Mid-level 10.07 10.20 0.13 0.64% Passed Cal.
High-level 20.45 20.50 0.05 0.24% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of CS - Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 49.24%
100% of Cal. Span High-level 100.00%
Test Date July 17, 2024 CO2
CS - Cal. Span 11.97
Units %
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
Mid-level 6.04 6.00 0.04 0.334% Passed Cal.
High-level 11.97 12.00 0.03 0.251% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 50.46%
100% of Cal. Span High-level 100.00%
Test Date SO2
CS - Cal. Span
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level
Mid-level
High-level
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level
40 to 60% of Cal. Span Mid-level
100% of Cal. Span High-level
Test Date July 17, 2024 NOx
CS - Cal. Span 247.00
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.20 0.20 0.081% Passed Cal.
Mid-level 101.90 99.90 2.00 0.810% Passed Cal.
High-level 247.00 246.80 0.20 0.081% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 41.26%
100% of Cal. Span High-level 100.00%
Test Date July 17, 2024 CO
1 CS - Cal. Span 25.30
10 Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.10 0.10 0.395% Passed Cal.
Mid-level 12.00 12.00 0.00 0.000% Passed Cal.
High-level 25.30 25.40 0.10 0.395% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 47.43%
100% of Cal. Span High-level 100.00%
Heber Unit 2 2024 NOx and CO rev
Division of Air Quality Stack Test Review of
Heber Light & Power
SO2 NOX CO CO2 O2 Engine #2
CS Calibration Span 247.00 25.30 11.97 20.45Units ppm ppm ppm % % Unprotected
CV - Cylinder Value:SO2 NOX CO CO2 O2Low-Level 0.00 0.00 0.00 0.00
Mid-Level 101.90 12.00 6.04 10.07
High-Level 247.00 25.30 11.97 20.45
0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 41.3% 47.4% 50.5% 49.2%
100% of Cal. Span 100.0% 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 101.90 12.00 6.04 10.07
Calibration Error Test
Cs - Measured Concentration SO2 NOX CO CO2 O2Low-Level 0.20 0.10 0.00 0.00
Mid-Level 99.90 12.00 6.00 10.20
High-Level 246.80 25.40 12.00 20.50
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 99.90 12.00 6.00 10.20
Low-Level 0.08% 0.40% 0.00% 0.00%
ppmdv Difference 0.2 0.1 0 0
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.81% 0.00% 0.33% 0.64% ppmdv Difference 2 0 0.04 0.13
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
High-Level 0.08% 0.40% 0.25% 0.24%
ppmdv Difference 0.2 0.1 0.03 0.05
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.30 0.30 0.00 0.10 System Bias.
SBi - Zero Bias TRUE 0.04% 0.79% 0.00% 0.49%± 5% of Span
Difference TRUE 0.1 0.2 0 0.1
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.00 11.90 6.10 10.20
SBi - Up-Scale Bias TRUE 0.45% 0.40% 0.84% 0.00%
Difference TRUE 1.10 0.10 0.10 0.00
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:7/17/2024 SO2
SO2 NOX CO CO2 O2 NOX
113.3 8.00 5.9 10.9 CO
0.0% 45.9% 31.6% 49.3% 53.3%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.10 0.30 0.20 0.10 System Bias.
SBi - Zero Bias TRUE 0.04% 0.79% 1.67% 0.49%± 5% of Span
Difference TRUE 0.1 0.2 0.2 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.40 12.00 6.10 10.20
SBi - Up-Scale Bias TRUE 0.61% 0.00% 0.84% 0.00%
Difference TRUE 1.5 0.0 0.1 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.00% 0.00% 1.67% 0.00% Drift
Difference TRUE 0.2 0.0 0.2 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass Pass
Up-scale Gas Drift TRUE 0.16% 0.40% 0.00% 0.00%
Difference TRUE 0.4 0.1 0.0 0.0Pass or Re-Calibrate Pass Pass Pass Pass
Engine #2 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
2.07 24.68 -0.22 24.66 799 5.90 10.90 83.20 29.38 27.96
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 453.1923
1.0160 0.84 41.860 104.00 80.0 34.288 4.895 0.1249 0.9990 0.999
Load - Megawatts
Avg. √∆P's Vs
(ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
0.7800 75.68 195,396 9,418 170,984.51 Enert >X
3D Pito #1 - Times
Date
Point No.∆P √∆P ts F tm F (in) tm F (out)
Final Vf Initial Vi
1 0.63 0.794 798 67 68 674.20 686.90 -12.70
2 0.62 0.787 797 69 72 747.10 692.00 55.10
3 799 69 75 655.70 618.20 37.50
4 800 71 78 807.50 783.40 24.10
5 800 74 82
6 799 77 86 2884.50 2780.50 Sum
7 799 80 88
8 799 82 89
9 795 84 89
10 799 84 90
11 799 83 90
12 800 82 91
13
1415
16
17
1819
20
21
2223
24
NOTEThese cells scans for the appropriate Cir. gas after the Cm
If this scan is incorrect change the Cdir to the correct gas value.
CO Calibration Gas
Heber Unit 2 2024 NOx and CO rev
Division of Air Quality Stack Test Review of
Heber Light & Power
SO2 NOX CO CO2 O2 Engine #2
CS Calibration Span 247.00 25.30 11.97 20.45
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2Low-Level 0.00 0.00 0.00 0.00
Mid-Level 101.90 12.00 6.04 10.07High-Level 247.00 25.30 11.97 20.45
0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 41.3% 47.4% 50.5% 49.2%
100% of Cal. Span 100.0% 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 101.90 12.00 6.04 10.07
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2Low-Level 0.20 0.10 0.00 0.00
Mid-Level 99.90 12.00 6.00 10.20
High-Level 246.80 25.40 12.00 20.50
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 99.90 12.00 6.00 10.20
Low-Level 0.08% 0.40% 0.00% 0.00%
ppmdv Difference 0.2 0.1 0 0
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.81% 0.00% 0.33% 0.64%
ppmdv Difference 2 0 0.04 0.13
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
High-Level 0.08% 0.40% 0.25% 0.24%
ppmdv Difference 0.2 0.1 0.03 0.05
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.10 0.30 0.20 0.10 System Bias.
SBi - Zero Bias TRUE 0.04% 0.79% 1.67% 0.49%± 5% of Span
Difference TRUE 0.1 0.2 0.2 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.40 12.00 6.10 10.20
SBi - Up-Scale Bias TRUE 0.61% 0.00% 0.84% 0.00%
Difference TRUE 1.5 0 0.1 0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:7/17/2024 SO2
SO2 NOX CO CO2 O2 NOX118.2 5.30 6.3 10.4 CO
0.0% 47.9% 20.9% 52.6% 50.9% CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.40 0.40 0.20 0.10 System Bias.
SBi - Zero Bias TRUE 0.08% 1.19% 1.67% 0.49%± 5% of Span
Difference TRUE 0.2 0.3 0.2 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.60 11.90 6.10 10.10
SBi - Up-Scale Bias TRUE 0.69% 0.40% 0.84% 0.49%
Difference TRUE 1.7 0.1 0.1 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.04% 0.40% 0.00% 0.00% Response Spec.
Difference TRUE 0.3 0.1 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass Pass
Up-scale Gas Drift TRUE 0.08% 0.40% 0.00% 0.49%
Difference TRUE 0.2 0.1 0.0 0.1Pass or Re-Calibrate Pass Pass Pass Pass
Engine #2 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
2.07 24.68 -0.22 24.66 799 6.30 10.40 83.30 29.42 28.05
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 452.9992
1.0160 0.84 41.050 97.60 81 33.562 4.594 0.1204 0.9990 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
0.7771 75.28 194,376 9,368 170,972.90 Enert >X
3D Pito #1 - Times
Date
Point No.∆P √∆P ts F tm F (in) tm F (out)
Final
Vf
Initial
Vi
1 0.62 0.787 800 76 77 765.10 709.20 55.90
2 0.62 0.787 801 77 80 719.50 690.80 28.70
3 799 76 84 596.10 591.20 4.90
4 800 75 87 826.80 818.70 8.10
5 799 74 88
6 799 72 89 2907.50 2809.90 Sum
7 798 72 89
8 797 71 90
9 797 72 91
10 797 73 92
11 798 75 93
12 798 76 95
1314
15
16
17
18
19
20
2122
23
24
Failed Bias Dialog
Failed Drift Dialog
Failed Cal Error Dialog
Failed Bias Dialog
Heber Unit 2 2024 NOx and CO rev
Division of Air Quality Stack Test Review of
Heber Light & Power
SO2 NOX CO CO2 O2 Engine #2
CS Calibration Span 247.00 25.30 11.97 20.45
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2Low-Level 0.00 0.00 0.00 0.00
Mid-Level 101.90 12.00 6.04 10.07High-Level 247.00 25.30 11.97 20.45
0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 41.3% 47.4% 50.5% 49.2%
100% of Cal. Span 100.0% 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 101.90 12.00 6.04 10.07
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2Low-Level 0.20 0.10 0.00 0.00
Mid-Level 99.90 12.00 6.00 10.20
High-Level 246.80 25.40 12.00 20.50
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 99.90 12.00 6.00 10.20
Low-Level 0.08% 0.40% 0.00% 0.00%
ppmv Difference 0.2 0.1 0 0
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.81% 0.00% 0.33% 0.64%
ppmv Difference 2 0 0.04 0.13
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
High-Level 0.08% 0.40% 0.25% 0.24%
ppmv Difference 0.2 0.1 0.03 0.05
Status Passed Cal. Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.40 0.40 0.20 0.10 System Bias.
SBi - Zero Bias TRUE 0.08% 1.19% 1.67% 0.49%± 5% of Span
Difference TRUE 0.2 0.3 0.2 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.60 11.90 6.10 10.10
SBi - Up-Scale Bias TRUE 0.69% 0.40% 0.84% 0.49%
Difference TRUE 1.7 0.1 0.1 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:7/17/2024 SO2
SO2 NOX CO CO2 O2 NOX125.90 3.50 6.60 9.80 CO
0.0% 51.0% 13.8% 55.1% 47.9% CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.40 0.30 0.20 0.10 System Bias.
SBi - Zero Bias TRUE 0.08% 0.79% 1.67% 0.49%± 5% of Span
Difference TRUE 0.2 0.2 0.2 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 101.50 11.90 6.10 10.20
SBi - Up-Scale Bias TRUE 0.65% 0.40% 0.84% 0.00%
Difference TRUE 1.6 0.1 0.1 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.00% 0.40% 0.00% 0.00% Response Spec.
Difference TRUE 0.0 0.1 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass Pass
Up-scale Gas Drift TRUE 0.04% 0.00% 0.00% 0.49%
Difference TRUE 0.1 0.0 0.0 0.1Pass or Re-Calibrate Pass Pass Pass Pass
Engine #2 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
2.07 24.68 -0.22 24.66 800.58 6.60 9.80 83.60 29.45 28.05
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 457.6499
1.0160 0.84 42.370 101.50 86.71 34.280 4.778 0.1223 0.9990 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
0.7765 75.27 194,042 9,367 170,306.24 Enert >X
3D Pito #1 - Times
Date
Point No.∆P √∆P ts F tm F (in) tm F (out)
Final
Vf
Initial
Vi
1 0.62 0.787 799 81 79 721.80 695.30 26.50
2 0.62 0.787 800 85 79 743.60 693.80 49.80
3 800 89 79 633.90 620.30 13.60
4 801 92 80 800.70 789.10 11.60
5 801 94 80
6 800 94 81 2900.00 2798.50 Sum
7 800 94 82
8 801 95 82
9 801 95 82
10 802 96 83
11 802 96 83
12 800 96 84
1314
15
16
17
18
19
20
2122
23
24