DAQ-2024-010454

1

DAQC-969-24
Site ID 10238 (B5)

MEMORANDUM

TO: CEM FILE – PACIFICORP – Huntington Power Plant

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Rob Leishman, Environmental Scientist

DATE: September 25, 2024

SUBJECT: Source: Huntington Power Plant Units 1 and 2
Contact: Russ Wilson – 435-687-4331
Location: Huntington Canyon, Emery County, UT
Test Contractor: Air Hygiene, Inc.
FRS ID#: UT00000049001501001
Permit/AO#: Title V operating permit #1501001005, dated January 22, 2020
Subject: Review of RA/PST Report dated May 28, 2024

On June 4, 2024, DAQ received a Relative Accuracy/Performance Specification Test (RA/PST) report for
the PacifiCorp Huntington Power Plant Units 1 and 2 in Huntington, UT. Testing was performed on April
10-11, 2024, to determine the relative accuracy of the CO2, NOx, SO2, and CO monitoring systems. The
DAQ-calculated test results are:

RA/PST EVALUATION:

Unit No. 1
NSPS RATA - Test Date - 4/10/2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status
SO2 Thermo Fisher 43iQ-ACAN 131 ppm 29.922 30.139 1.7% Passed
lbs/MMBtu 0.086 0.088 4.5% Passed
CO2 Thermo Fisher 410iQ-ACN 133 % 10.450 10.230 2.6% Passed
NOx Thermo Fisher 42iQ-ACANN 132 ppm 115.567 112.353 3.3% Passed
lbs/MMBtu 0.238 0.236 1.7% Passed
CO Thermo Fisher 48iQ-CAN ppm 63.678 60.348 17.9% Passed
lbs/MMBtu 0.081 0.075 5.2% Passed
Volumetric Flow Rate wscfh 79992356 79475462 1.6% Passed
Stack Test Deviation Report
There were no deviations observed during testing.
Calibration gases were in date and met performance specifications.

1 8 2
2

Unit No. 1
Acid Rain Tests - Test Date - 4/10/2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status Testing
Frequency
SO2 Thermo Fisher 43iQ-ACAN 131 ppm 29.922 30.138 5.00% Passed Annual
NOx Thermo Fisher 42iQ-ACANN 132 lbs/MMBtu 0.238 0.236 1.60% Passed Annual
CO2 Thermo Fisher 410iQ-ACN 133 % 10.456 10.239 2.61% Passed
Equation - Di (Rmi – CEMi)
Rmi = 0.2364
CEMi = 0.2381
Di = 0.0018 Passed

Unit No. 2
NSPS RATA - Test Date - 4/11/2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status
SO2 Thermo Fisher 43iQ-CAN 231 ppm 16.389 15.846 5.7% Passed
lbs/MMBtu 0.044 0.043 1.7% Passed
CO2 Thermo Fisher 410iQ-CAN 234 % 11.250 11.100 1.9% Passed
NOx Thermo Fisher 42iQ-ACANN 232 ppm 99.833 100.518 1.2% Passed
lbs/MMBtu 0.190 0.195 2.6% Passed
CO Thermo Fisher 48iQ-CAN ppm 122.711 119.552 5.5% Passed
lbs/MMBtu 0.145 0.142 5.4% Passed
Volumetric Flow Rate wscfh 69382345 69012770 1.6% Passed
Stack Test Deviation Report
There were no deviations observed during testing.
Calibration gases were in date and met performance specifications.

Unit No. 2
Acid Rain Tests - Test Date - 4/11/2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status Testing
Frequency
SO2 Thermo Fisher 43iQ-CAN 231 ppm 15.855 15.845 5.70% Passed Annual
NOx Thermo Fisher 42iQ-ACANN 232 lbs/MMBtu 0.190 0.195 2.70% Passed Annual
CO2 Thermo Fisher 410iQ-CAN 234 % 11.256 11.106 1.92% Passed
Equation - Di (Rmi – CEMi)
Rmi = 0.1946
CEMi = 0.1904
Di = 0.0042 Passed

DEVIATIONS: No deviations were noted in this report.

CONCLUSION: PacifiCorp operates the continuous emissions monitors (CEMs)
on the Huntington Power Plant Unit 1 and Unit 2 stacks to
measure CO2, NOx, SO2, and CO emissions. The CEMs were
audited by the DAQ and found to meet quality assurance
requirements found in 40 CFR Part 60, Appendix B,
Performance Specification 1, and R307-170, Continuous
3

Emission Monitoring System Program. Quarterly cylinder gas
audits and an annual relative accuracy test audit were conducted
in accordance with the procedures outlined in UAC R307-170.

RECOMMENDATION: The PacifiCorp Huntington Power Plant Units 1 and 2 CEM
systems were operating as required in R307-170 and 40 CFR
60.13 at the time of this evaluation.

HPV: No.

ATTACHMENTS: RATA Review Spreadsheets.
YHg.ffF"pRP ENERGY
Huntington Power Plant
6 miles west of Huntington, Utah on Hwy. 3l
P.O. Box 680
Huntington, Utah 84528
May 28,2024
Mr. Bryce Bird, Director
Utah Department of Environmental Quality
Division of Air Quality
195 North 1950 West
P. O. Box 144820
Salt Lake City, Utah 84114-4820
Attn: Mr. Rob Leishman
UTAH DFPARTMFNT OF
ENVIROI.JIIENTAL OUALITY
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RE: 2024 RATA Reports
Dear Mr. Bird,
The Annual Source Emission Test Reports, or Relative Accuracy Test Audits (RATAs) of the Continuous
Emissions Monitoring Systems (CEMS) in service at the PacifiCorp Huntington Plant Units 1 and 2 have
been completed per the specifications found in 40 CFR Part 60 and 75. The low-load, and high-load Flow
RATAS, along with the high-load Gas RATAs were conducted on April 11th and April 30th, 2024.
Enclosed are the RATA reports for the Huntington Plant Units 1 and 2 Flow and Gas CEMS.
I am authorized to make this submission on behalf of the owners and operators of the affected source or
affected units for which the submission is made. I certify under penalty of the law that I have personally
examined, and am familiar with, the statements and information submitted in this document and its
attachments. Based on my inquiry of those individuals with primary responsibility for obtaining the
information, I certify that the statements and information are to the best of my knowledge and belief true,
accurate, and complete. I am aware that there are significant penalties for submitting false statements
and information or omitting required statements and information, including the possibility of fine or
imprisonment.
Should youlhave any questions or concerns please contact Terry Guthrie, Hunter and Huntington Plant
Environm/ntal tvfnaOer at (435) 6874334.
Sincerely,
,.-\ /,^-=.
tLaren Hu
Managing Director - Hunter and Huntington Plants
Responsible Official
Enclosures: "Source Test Report tor 2024 RATA Testing Unit 1 &
cc:
Scarlet Jackson - NTO w/o enclosure
Youn Joo Kim - EPA Region VlllMenclosure
Russ Willson - Huntington Plant w/enclosure
Tom \Mscomb - NTO w/o enclosure
Unit 2"
Source Test Report for 2O24 RATA Testing
Unitl&Unit2
PacifiCorp
Huntington Power Plant
Huntington, Utah
Prepared For:
PacifiCorp
l4O7 W North Temple, Suite 210
Salt Lake City, Utah 84116
Prepared By:
Montrose Air Quality Services, LLC
990 West 43rd Avenue
Denver, Colorado 80211
For Submission To:
Utah Division of Air Quality
195 North 1950 West
Salt Lake City, Utah 84116
Document Number: GPO43AS-O36878-RT-1-579
Test Dates: April 11 & 30,2(J24
Submittal Date: May 3O, 2024
STAE
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DIVISION OF AIR OUALITY
M M?NISHIA
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Review and Ceftification
All work, calculations, and other activities and tasks performed and presented in this
document were carried out by me or under my direction and supervision. I hereby certify
that, to the best of my knowledge, Montrose operated in conformance with the
requirements of the Montrose Quality Management System and ASTM D7036-04 during this
test project.
Signature:
Name:
May L3,2024
Title: project Manager
I have reviewed, technically and editorially, details, calculations, results, conclusions, and
other appropriate written materials contained herein. I hereby certify that, to the best of my
knowledge, the presented material is authentic, accurate, and conforms to the requirements
of the Montrose Quality Management System and ASTM D7O36-O4.
Signature:
Name:
l{ay 13,2024
QA/QC Specialist
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Matthew Parks
G P043AS-036878-RT- 1 579 Page 2 of 290
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Table of Contents
Paqe
1.0 Introduction........ ......,........... 5
1.1 Summary of Test Program ...,.....,..... 5
1.2 Key Personnel........... ................. 9
2.0 Plant and Sampling Location Descriptions............. .........11
2.L Process Description, Operation, and Control Equipment............ ............11
2.2 Flue Gas Sampling Locations .........11
2.3 Operating Conditions and Process Data., ............11
2.4 CEMS Description ........t2
3.0 Sampling and Analytical Procedures ..............13
3.1 Test Methods............ .....13
3.1.1 EPA Method 2G ........... ................13
3.1.2 EPA Method 2H............ ..............15
3.1.3 EPA Method 4............. ....16
3.1.4 EPA Methods 3A, 6C, 7E, and 10 ........... ................18
3.2 ProcessTestMethods....... .......19
4.0 Test Discussion and Results....,.... ..........20
4.L Field Test Deviations and Exceptions.. .............20
4.2 Presentation of Resu1ts.............. ..............20
5,0 Internal QA/QC Activities ...........2t
5.1 QA/QC Audits ...................21
5.2 QA/QC Discussion. ...................21
5.3 Quality Statement ..........21
List of Appendices
A Field Data and Calculations . ......22
A.1 Sampling Locations.. ......23
A.2 RATA Results....... ......25
A.2.1 Unit 1............. ..........26
A.2.2 Unit 2 .....33
A.3 Field Data ...................40
A.3.1 Unit 1...... .......4L
A.3.1.1 Low-Load Flow Data ...............42
A.3.1.2 High-Load Flow Data ..................63
A.3.1.3 Instrumental Test Method Data......... ..............85
A.3.2 Unit 2......... ...............93
A.3.2.1 Low-Load Flow Data ......94
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A.3.2.2 High-Load Flow Data ...115
A.3.2.3 InstrumentalTest Method Data......... ..........131
A.4 Example Calculations.......... .............145
B Facility Process Data........ ............154
8.1 Unit 1 ...........155
B.1.1 Low-Load Flow RATA........ .............156
B.1.2 High-Load Flow RATA. ....166
B.1.3 Gas RATAs..,.... ...L77
8.2 Unit 2............. ................188
B.2.1 Low-Load Flow RATA........ ..............189
B.2.2 High-Load Flow RATA. ....199
8.2.3 Gas MTAs...... ..............210
C Quality Assurance/Quality Control ..........22t
C.l Units and Abbreviations............ ......222
C.2 Manual Test Method QA/QC Data........ ............230
C.3 Instrumental Test Method QA/QC Data........ ....238
C.3.lUnit 1............. .............239
C.3.2 Unit 2............. .............256
C.4 Calibration Gas Certificates......... ....272
C.5 Accreditation Information/Ceftifications ...........284
List of Tables
Table 1-1 Summary of Test Pro9ram............. ................5
Table 1-2 Summary of RATA Results - Huntington Unit 1.............. .................7
Table 1-3 Summary of RATA Results - Huntington Unit 2............. .................. B
Table 1-4 Test Personnel and Observers........... ............10
Table 2-1 Sampling Locations.........,.. .,........11
Table 2-2 CEMS Information .........12
List of Figures
Figure 3-1 EPA Method 2G Sampling Train ......L4
Figure 3-2 EPA Method 4 Sampling Train........ ...............17
Figure 3-3 EPA Methods 3A, 6C, 7E, and 10 Sampling Train ............19
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1.O Introduction
1.1 Summary of Test Program
PacifiCorp contracted Montrose Air Quality Services, LLC (Montrose) to perform a MTA test
program at Huntington Power Plant located in Huntington, Utah. The tests were conducted
in accordance with the requirements of UDEQ Operating Permit 1501001004 and (as
applicable) 40 CFR Parts 60 and 75.
The specific objectives were to:
o Perform annual RATAs on the Volumetric Flow Rate, Carbon Dioxide, Sulfur
Dioxide, Nitrogen Oxides and Carbon Monoxide CEMS installed on Units 1 and
2.
o Conduct the test program with a focus on safety
Montrose peformed the tests to measure the emission parameters listed in Table 1-1.
Table 1-1
Summary of Test Program
To simplify this report, a list of Units and Abbreviations is included in Appendix C.1.
Throughout this report, chemical nomenclature, acronyms, and reporting units are not
defined. Please refer to the list for specific details.
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GP043AS-036878-RT- 1 579
4/tL/2024 Huntington
Unit 2
Low Volumetric Flow Rate MTA EPA M2G/H, 3, 4 9 >5
High Volumetric Flow Rate RATA EPAM2G/H,3,4 9 >5
High Oz, COz, SOz, NOx, CO MTAsx EPA M3A, 6C,7E, and 10 9 2t
4/s0/2024 Huntington
Unit 1
Low Volumetric Flow Rate MTA EPAM2G/H,3,4 9 >5
High Volumetric Flow Rate MTA EPAMZG/H,3,4 9 >5
High Oz, COz, SOz, NO*, CO MTAs EPA M3A, 6C,7E, and 10 9 2t
Page 5 of 290
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This report presents the test results and supportlng data, descriptions of the testing
procedures, descriptions of the facility and sampllng locations, and a summary of the quatity
assurance procedures used by Montrose. The average emission test results are summarized
and compared to their respective performanc€ specifications in Tables 1-2 through 1-4.
Detailed results for individual test runs and all supportlng data can be found in the
appendlces.
The testlng was conducted by the Montrose personnel listed in Table 1-5. The tests were
conducted accordlng to the test plan (protocol) that was submitted to and approved by
UDEQ.
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Table 1-2
Summary of RATA Results - Huntington Unit 1
April 1O & 30, 2024
Part 6O
Sulfur Dioxide (SOz)
lb/mmBtu PS-2 < 20.0olo of RM 3,70/o
lb/hr PS-6 < 20.0olo of RM 2.4o/o
Nitrogen Oxides (NOx as NOz)
ppmvw PS-2 < 20.0olo of RM 3.2o/o
lb/hr PS-6 < 20.0olo of RM 3.5o/o
Carbon Monoxide (GO)
ppmvw PS-4A 3 5olo of AS 3.7olo
lblmmBtu PS-5 < 20.0olo of RM L5.Oo/o
lb/hr PS-6 3 20.0olo of RM L7.Solo
Part 75
Volumetric Flow (Low Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 5.Oolo
Volumetric Flow (High Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM L.1o/o
Carbon Dioxide (COz)
o/o volume wet App. B Sect. 2.3.1.2 Annual: 5 7.5olo of RM 2.5o/o
Sulfur Dioxide (SOz)
ppmvw App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM L.2o/o
Nitrogen Oxides (NO, as NOz)
lblmmBtu App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM L.5o/o
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Table 1-3
Summary of RATA Results - Huntington Unit 2
April 11, 2()24
Part 6O
Sulfur Dioxide (SOz)
lblmmBtu PS-2 < 20.0olo of RM 2.3o/o
lblhr PS-6 S 20.0olo of RM 6.4o/o
Nitrogen Oxides (NOx as NOz)
ppmvw PS-2 < 20.0olo of RM O.2o/o
lb/hr PS-6 < 20.0olo of RM L.5o/o
Carbon Monoxide (CO)
ppmvw PS-4A S 10o/o of RM 7.lolo
lblmmBtu PS.6 S 20.0olo of RM 3.2o/o
lblhr PS-5 S 20.0olo of RM tO.Oolo
Part 75
Volumetric Flow (Low Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 2.3o/o
Volumetric Flow (High Load)
wscfh App, B Sect. 2.3.1.2 Annual: < 7.5olo of RM 7..5o/o
Carbon Dioxide (COz)
o/o volume wet App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM l.8o/o
Sulfur Dioxide (SOz)
ppmvw App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 5.9o/o
Nitrogen Oxides (NO, as NOz)
lblmmBtu App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 3.8o/o
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GP043AS-036878-RT- 1 579 Page 8 of 290
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L.2 Key Personnel
A list of project participants is included below:
Facllity Information
Source Location: PaclfiCorp
Huntlngton Wyoming Plant
8 Mlles West of Huntington on Hwy 31
Project Contact: Tom Wlscomb
Role: Sr. Environmental Advisor
Company: PaciflCorp
Telephone: (80r) 220-2373
Emall : [e-mail]
Agency Informatlon
Regulatory Agency: Utah Department of Air Quallty
Agency Contact: Rob Lelshman
Telephone: [phone]
Email: [e-mail]
Tectlng Company Informatlon
Testing Firm: Montrose Alr Quallty Services, LLC
Contact: Cralg Kormylo
Title: Dlstrlct Manager
Telephone: [phone]
Email: [e-mail]
Russell Wlllson
Senior Environmental Analyst
PacifiCorp
(43s) 687-4331
Russel !. Wl I lson@ Pacifi Corp. com
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Test personnel and observers are summarized in Table 1-4.
Table 1-4
Test Personnel and Observerc
Craig Kormylo
Project Manager
Qualified Individual (QI)
Trailer operator
Sample train operator
Sample train operator
Sample train operator
Marcus Martello-Trotter Sample train operator
Calculations and report preparation
Test Coordinator
Plant Representative
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GP043AS-036878-RT- 1 579 Page 10 of 290
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2.O Plant and Sampling Location Descriptions
2.1 Process Description, Operation, and Control
Equipment
The Huntington Plant comprises two pulverized coal-fired boilers. Huntington Unit #1 is
equipped with low-NO, burners and overfire air for nitrogen oxides (NO,) control, a flue gas
desulfurization (FGD) scrubber for sulfur dioxide (SOz) control and pulse-jet fabric filters for
particulate matter (PM) control. Huntington Unit #2 is equipped with low-NOx burners and
overfire air for NOx control, an FGD scrubber for SOz control and pulse-jet fabric filters for
PM control.
2.2 Flue Gas Sampling Locations
Information regarding the sampling locations is presented in Table 2-1.
Table 2-1
Sampling Locations
Sample location(s) were verified in the field to conform to EPA Method 1.
See Appendix A.1 for more information.
2.3 Operating Conditions and Process Data
Emission tests were performed while the source/units and air pollution control devices were
operating at the conditions required by the relevant performance specifications. The units
were tested when operating within the load levels required by 4Q CFR Paft 75.
Plant personnel were responsible for establishing the test conditions and collecting all
applicable unit-operating data. The process data that was provided is presented in Appendix
B. Data collected includes the following parameters:
. Unit Load (MW)
. Relevant CEMS Parameters
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2.4 CEMS Description
Information regarding the monitoring systems is presented in Table 2-2.
Table 2-2
CEMS Information
Unit 1
Flow Teledyne Monitor Labs Model 150 136
COz Thermo Fisher Model 410|Q-ACN 133
SOz Thermo Fisher Model 43|Q-CAN 131
NOx Thermo Fisher Model 42iQ-ACANN L32
co Thermo Fisher Model 48iQ-CAN
Unit 2
Flow Teledyne Monitor Labs Model 150 236
COz Thermo Fisher Model 410|Q-CAN 234
SOz Thermo Fisher Model 43|Q-CAN 23L
NOr Thermo Fisher Model 42|Q-ACANN 232
co Thermo Fisher Model 48|Q-ACN
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3.O Sampling and Analytical Procedures
3.1 Test Methods
The test methods for this test program have been presented in Table 1-1. Additional
information regarding specific applications or modifications to standard procedures is
presented below.
3.1.1 EPA Method 2G, Determination of Stack Gas Velocity and
Volumetric Flow Rate with Two-Dimensional Probes
EPA Method 2G is used to measure the velocity pressure and the yaw angle of the flow
velocity vector in a stack or duct using a 2-D probe. Alternatively, these measurements are
made by operating one of the three-dimensional (3-D) probes described in Method 2F,in
yaw determination-only mode. From these measurements and a determination of the stack
gas density, the average near-axial velocity of the stack gas is calculated. The near-axial
velocity accounts for the yaw, but not the pitch, component of flow. The average gas
volumetric flow rate in the stack or duct is then determined from the average near-axial
velocity.
Pertinent information regarding the performance of the method is presented below:
o Method Options:
o None
o Method Exceptions:
o None
. Target and/or Minimum Required Sample Duration: 5 minutes
The typical sampling system is detailed in Figure 3-1.
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GP043AS-036878-RT- 1 579 Page 13 of 290
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Figure 3-1
EPA Method 2G Sampllng Train
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3.L.2 EPA Method 2H, Determination of Stack Gas Velocity Taking
into Account Velocity Decay Near the Stack Wall
EPA Method 2H is used to measure the stack gas velocity for calculating the volumetric flow
rate while taking wall effects into account. To do this, a wall effects adjustment factor is
determined. The factor is used to adjust the average stack gas velocity obtained using EPA
Method 2,2F, or 2G while taking velocity decay near the stack or duct wall into account.
The method contains two possible procedures: a calculational approach which derives an
adjustment factor from velocity measurements and a default procedure which assigns a
generic adjustment factor based on the construction of the stack or duct.
The calculational procedure derives a wall effects adjustment factor from velocity
measurements taken using Method 2,2F, or 2G at 16 (or more) traverse points specified in
EPA Method 1 and a total of eight (or more) wall effects traverse points specified under this
method. The calculational procedure based on velocity measurements is not applicable for
horizontal circular ducts where build-up of pafticulate matter or other material in the bottom
of the duct is present.
A default wall effects adjustment factor of 0.9900 for brick and mortar stacks and 0.9950
for all other types of stacks and ducts may be used without taking wall effects
measurements in a stack or duct.
When the calculational procedure is conducted as part of a relative accuracy test audit
(RATA) or other multiple-run test procedure, the wall effects adjustment factor derived from
a single traverse (i.e., single RATA run) may be applied to all runs of the same RATA
without repeating the wall effects measurements. Alternatively, wall effects adjustment
factors may be derived for several traverses and an average wall effects adjustment factor
can be applied to all runs of the same RATA.
Pertinent information regarding the performance of the method is presented below:
o Method Options:
o None
o Method Exceptions:
o None
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GP043AS-036878-RT- 1 579 Page 15 of 290
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3.1.3 EPA Method 4
Determination of Moisture Content in Stack Gas
EPA Method 4 is a manual, non-isokinetlc method used to measure the moisture content of
gas streams. Gas is sampled at a constant sampling rate through a probe and impinger
train. Moisture is removed using a serles of pre-weighed lmpingers containing methodology-
speciflc liquids and silica gel lmmersed ln an ice water bath. The implngers are weighed
after each run to determlne the percent moisture.
Pertinent information regarding the performance of the method is presented betow:
o Method Options:
o None
r Method Exceptlons:
o None
The typical sampling system is detailed in Flgure 3-2.
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Figure 3-2
EPA Method 4 Sampling Train
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GP043AS-036878-RT-1 579
SAMPI.E LINE
(stadard tp)- VACUUM.- LNE
BY-PASSVALVE(6mlrljud) VACUUM GAUGE
THERMOCoIJPLESII
MANOITETER ------D
Page 17 of 290
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3.1.4 EPA Methods 3A, 6C, 7E, and 1O
Determination of Oxygen, Carbon Dioxide, Sulfur Dioxide, Nitrogen Oxides,
and Carbon Monoxide Concentrations in Emissions from Stationary Sources
(Instrumental Analyzer Procedures)
Concentrations of Oz, COz, SOz, NOx, and CO are measured simultaneously using EPA
Methods 34, 6C, 7E, and 10, which are instrumental test methods. Conditioned gas is sent
to a series of analyzers to measure the gaseous emission concentrations. The performance
requirements of the method must be met to validate the data.
Pertinent information regarding the performance of the method is presented below:
o Sampling is performed using a dilution probe
o A nondispersive infrared analyzer is used to measure COz
o An ultraviolet absorption analyzer is used to measure SOz
o A chemiluminescent analyzer is used to measure NOx
o A gas filter correlation nondispersive infrared analyzer is used to measure
co
o NO and NOz are measured separately and summed to report NOx
emissions
o Gas stratification testing is performed across a grid of 12 points
determined using EPA Method 1 in accordance with 40 CFR Part 60,
Appendix B, PS2 58.1.3.2 and 40 CFR Part 75, Appendix A, 96.5.6.1.
Stratification testing is performed for two minutes per traverse point in
accordance with 40 CFR Part 75, Appendix A, 95.5.6.1(c). If diluent and
pollutant concentrations are within 5o/o of their mean concentrations,
subsequent gas RATA testing is performed at a single point in the stack as
allowed by 40 CFR Part 60, Appendix B, PS2 5B.1.3.2 and 40 CFR Paft 75,
Appendix A 56.5.6.3(b). If diluent and pollutant concentrations are within
10o/o of their mean concentrations, RATA testing is performed at three
points located 0.4 meter, 1.0 meter and 2.0 meters from the stack wall,
as required by 40 CFR Part 60, Appendix B, PS2 58.1.3.2 and 40 CFR Part
75, Appendix A, 96.5.6.1(a).
The typical sampling system is detailed in Figure 3-3.
'a
| /.r ^ r- t I .l . ..
GP043AS-036878-RT-1579 Page 18 of 290
I r0
Figure 3-3
EPA Methods 3A (OzlCOz), 6C, 7E, and 1O Sampling Train
3.2 Process Test Methods
The test plan did not require that process samples be collected during this test program;
therefore, no process sample data are presented in this test report.
Erhaust
/ Calibrdion Gas
SIGNAL
EfEust
Samplr / Calbration Gas
SIGNAL
s------
SIGNAL
.Af,TR'
iOTAITIRSWTH
FI'YIC ffTiOL
VAES
*!
!SROIflETEi
WTH fLflCOXTiC
VAE
HEATEO
SAMPLE
UNE
#!
I
iT{
SPU'ADB?S'
iOTT:TERSHTHfLffcdna vaws
CALIBRATION
GAS UNE
tt
/ rl I t-f a r I .l
GP043AS-036878-RT-1 579 Page 19 of 290
i-1
Irl
o Do
!ri'r ,r ,, 11 {-i,il i i l \' ,i li: l:i',,'i,l-. [r:,
4.O Test Discussion and Results
4.L Field Test Deviations and Exceptions
Due to powerllne distribution restrictions, the testing performed on April 10th could not be
completed at high load. The Unit I high load testlng was completed on April 30, 2024. No
further fleld deviations or exceptions from the test plan or test methods were ldentified by
the project manager during thls test program.
4.2 Presentation of Results
The average results are compared to the permlt limits in Tables 1-2 and 1-3. Emissions
are repofted in units consistent with those in the appllcable performance speciflcations.
Additlonal informatlon ls included ln the appendlces as presented in the Table of Contents.
Fa cif rClnp
2124 i.ATA Rep.rt. Huntnr{t.n Ftwe; iiant
GP043A5-036878-RT- 1 s79 Page 20 of 290
o ro
5.O Internal QA/QC Activities
5.1 QA/QC Audits
The meter boxes and sampling trains used during sampling performed within the
requirements of their respective methods. All post-test leak checks, minimum metered
volumes, and minimum sample durations met the applicable QA/QC criteria, except where
noted in Section 5.2.
EPA Method 3A, 6C, 7E, and 10 calibration audits were all within the measurement system
performance specifications for the calibration drift checks, system calibration bias checks,
and calibration error checks, except where noted in Section 5.2.
The NOz to NO converter efficiency check of the analyzer was conducted per the procedures
in EPA Method 7E, Section 8.2.4. The conversion efficiency met the criteria, except where
noted in Section 5.2.
5,2 QA/QC Discussion
All QA/QC criteria were met during this test program.
5.3 Quality Statement
Montrose is qualified to conduct this test program and has established a quality
management system that led to accreditation with ASTM Standard D7O36-O4 (Standard
Practice for Competence of Air Emission Testing Bodies). Montrose participates in annual
functional assessments for conformance with D7036-04 which are conducted by the
American Association for Laboratory Accreditation (A2LA). All testing performed by Montrose
is supervised on site by at least one Qualified Individual (QI) as defined in D7036-04
Section 8.3.2. Data quality objectives for estimating measurement uncertainty within the
documented limits in the test methods are met by using approved test protocols for each
project as defined in D7036-04 Sections 7.2.L and 12.10. Additional quality assurance
information is included in the report appendices. The content of this report is modeled after
the EPA Emission Measurement Center Guideline Document (GD-043).
aa
| / ,r r ,-ta r | .O - .
GP043AS-036878-RT- 1 579 Page 21 of 290
Appendix A
Field Data and Calculations
GP043AS-036878-RT- 1 s79 Page 22 ot 290
I rl
Appendix A.1
Sampling Locations
| / rr r, ,a rO tl - .
GP043AS-035878-RT- 1 579 Page 23 of 290
O 1l
Unit
Diameter (D)
Upstream Distance (A)
Traverse Point 1
Traverse Point 2
Traverse Point 3
1
323.3',
>220'
2
322.7',
>220'
>266',Downstream Distance (B) >266'
Sample Polnt Dlstances from Stack Wall
14.1"
47.3"
95.7',
14.1"
47.3"
95.5"
Volumetric FIow Rate Sample Points
Unlt
Diameter (D)
Upstream Distance (A)
Downstream Distance (B)
Sample Polnt Dlstances from Stack Wall
Traverse Point 1
Traverse Point 2
Traverse Point 3
Traverse Point 4
12
323.3" 322.7">220', >220'>266', >266',
10.4" 10.4"33.9', 33.8',62.7" 62.5"
104.5', 104.3',
Pacificorp Huntington Power Plant sampling Locations
Pollutant Stratification Test Points
Stack Cross Section (A-A)
+++ + + +++
12 3 a a 3 2t
Stack Cross Section (A-A)
ta
a r ,r r ?-,0
GP043AS-036878-RT-1 579 Page 24 of 290
a ro
Appendix A.2
RATA Results
Da
| , '^ . ,- a r O ,l . ..
GP043AS-036878-RT- 1 579
T
Page 25 of 290
Appendix A.2.1
Unit 1
Page 26 of 290
PacifiCorp
Huntington 1
low Load Flow RATA
4lLO/2O24
Parameter:Exhaust Gas Flow (wscfhl
Run f
1
2
3
4
5
6
7
8
9
10
LI
12
190
189
190
189
190
19r
190
189
190
6:25 6:43
6:45 6:59
7:Ol 7t13
7i22 7t3l
7:33 7i42
7:44 7:52
7:54 8:03
8:05 8:ll
8:13 8:20
Start Tlme Stop Tlme Unlt Load Dlfference Use?
-1,096,000 Yes
-1,597,000 Yes
-1,552,000 Yes
-1,452,000 Yes
-1,204,000 Yes
-1,474,000 Yes
-1,688,000 Yes
-2,L67,OOO Yes
-L,475,OOO Yes
Yes
No
No
WAF Applied?
RATA Results
Number of Runs: 9
T-value 2.306
Standard Deviation 30&078
Confidence Coefficient 236,810
Relative Accuracy (%RM) 4.97%
Bias Adjustment Factor 1.000
RA<10% (semFAnnual)
RM
35,678,000
35,298,000
35,498,000
35,564,000
36,257,000
35,746,000
35,545,000
35,569,000
35,740,000
CEM
36,774,000
36,895,000
37,160,000
37,015,000
37,451,000
37,220,000
37,233,000
37,736,@0
17,2t5,000
Average 190 35,6s5,(xl0 33,471,qr0 -1,535,0q1
GP043AS-036878-RT- 1 579 Page 27 of 290
PaciliColp
Huntlngton 1
Hlth Load Flow RATA
413012024
Param€ter: Exhaust Gas Flow (wscfhl No
Run fl
1
2
3
4
5
6
7
8
9
10
11
L2
Start nme Stop Tlme Unit Load
74:45 15:22
15:38 15:58
16:14 15:34
16:50 l7:1O
L7t25 17:45
17:58 18:18
18:33 18:53
19:09 L9:29
79:44 20:Q4
Dlfference Use?
162,000 Yes
-800,000 Yes
-1,257,W Yes
-758,000 Yes
1,251,000 Yes
1,362,000 Yes
L77,000 Yes
706,000 Yes
470,000 Yes
Yes
No
No
WAF Applied?
RAIA Resulk
Number of Runs: 9
T-value 2.305
Standard Deviation 921,955
Confidence Coefficient 708,576
Relative Accuracy (%RM) l.O7%
Bias Adjustment Factor 1.000
RA<10% (semi-Annual)
489
489
490
49L
491
486
452
451
46L
RM
80,773,000
80,318,000
80,426,000
79,276,000
80,119,000
80,034,000
80,189,000
80,28&000
79,AzL,0@
CEM
80,511,000
81,118,000
81,583,000
80,034,000
78,868,000
78,672,000
80,012,000
79,582,000
79,351,000
Average tt80 80,t78,222 71,993,l(x'145,889
G P043AS-036878- RT-1 579 Page 28 of 290
Job Code PROJ-036878
Pacificorp, Huntingon Unit 1
Test Date: 4l3ol24
Parameter:cO2 (%vw)
Run #
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
Load
489
489
490
49t
491
486
462
457
467
RM
LO.4
10.4
10.3
10.4
LO.7
10.5
9.9
9.9
9.8
CEM
10.5
10.5
10.5
to.7
10.9
to.7
10.0
10.1
10.1
Start Time End Time
L4:46 15:72
15:38 15:58
15:14 15:34
15:50 L7:LO
\7:25 77:45
17:58 18:18
18:33 18:53
19:09 !9:29
!9:44 2O:04
Difference Used?
-0,2 x
-0.1 x
-o.2 x
-0.3 x
-O.2 x
-0.2 x
-0.1 x
-0.2 x
-0.3 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P7S, Annuahoz I Coz%
9
2.306
0.1
0.1
2.5%
nla
nla
nla
Relative Accuracy Limit:
RA<l.s%o or t0.7o/o
Average la0 10,510.3 -0.2
Parameter:NOx (lb/mmBtul
Run f
1
2
3
4
5
6
7
8
9
10
11
L2
13
L4
15
Load
489
489
490
49t
49L
485
462
46L
461
RM
0.238
o.237
0.235
0.220
o.276
0.2L7
0.2s5
0.251
0.255
CEM
o.243
0.240
o.237
0.219
0.220
0.218
0.259
0.253
o.254
Start Time End Time
L4:46 L5:22
15:38 15:58
16:14 t6:34
16:50 17:L0
!7:25 77:45
17:58 18:18
18:33 18:53
19:09 19:29
!9:44 20:44
Difference Used?
-0.005 x
-0.003 x
-0.002 x
0.001 x
-0.004 x
-0.001 x
-0.003 x
-0.002 x
0.001 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: NOx lb/mmBtu
9
2.305
0.002
0.002
L.s%
n/a
nla
1.000
Relative Accuracy Limit:
RA<7.5% or t0.015 lb/mmBtu
Average It80 0.236 0.238 -0.002
Parameter:SO2 (ppmvwl
Run f
1
2
3
4
5
6
7
8
9
10
11
t2
13
74
15
Load
489
489
490
491
497
486
462
46r
46t
RM
30.2
24.6
74.9
29.7
32.2
34,4
30.0
31.5
33.1
CEM
30.3
24.4
25.4
29.8
32.1
33.7
29.8
31.1
33.0
-0.1
0.2
-0.5
-0.1
0.1
o.7
o.2
0.4
0.1
9
2.305
0.3
0.3
1.2%
nla
n/a
1.000
Start Time End Time
74:46 t5:22
15:38 15:58
75:14 15:34
15:50 L1:!O
L7:25 !7:45
17:58 18:18
18:33 18:53
19:09 19:29
!9:44 20:04
Difference Used?RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: SO2 / NOx ppm
Relative Accuracy Limit:
RAs7.5% or !12.0ppm
Average 30.0
GP043AS-036878-RT-1 579
480 30.1 0.1
Page 29 of 290
Job Code PROJ-036878
PacifiCorp, Huntington Unit 1
Test Date: 4l3ol24
Parameter:NOx (ppmvwl
Run #
1
2
3
4
5
6
7
8
9
10
t7
72
13
14
15
Load
489
489
490
497
49L
485
462
467
461
RM
tLs.Z
114.3
7L2.9
105.9
107.5
105.0
LLl.7
115.0
L76.2
CEM
119.5
rL7.4
115.5
109.0
111.1
108.9
121.0
118.1
119.3
Start Time End Time
14:45 15:22
15:38 15:58
76:t4 16:34
15:50 17:10
77:25 77:45
17:58 18:18
18:33 18:53
19:09 79:29
19:44 20:04
Difference Used?
-4.3 x
-3.1 x
-2,7 x
-2.1 x
-3.5 x
-2.9 x
-3.3 x
-3.1 x
-3.1 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O, PS2: SO2 / NOx ppm
9
2.306
0.6
0.5
3.2%
n/a
nla
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 480 -3.1L12.4 115.5
Parameter:SO2 (lb/mmBtul
Run f
L
2
3
4
5
6
7
8
9
10
L7
72
13
t4
15
[oad
489
489
490
49L
491
486
462
46L
467
RM
0.087
o.077
o.o72
0.08s
0.090
0.098
0.091
0.096
0.101
CEM
0.085
0.059
o.o72
0.083
0.088
0.094
0.089
0.092
0.098
Start Time End Time
L4:46 !5:22
15:38 15:58
76:L4 16:34
15:50 77:LO
!7:25 !7:45
17i58 18:18
18:33 18:53
19:09 L9:29
19:M 20:04
Difference Used?
0.002 x
0.002 x
0.000 x
0.002 x
0.002 x
0.004 x
0.002 x
0.004 x
0.003 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS2r SO2 / NOx ppm
9
2.306
0.001
0.001
3.7%
nla
n/e
nla
Relative Accuracy Limit:
20% RM or 10%EL
Averate 480 0.088 0.086 0.002
G P043AS-036878-RT- 1 579 Page 30 of 290
Job Code PROJ-035878
Pacificorp, Huntington Unit 1
Test Date: 4l3gl24
Parameter:Nox (lb/hr)
Run #
1
2
3
4
5
6
7
8
9
10
11
!2
13
L4
15
Load
489
489
490
491
49L
486
462
46t
467
RM
1111.3
1095.0
1084.5
LO72.t
L028.4
1013.3
1126.8
1102.5
Lro7.2
CEM
1150.8
1138.0
!t27.5
1041.5
1045.5
L023.4
1155.7
1L22.5
1130.6
Start Time End Time
14:46 15:22
15:38 15:58
16:14 15:34
16:50 17:10
17:25 L7:45
17:58 18:18
18:33 18:53
19:09 L9:29
79:44 2O:O4
Difference Used?
-39.5 x
-42,0 x
-43,7 x
-29.4 x
-18.1 x
-10.1 x
-28.9 x
-20.0 x
-23.4 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS6: Mass Emissions
9
2.305
11.5
8.9
3.5%
nla
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 480 1075.8 1104.1 -28.3
Parameter:so2 llb/hrl
Run #
L
2
3
4
5
6
7
8
9
10
17
L2
13
t4
15
Load
489
489
490
497
491
486
462
451
461
RM
405.1
329.r
332.5
391.8
428.3
457.2
399.5
420.5
439.5
CEM
405.0
328.0
343.8
395.8
420.3
439.9
395.9
4LL.2
434.2
Start Tlme End Time
!4:46 L5:22
15:38 15:58
16:74 15:34
16:50 l7:1O
!7:25 !7:45
17:58 18:18
18:33 18:53
19:09 L9:29
L9:44 20:04
Difference Used?
1.1 x
1.1 x
-11.3 x
-4.0 x
8.0 x
17.3 x
3.6 x
9.3 x
5.3 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O, PS6: Mass Emissions
9
2.305
8.2
5.3
2.4%
n/a
nla
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average tt80 400.5 397.t 3,4
GP043AS-036878-RT- 1 579 Page 31 of 290
Job Code PROJ-036878
Pacificorp, Huntlngton Unit 1
Test Date: 4lr0l24
Parameter: CO (ppmvwl
Run #
1
2
3
4
5
6
7
8
9
10
tt
12
13
L4
15
Load
489
489
490
49t
49I
486
462
461
46r
RM
62.9
52.r
43.3
68.4
191.1
108.2
4.7
s.2
5.8
CEM
50.3
51.1
46.7
95.4
188.4
108.3
7.8
6.2
7.9
Start Time End Time
74:46 75:72
15:38 15:58
L6:14 16:34
16:50 tl:IO
t7:25 77:45
17:58 18:18
18:33 18:53
19:09 !9:29
t9:44 20:04
Difference Used?
2.6 x
1.0 x
-3.4 x
-28.0 x
2.7 x
-0.1 x
-3.7 x
-1.0 x
-L.L x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS4A: CO ppm <20O
Relative Accuracy Limit:
10% RM or 5%EL or I d | +CC<Sppm
9
2.305
9.5
7.3
17.80/o
289
3.7o/o
nla
Average 480 60.2 -3.463.7
Parameter:cO (lblmmBtul
Run #
1
2
3
4
5
6
7
8
9
10
11
72
13
14
15
Load
489
489
490
497
497
486
462
46r
467
RM
0.079
0.066
0.055
0.085
o.234
0.135
0.00s
0.007
0.009
CEM
0.o74
0.054
0.058
0.L77
0.227
0.131
0.010
0.008
0.010
Start Time End Time
!4:46 !5:22
15:38 15:58
16:14 16:34
16:50 L7:lO
77:25 17:45
17:58 18:18
18:33 18:53
19:09 !9:29
L9:44 2O:O4
Dlfference Used?
0.005 x
0.002 x
-0.003 x
-0.031 x
0.007 x
0.004 x
-0.005 x
-0.001 x
-0.001 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O PS6: Mass Emissions
9
2.306
0.011
0.009
t5.o%
n/a
n/a
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 480 0.075 0.078 -0.003
Parameter:co (lb/hrl
Run f
7
2
3
4
5
5
7
8
9
10
11
L2
13
L4
15
Load
489
489
490
49L
497
486
462
461
45t
RM
369.3
304.4
253.3
394.0
1113.3
529.8
24.2
30.5
39.4
CEM
353.0
301.6
277.O
555.3
1080.1
620.1
45.5
3s.8
45.8
Start Time End Time
74:46 75122
15:38 15:58
75:14 16:34
16:50 77:LO
!7:25 L7:45
17:58 18:18
18:33 18:53
19:09 t9:29
L9:44 2O:O4
Difference Used?
16.3 x
2.8 x
-23.7 x
-162.3 x
33.2 x
9.7 x
-2t.3 x
-5.2 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accurary (%EL)
Bias Adjustment Factor
P6Q PS5: Mass Emi$ions
9
2.306
57,7
44.0
L7.5%
1585
3.6%
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 368.4
GP043AS-036878-RT- 1 5 79
480 350.9 -17.4
Page 32 of 290
Appendix A.2.2
Unit 2
Page 33 of 290
PacmCorp
Huntlngton 2
low load Flow RATA
4ltu2c24
Parrmeter: Exhaust Gas Flow (wlcft)WAF Applied? Yes
Runf startrlm€ stopflmc unltload BM cEM Dlfference Use? RATARBults1 11:50 11:59 2O5 15,947,W 32490,000 -1,543,000 yes NnmbmiRm;2 12:01 12:08 197 35,719,000 35,96r.000 -U2,0@ yes T-vatue
9
2.3063 12:10 12:18 189 35,152000 34,273,000 884OOO Yes Standard Deviation 818,8254 L2:28 72136 190 34,835,000 34,463,000 372,0@ Yes Confldencecoefficient 629,4A45 12:38 !2:45 190 34648,000 34,443,000 205,000 Yes RelativeAccurasy(%RM) 2,Zg%6 !2:47 12:55 r92 34565,000 34451,000 115,OOO Yes BiasAdjustment Factor 1.OOO7 L2;57 13:04 190 34,579,000 34,739,000 -160,000 yes
8 13:06 13:11 190 35,5740m 3to12,o0o 562,000 Yes P7sRel.uv€Accura.vst ndards9 13:13 13:18 190 36,586,000 35,215,0@ L371,OOO yes RA<?i%lAnn,ra0-
10
11
L?.
No RA<10%(Semi-Annual)
No
No
AYerate 193 3s,290,111 35,r15,:tit3 t7t;t78
GP043AS-036878-RT-1579 Page 34 of 290
PacifiCorp
Huntlngton 2
High Load Flow RATA
4hr12024
Parameter:Erhaust Gas Flow (wscfh)
Run fl
1
2
3
4
5
6
7
8
9
10
11
t2
L4t42 15:19
15:32 15:52
16:05 16:25
16:37 16:57
17:10 L7t3O
77:44 18:04
t8:17 18:37
19:01 l9i2l
19:33 19:53
StartTlme StopTime UnitLoad Dlfference use?
104,000 Yes
-404,000 Yes
79,000 Yes
125,000 Yes
299,000 Yes
258,000 Yes
900,000 Yes
-1,556,000 Yes
-2,188,000 Yes
No
No
No
wAF Applied?
RATA Results
Number of Runs: 9
T-value 2.100
Standard Deviation 1,000,1107
Confidence Coefficient 758,979
Relative Accuracy (%RM) L.sL%
Bias Adiustment Factor 1.000
RA<10% (semi-Annual)
437
436
436
435
436
436
434
434
435
RM
69,595,000
68,273,000
58,921,000
69,0s9,000
68,925,000
69,339,000
59,490,000
68,927,000
69,427,O00
CEM
69,491,000
68,677,000
68,842,000
68,934,000
68,627,000
69,081,000
58,590,000
70,583,000
71,615,000
Average 435 59,105,333 69,182,222 -275,889
GP043AS-036878-RT- 1 579 Page 35 of 290
Job Code PROJ-O36878
PacifiCorp, HuntinSton Unit 2
Test Dat€: 4llLl24
Parameter: CO2 (%vw)
Run #
L
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
Load
437
436
436
435
436
435
434
434
43s
RM
77.2
77.2
71.2
tL,2
tL.2
7L.2
LL.2
10.9
10.8
CEM
11.4
11.3
LL,4
lL.4
L7.4
11.3
It.4
11.0
10.9
Start Time End Time
L4:42 15:19
15:32 15:52
16:05 t6:25
76:37 16:57
77:70 L7:30
t7:M 18:04
18:17 !8:37
19:01 19:21
19:33 19:53
Difference Used?
-0.2 x
-0.1 x
-0.2 x
-0.2 x
-0,2 x
-0.1 x
-o.2 x
-0.1 x
-0.1 x
RATA Results
Number of Runs;
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
RA<7.5% ot t0.7o/o
9
2.305
0.1
0.0
t.8%
nla
nla
n/a
Average 11.143s 11,3 -0.2
Parameler:NOx (lb/mmBtul
Run #
1
2
3
4
5
6
7
8
9
10
11
t2
13
t4
15
Load
437
435
436
435
435
436
434
434
435
RM
0.189
0.195
0.197
0.198
0.198
0.196
0.197
0.203
0.203
CEM
0.184
0.189
0.190
0.191
0.190
0.190
0.189
0.195
0.196
Start Tlme End Time
14:42 15:19
75:32 15:52
16:05 L6:25
15:37 L6:57
17:10 17:3O
t7144 18:04
18:77 18:37
19:01 t9:21
19:33 19:53
Difference Used?
0.005 x
0.005 x
0.007 x
0.007 x
0.008 x
0.006 x
0.008 x
0.007 x
0.007 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
RA<7.5% or t0.015 lblmmBtu
9
2.305
0.0
0.0
3.8%
n/a
n/a
1.035
Averate 0.007o.L97 0,191
Parameter:SO2 (Dpmvwl
Run fl
1
2
3
4
5
6
7
8
9
10
L7
L2
13
L4
15
Load
437
436
436
435
436
435
434
434
435
RM
77.1
!4.9
16.0
15,2
L4.7
15.8
15.8
16.3
16.3
CEM
L5.7
15.6
L6.7
15.7
15.6
15.5
16.4
t7.!
17.2
0.5
-o.7
-o.7
-0.5
-0.9
-0.7
-0,5
-0.8
-0.9
9
2.306
0.5
o.4
5.9%
n/a
n/a
1_000
Start Time End Time
14:42 15:19
15:32 15:52
16:05 16:25
t6:37 16:57
17:10 L7:3O
77:44 18:04
t8tL7 78:37
19:01 t9:21
19:33 19:53
Difference Used?RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coefficlent
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: SO2 / NOx ppm
Relative Accuracy Limit:
RA<7.5% or t12.0ppm
Average
GP043AS-036878-RT- 1 579
43s 15.8 16.4 -0.6
Page 36 of 290
Job Code PROJ-036878
PacifiCorp, HuntinSton Unit 2
Test Date: 4lL1l24
Parameter:NOx (ppmvw)
Run #
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
Load
437
436
435
435
436
435
434
434
435
RM
96.7
99.s
100.7
100.8
roo.7
99.8
100.2
100.5
99.4
CEM
97.4
99.5
100.5
100.8
100.3
99.9
100.2
100.5
99.3
Start Time End Time
!4:42 15:19
15:32 15:52
15:05 16:25
15:37 !6:57
77:70 L7:3O
77:44 18:O4
18:17 18:37
19:01 L9:21
19:33 19:53
Difference Used?
-0.7 x
0.0 x
0.1 x
0.0 x
0.4 x
-0.1 x
0.0 x
0.0 x
0.1 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accurary (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O PS2: SO2 / NOx ppm
9
2.306
0.3
0.2
0.2%
n/a
n/a
n/a
Relative Accuracy Limit:
20% RM or 10%EL
AveraSe 0.0435glt.8 99.8
Parameter: SO2 (lb/mmBtul
Run #
1
2
3
4
5
6
7
8
9
10
11
12
13
74
15
[oad
437
436
436
43s
436
436
434
434
43s
RM
0.047
0.041
0.044
0.041
0.040
0.043
0.043
0.046
o.047
CEM
0.044
0.041
0.044
0.041
0.041
0.044
0.043
0.045
o.o47
Start Time End Tlme
\4:42 15:19
15:32 L5:32
16:05 76:25
!6:37 L6:57
t7:!O 17:30
!7:44 18:04
78:77 78:37
19:01 t9:2!
19:33 19:53
Dlfference Used?
0.003 x
0.000 x
0.000 x
0.000 x
-0.001 x
-0.001 x
0.000 x
0.000 x
0.000 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6Q PS2: SO2 / NOx ppm
9
2.305
0.001
0.001
2.3o/o
nla
nla
nla
Relative Accuracy Limit:
2Oo/"RM or |O%EL
Avcrage 435 o.0tt4 0.043 0.000
G P043AS-036878-RT- 1 579 Page 37 of 290
Job Code PROJ-036878
Pacificorp, Huntington Unit 2
Test Date: 4lL,.l24
Parameter:so2 (lb/hr)
Run #
1
2
3
4
5
5
7
8
9
10
L7
L2
13
14
15
Load
437
436
436
435
436
436
434
434
43s
RM
200.0
L69.2
183.5
774.1
158.9
182.3
782.6
186.9
188.7
CEM
192.8
777.3
190.4
L79.5
777.6
189.5
185.8
199.9
204.1
Start Time End Time
14:42 15:19
15:32 15:52
16:05 16:25
L6:37 15:57
77:t0 L7:3O
77:M 18:04
t8:I7 18:37
19:01 !9:2L
19:33 19:53
Difference Used?
7.2 x
-8.1 x
-5.8 x
-5.4 x
-8.7 x
-7.2 x
-4.2 x
-13.0 x
-15.4 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P5O PSG: Mass Emissions
9
2.306
5.3
4.9
6.4%
n/a
nla
n/a
Relative Accuracy Limit:
ZO%RM ot !Oo/.EL
Average 188.7435 181.8 -5.8
Parameter: Nox(lb/hrf
Run #
1
2
3
4
5
5
7
8
9
10
11
t2
13
L4
15
[oad
437
436
436
435
436
436
434
434
435
RM
803.8
811.1
828.5
831.0
828.4
826.6
831.3
827.5
823.8
CEM
808.7
815.1
827.3
830.0
822.3
824.O
820.4
846.9
848.6
Start Time End Tlme
L4:42 15:19
15:32 t5:52
16;05 16:25
76:37 L6:57
77:lO L7:3O
17t44 18:04
78:L7 18:37
19:01 79:2!
19:33 19:53
Difference Used?
-4.9 x
-5.0 x
1.3 x
1.0 x
6.1 x
2.6 x
10.9 x
-19.4 x
-24.4 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS6: Mass Emissions
9
2.306
71,7
9.0
1.5%
nla
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 435 423.6 427.1 -3.6
GP043AS-036878-RT- 1 579 Page 38 of 290
Job Code PROJ-036878
PacifiCorp, Huntin$on Unit 2
Test Date: 4lt!24
Paramoter:CO (ppmvwl
Run f
t
2
3
4
5
6
7
8
9
10
11
L2
13
t4
15
toad
437
436
436
435
436
436
434
434
43s
RM
101.9
51.3
88.2
77,0
55.1
84.0
732.3
212.6
255.5
CEM
111.9
62.4
90.1
79.6
69.3
87.8
L24.9
221.3
267.3
Start Time End Time
74:42 15:19
15:32 15:52
15:05 76:25
16:37 L6:57
L7:!O L7:30
L7:44 18:04
L8:17 18:37
19:01 79:21
19:33 19:53
Difference Used?
-10.0 x
-1.1 x
-1.9 x
-2.6 x
-4.2 x
-3.8 x
7.4 x
-8.7 x
-11.8 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P50, PS4A: CO ppm <2fl)
Relative Accuracy Limit:
10% RM or 5%EL or I d | +CC<Sppm
9
2.306
5.7
4.4
7.1%
nla
n/a
nla
Average 435 119.8 123,8 -4.1
Parameter:Co (lb/mmBtul
Run #
1
2
3
4
5
6
7
8
9
10
11
12
13
t4
15
Load
437
436
435
435
435
435
434
434
435
RM
0.121
0.073
0.105
0.092
0.078
0.100
0.158
0.252
0.318
CEM
0.128
o.072
0.104
0.092
0.080
0.101
0.t44
0.252
0.322
Start Time End Time
!4:42 15:19
15:32 15:52
16:05 L6:25
!6:37 76:57
!7:LO L7:3O
17:44 18:04
78:77 \8:37
19:01 t9:27
19:33 19:53
Difference Used?
-0.007 x
0.001 x
0.001 x
0.000 x
-0.002 x
-0.001 x
0.014 x
0.000 x
-0.004 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6Q PS5: Mass Emissions
9
2.305
0.006
0.004
3.204
nla
nla
n/a
Relative Accuracy Limit:
ZOo/.RM or LO%EL
Average 435 0.145 0.145 0.000
Parameter:co (lb/hr)
Run f
1
2
3
4
5
6
7
8
9
10
11
L2
13
74
15
Load
437
435
436
435
435
436
434
434
435
RM
515.5
304.1
44t.7
385.8
326.0
423.7
568.2
106s.1
1289.3
CEM
565.2
371.7
451.4
398.7
345.9
440.9
620.7
1L37.7
1390.9
Start Time End Tlme
!4t42 15:19
15:32 15:52
15:05 16:25
76:37 16:57
77:70 l7:3O
L7:M 18:04
78:L7 !8:37
19:01 79:21
19:33 19:53
Oifference Used?
-49.7 x
-7.6 x
-9.7 x
-11.9 x
-19.9 x
-L7.7 x
47.5 x
-72.6 x
-101.6 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS6: Mass Emissions
9
2.305
43.0
33.0
t0.o%
nla
nla
n/a
Relative Accuracy Limit:
20%RM or LO%EL
Average
GP043AS-036878-RT- 1 579
43s 602.3 629.2
Page 39 of 290
| 1l
Appendix A.3
Field Data
tt
/ ,r l .- a a a .a - .
GP043AS-036878-RT-1579 Page 40 of 290
a rl
Appendix A.3.1
Unit 1
/ . L L .- I t - .
GP043AS-036878-RT-1579 Page 41 of 290
Appendix A.3.1.1
Low-Load Flow Data
Client PacifiCorp
Unit lD Huntington 1
Load Low
EPAMethod3&4Data
lnputs
Barometric Pressure ("H8)
Stack Static Pressure ("H2O)
oz (%vd)
CO2 (%vd)
Vr. Volume of Water Condensed (mL)
Vm Volume of Stack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
Tm Temperature at Gas Meter ("F)
Calculations
Pm Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ("R)
Vwc(std) Volume of Water Condensed (sc{}
Vm(sta) Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B*,.t Saturated Moisture Content (%/100)
Bs Measured Moisture Content (%/100)
Bs Stack Gas Moisture Content (%/100)
23.80 23.80 23.80
-3.40 -3.40 -3.40
7.5 7.5 7.5
11 11 11
23.80 23.80 23.80
-3.40 -3.40 -3.40
7.5 7.5 7.5
11 11 LL
23.80 23.80 23.80
-3.40 -3.40 -3.40
7.5 7.5 7.5
11 11 11
23,93 23.93 23.93
523 523 523
4.OL 4.01 4.01
37.43 37.43 37.43
43.0 42.9 42.9
0.108 0.108 0.108
0.097 0.097 0.097
0.097 0.097 0.097
85.6 8s.6 85.5 85.2 85.2 85.2 85.2 85.2 85.2
47.8598 47.8598 47.8598 46.982 45.982 46.982 46.982 46.982 46.982
0.987 0.987 0.9A7 0.987 0.987 0.987 0.987 0.987 0.987
1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8
57 57 57 53 63 53 63 63 53
23.93
577
4.03
38.57
42.8
0.108
0.095
0.095
23.93
577
4.03
38.s7
42.9
0.108
0.09s
0.095
23.93 23.93
5t7 523
4.03 4.01
38.57 37.43
42.6 42.6
0.106 0.105
0.09s 0.097
0.095 0.097
23.93 2?.91
523 523
4.01 4.01
37.43 37.43
42.8 42.9
0.108 0.108
0.097 0.097
0.097 0.097
GP043AS-036878-RT-1 579 Page 43 of 290
Low Load Run fl
Location: Huilintton I
Load (MW): 1!r0
Dat6: 4ll0l2024
St nTim€: 5!25
Endllm.: 6:43
Probe / Gas Data
Adjusted Results
Va(avgl: 21.57 ttls*
Qsw: 35,321,552 mcf/hr
Qsd:
PEbG *1 Re: 0 detrs
Prcbe *2 R^rc: 0 detrees
PBbe*1Rs@: .OJ deS.eei
Probe #2 Rs@: -l.8 dctrc6
8.,: 0.0945 %/100
Md: 30.05 lbllb.mole
M,r 2E.92 lbllb-mole
Pe: 23.EO in Hg
P.: .3./O ln HrOP.:_!1:1ln Hr
96COr: 11O X
%Oi 75
%COr 0.0 %*
Flow RATA Traverse Data
Polnt lD Probe lO Sta.kTemp
(F)
Comct.d
YawAngle YawAntle Pl-Pz
(des) Q"(des) (ln H,ol c-
Unadlurted R.placrm.nt Point Uscd #WAF
Axlal Veloclty Axlal VelGlty for polnts
V-|ft/s€cl V-lft/secl wAF? u.ed
001 I 110 -3 -2.9 o1 0.809 21-890 nla
002 109 4 -3.9 0.15 o-80q0 24.427 nla
m3 110 -5 -s.9 o.77 0.8090 25.949 nla
004 L 111 0.77 0.8090 25.O77 n/a
005 t08 -5 -4.9 0.11 o.m90 20.477
m6 1 111 -3 0.1s 0.8090 24.495 nla
007 1 111 -4 0.18 0.8090 26.805 nla
008 t11 -3 -2.9 0.17 0.8090 26.O77
009 2 108 -3 o 10 0.8380 20.68S nla nla
010 2 10q 4 2.2 0.12 0.8380 22.667
109 -4 -2.2 0.13 0.8380 23.593
o72 2 109 -3 0.15 0.8380 25.3s6 nla nla
013 7 to7 3 0.10 0.a380 20.666
o14 2 L07 4 5.8 6_12 0.8380 22.524
015 2 108 4 5.8 0.14 0.8380 24.354
016 108 3 -t.2 o.l4 0.8380 24.474
tveraSes 10!r.1 -2.7 -1-' 0.14 0.8235 2!.fi1 nla nlz
G P04 3AS -0368 78 - RT- 1 5 79 Page 44 of 290
Low Load Run #2
Locltion: Huntiruton 1
L@d (Mwlr 189
Date: 4l1Ol2O24
StanTimc: 6:45
EndTimt: 6:59
Probe / Gas Data
Probe f1 Re: 0 deSrees
Probe f2 R&o: 0 defees
Probe fl i5@: {.l det?eel
Prob€ f2 qro: -1.8 degres
Br.r 0.0946 %/100
Mdr it0.06 lb/ltsmol.
M,: 28.92 lb/lEmole
Pb.r 23.9) in Hg
P.: -3.40 in H2O
P.: 23.55 in H8
%COr: U.0 %
wi-!!%
%CO: 0.0 %
81-5 %
Flow RATA Traverse Data
Polnt lD Probe lD
Corractcd
StlckTemp YawAngle Y.wAntle Pl-Pz
tFl lddl O.ldml lln H.ol
Unldlust.d Raplaccmant Polnt Uscd * WAF
Axlsl velcity kial Velcity for Polnts
v- lftl*l v- lftlarl wAF? u3.dc_
001 1 109 -3 2.9 0.12 0.809 27.477
002 1 110 -4 -3.9 0.13 0.8090 22.760
oo3 110 -3 -2.9 o15 o 80{25.276
004 1 111 1.9 0.16 0.8090 25.3t7
005 I 109 4 -3.9 o-12 0.8090 21.848
offi -3 o 1a 0.8090 ?3 66S
007 1 111 -3 2.9 0.16 0.8090 25.294 nla nla
008 1 111 -3 2.9 0.16 0.8090 75.294
ooq 108 -1 0.8 0.11 0.8380 21.697
010 2 108 ,1 0.8 0.11 0.8380 47.697
011 2 109 1 0.8 0.1s 0.8340 25.359
07)l09 0-8 0.14 0.8380 24.499
013 2 t07 .3 t.2 0.11 0.8380 27.675
014 z 108 -2 4.2 0.11 0.8380 21.699
015 2 108 0-8 o.l4 0.8380 24.471
o16 lm -o?o 14 0.8380 24.SOL
rverages 109.3 -2,? -1.4 0.14 0.8235 23.5s9 nla nla
GP043AS-036878-RT-1579 Page 45 of 290
Low Load Run #3
Lootion: Huntington 1
Load(Mlry): lX
Drte: 4llol2o24
StanTime: ?:01
EndTime: 7113
Probe / Gas Data
Probc *1 Reo: 0 degreeg
Prob€ #2 Re: 0 detrer
Probe *1 &@: .{rl deSret
Probe f2 &Lo: -t€ de8res
B*.: 0.0945 %/100
Md: 30.06 lbllb-mol.
M,: 26.92 lbllEmolc
Ph,: 23.80 In Ht
Pt: '3'40 ln H2O
P.: 23.55 ln Hg
%COrr 11.0 96
'kozt 7,5'A
%COt O.O %
81.5 %
Flow RATA Traverse Data
Polnt lD Probe lD
Coract€d
St.ckTemp YawAryle YrwAntle Pl-P2
(R (des) q (desl (in H,0)
Unadlustad Rephc€oent Pointusrd *wAF
Arlal Veloctty Axill Veloclty for Polnts
v. Ittl*c) v. (fvscl wAF? U*dq
ool 109 {-3.9 o.72 0.809 21.848
002 109 -3 -2.9 0.1s 0.8090 24.452
003 110 4 3.9 0.17 0.8090 26.O27
OM 110 1.9 0.16 0.8090 25.295
005 109 4 -3.9 0_1 0.8090 20.918
110 4 9 0.14 0.8090 23.6\9
oo7 110 4 -3.9 o.t7 o.aom 26.027
008 110 -3 -29 o.1s 0.8090 24.474
009 107 -0.2 0.09 0.8380 19 610
010 108 5 -3.1 o.12 o a3ao 22.624
011 108 -o)0.1s 0.8380 25.339
o12 108 2 -0.2 0.15 0.8380 25.339
013 t07 -2 4.)o.10 0.8380 20.671
014 104 -4 2.2 0.12 0.8380 22.641
108 4 -2.2 0.14 0.83ao 24.462
016 108 2 -o)01q 0.8380 25.339
lverates 10E.7 -3,2 -2,2 0.14 0.82t5 23.668 nl, nl^
G P043AS-036878-RT- 1 579 Page 46 of 290
Low Load Run #4
Lcation! Huntlngton 1
Load (Mw): 189
Date: q1Ol2O24
Startlime: 7,22
EndTime: 731
Probe / Gas Data
Prob! r,1 RM: 0 delrees
Probc f2 Re: 0 degres
Prob€ flt Rio: .Ol degres
Probe*2&ro: -1.8 degr.€s
Bs: 0.0968 %/100
Md: :10.06 lb/ltsmolc
M": 28.89 lb/lEmol€
Ph,: 23.9) in Hg
P.: -3./O in H2O
P.: 23.55 ln Hg
,4,CO2, M.O %
Y.O2t_1!%
%CO: 0.0 %
81.5 %
Flow RATA Traverse Data
Polnt lD Probe lO
Corrccted
StrclTtmp YawArule YawAndo P7-P2
lFl ld.rl o.-rd.rl lln H-ol
Unadruitcd Replement Polnt Usd # wAF
tulal Vclctty Axi.l Vel&ity for Points
v- Itt/ocl v- lftlecl wAF? us.dL
001 1 108 -3 2.9 0.11 0.809 20.931
oo2 1 110 4 -3.9 0.15 o_a0m 24.459 a/a nla
o03 t 10 -)o.15 o.4090 24.503
004 1 110 -3 2.9 0.16 0.8090 25.288
005 I 106 4 -3.9 0.12 0.8090 21.839
om 110 -3 o_ 15 o.aom 24.445
007 I 110 -3 2.9 0.17 0.8090 26.066
008 1 110 -3 -2.9 0.15 0.8090 24.445
ooq rot 4 n)o 10 o 4380 20.643
010 2 108 -s 0.12 0.8380 22.639
011 2 108 -6 -4.2 0.14 0.8380 24.425
01)10a -3 o lq o a3m 25 1dS
013 2 t07 -5 0.12 0.8380 )? 619
014 2 108 4 -2.2 0.13 0.8380 23.583
o15 2 to7 -4 -2.2 o.13 0.8380 23.567
016 2 108 .3 1.2 0.14 0.8380 )4 n%
lverages 108.5 -3.8 -2,9 0.14 0.82t5 23.7tO nla nla
G P043AS-036878-RT- 1 579 Page 47 of 29O
Low Load Run #5
Locctionr Huntington I
tod (MW): 190
Datei 4lt0l2024
StanTlmc: 7:33
EndTimer 742
Probe / Gas Data
Protrc *1 Reo: 0 defecs
Prob€ #2 Reo: 0 degrees
Probe fl &@: .01 degrees
Prob€ n2 &ro: .1.8 de8rees
Bsr 0.0968 %/100
Md: 30.06 lb/lb-mole
M3: 28.t9 lb/lb-mote
Pbr: 23.E0 ir H8
P.: -3.i(, ln H2O
Pr: 23.55 in Ht
%CO, A.O %
/&",------J!%
Y"COt 0.0 %
Flow RATA Traverse Data
Polnt lo Probe lO
Co[ected
StEakTemp YawAngle YrwAnde P7-P2
(F) (des) q" (dcs) (in H,o)
Unadlustrd Replaccm€nt Polntusd #WAF
ArlalvelGity Axlalvelocity for points
v. (fvsc) v. (tVcc) wAF? us€dc,
001 I 110 o-L2 0.809 21.900
002 I 110 4 -3.9 0.16 0.8090 25.262
003 I .2.9 o_17 0.8090 26.066 nla
004 1 110 0.18 0.8090 26.841
005 108 .1.9 o.72 o aoqo 2r.877
006 I 111 "1 -o_9 o14 0.8090 23.703
007 1 1 -2.9 0.16 0.8090 25.310
008 111 -3 .2.9 0.16 0.80m 25.310
009 2 107 -s -1)0.1 0.8380 21.656 n/a nla
010 2 108 -5 -3.2 0.13 o.83a0 23.563
o11 2 108 5 4.7 0.14 0.8380 24.425
012 2 109 -s)0.15 0.8380 25 2A
013 2 107 -5 -3.2 0.12 0 a3a0 22.619
014 2 108 -6 4.2 0.13 0.8380 23.537
015 2 109 6 4)0.14 0.8380 24.4A7
016 2 109 6 0.15 o 8380 25.305
verates 109.1 4.2 -3.2 0.14 0.823s 24.193 nla nle
GP043AS-036878-RT- 1 579 Page 48 of 290
Low Load Run #5
Location: Huntington I
Load (MWlr 191
Date: 4l,,012024
StartTimr: 7t44
EndTime: 752
Probe / Gas Data
PEbc nl Re: 0 deSrees
Probc t2 Re: 0 dagrees
Pobe fl q@: .01 detrees
Probe #2 &Lo: -1,8 det.ees
BEr 0.0968 %/100
MttJlb/b-mot'
M,r 28.89 lb/lb-mol.
Ph,: 23.E0 ir Ht
Pt: .3.4{, in H2O
P,: 23.55 ln H8
"4CO2t
77,4 'rL
'ho2t 7 5 .t(
%COt 0.0 ,6
81.5 X
Flow RATA Traverse Data
Poif,t lO Prob€ lO Stlct Tmp
tFl
C0rect€d
YawArl8le YrwAndc PL-PZ
(d€rl (Llderl lin H"ol c
Umdruned Rephement Polnt Used *wAF
tuial Vel8ity Axial Veltrity for Points
v- lftlscl v- 1ft/scl wAF? used
001 1 10?-3 -29 0_809 21.442
oo)l lo 4 3.9 0.15 0.8090 24.459
003 110 '5 .4.9 0.17 0.8090 26.OM
004 111 4 -39 o.17 o ao$16 06)
00s 110 2.9 0.11 0.8090 20.968 ila
006 110 4 -3.9 0.15 0.8090 24.459
007 111 -5 4.9 0.15 o 4090 2S )AO
004 -5 4.9 o.r7 0.8090 26.O27
009 109 -3 L.2 0.11 0.8380 21.773
010 2 r08 -o.2 0.1 0.8380 22.674
011 I 109 -2 -o.2 0.14 0.&180 24.512 n/a
012 2 109 -5 -3.2 o.14 o-8380 24.41 4
013 2 107 -3 o.1 o a3ao 21.685
014 109 -3 L.2 0.11 0.8380 2t.123
015 2 108 .3 L.2 0.14 0.8380 14.4
016 2 108 4 -2.2 0.15 o a3ao )\ 712 n/a
,etag6 109.2 -3.5 -2,7 0.14 0.8235 23.855 nlz nla
GP043AS-036878-RT- 1 579 Page 49 of 290
Low Load Run f7
Locatlon: Hurtlngton 1
Load (MW): 190
oate: 4ltol2o24
StanTlmer 7:54
Ehd Time: 8:03
Probe / Gas Data
ProbG 81 Ra6: 0 deSrei
Prcb€ *2 R^m: 0 detEs
Probe il Ru: {rl detrce'
Prcbe *2 RsLo: -1.8 d€trels
fu,: 0.0968 %/100
Md: :10.06 lb/lb.mole
M,: 28.E9 lb/lb-molc
Ptu:-3lgllnHr
Pt: -3./O ln HrO
P,: 23.55 ln Hg
%CO2, ,l,0
%Ort Ls
COr 0.0 96
E1.5 %
Flow RATA Traverse Data
Polnt lO Pobe lD
corEdcd
StaclTcmp YawAnde YawAngle
(Fl (de8) o-(des)
PL.?2
(in H:0)
Unadlurtld Raplac.ment Point Used *WAF
Axial Veloclty Axlal Velo.lty for Points
V,llt/recl V.(ftlrecl WAF? Usedc-
00r 1m .3.9 0.11 0.809 20.927
002 110 -4 -3.9 0.14 0.8090 23.630
003 110 4 -39 0.16 0.8090 25.262
m4 111 .2.9 0.16 0.8090 25.310
005 109 4 -3.9 o.12 0.8090 21.858
006 -4 .3.9 0.15 0.8090 24.441
007 111 -4 ,3.9 0.16 0.8090 25.284 nla
008 2.9 0.16 0.8090 25.310
m9 108 -L.2 0.11 0.8380 21.70A ala n/a
010 108 4 .2.2 0.12 0.8380 22.657 n/a
011 108 -2.2 0.14 0.8380 24_473
012 109 0.8 0.14 0.8380 24.570
013 108 -4 -7.2 o,0.8380 21,693
014 108 -5 .3.2 0.L2 0.8380 22.639
015 109 -3 -1.2 0.14 o-a3m 24.507
016 109 -3 0.15 0.8380 25.367
,erages 109.3 -3.6 -2,6 0.14 0.8235 23.725 nle ala
GP043AS-035878-RT-1 579 Page 50 of 290
Low Load Run f8
Location: Huntington 1
Load (Mwl: 189
Date: 4lt0l2o24
Stanlimo: 8105
Endlimc: 8r1t
Probe / Gas Data
Probe g1 Re: 0 dcSaees
Prob! f2 R&o: 0 dcSr€es
Prob€flRao: .01 dct.€ei
Prob. #2 RsLo: .1.8 degrecs
8*: 0.0968 t6l100
Md: 30.(f lb/Emolr
M,: 2E.89 lb/lEmole
Pb,r 23.80 ln Hg
Pr: .3./O in H2O
P!: 23.55 ln H!
%CO2t l,O
"1wi-J%
%COt 0.0 %
81.5 %
Flow RATA Traverse Data
Point lD Prob. lD
Co[cctcd
StlclTcmp YrwAngle YawAryle Pl-Pz
(Fl (derl o. (derl (ln H,0)
Unadlustcd Rllirccmcnt Polnt Uscd f WAf
tuial Vclodty Alirl Veloclty for Pointi
V.lft/s*) V.(ft/secl WAF? Usedc-
001 108 2.9 0.10 0.809 19.957
oo2 10 -3 -2.9 o1q 0.8090 24.445
oo3 -4.9 0.15 0.8090 24.444
004 10 -2 1.9 0.16 0.8090 25.306
005 10 -3 -29 o1 0.8090 20.968
oo5 1.9 0.15 0.8090 24.524
007 .1 -0.9 0.15 0.8090 24.515
008 -3 2.9 0_15 o aos ,q 110
oo9 107 4 0.11 0.E380 2L.674
010 108 -r.2 0.13 0.8380 23.595
011 108 -4 -2.2 0.14 o.a3a0 74 473
012 108 -o2 o 15 0.8380 25.350
013 108 1.2 0.11 0.8380 2r.704
014 108 .3 1.2 0.13 0.8380 23.595
01s 109 4 2.2 o14 0.8380 24.494
109 0.15 0.8380 25.373
rveratGS 109,2 -2.9 -2.0 0.14 0.823s 23.717 nla nla
GP043AS-036878-RT- 1 579 Page 51 of 290
LowLoad Run#l
L@tioni Huntintton I
Load (MWlr 190
Datci 4ltnlm24
St.rt Tlme: 8:13
EndTlfrCi 8:20
Probe / Gas Data
Probe #1 Re: 0 defee!
Prob! *2 Reoi 0 detres
Prcberl Rs6: -01 degre.s
Prob€ *2 &Lo: -il dctre!
B*r 0.0968 %/100
Md: :10.06 lb/lb-molc
M,: 28.89 tbltEmotc
Pb,: 23.t0 in Hg
P.: -3./O inH2O
Pt: 23.55 in Ht
ct4co2t l,.O %
%olt_!2%
'/&Ot 0.0 96
: 81,5 %
Flow RATA Traverse Data
Point lD Probe lO
Corrcctad
St.ckTemp YawAnglc YawAntlc ?l-Pz
(F) (d€sl O-(de.l (ln H,ol
Unadluned R.pltccmcnt Pointusad #WAF
Axial Velcity Arial Velfilty lor Points
V.(ft/.cc) v-(ft/se.l wAF? Usedc.
001 10a 4 3.9 0.12 0.809 21.839
002 110 3 -2.9 0.15 o.80m 24.485
003 1 111 3 "2.9 016 0.8090 25.310
004 3 -2.9 0.16 0.8090 25 310 nla
005 109 2 1.9 o.12 0.8090 2t.897
006 1 111 -3 0.14 0.8090 21.675
007 772 3 -2.9 o.8090 24.52A
008 1 L71 -4 39 o 16 0.8090 25.2U
009 104 .7.2 0.11 0.8380 27.704
010 2 109 -4 -2.2 0.13 0.8380 23.603
011 2 108 -o2 0.15 0.8380 25.350
o12 10E 3 -L.2 0.14 0.8380 24.446
013 2 107 4 .).2 0_1 0.8380 2r.674
014 2 108 4 o.L2 0.8380 27.651
01s 108 3 -L.2 0.14 0.8380 24.446
016 2 101)3 t_2 o.1s 0.8380 25.367
lverages 109.3 -r,2 -2,2 0.14 0.82t5 23.853 nla nlz
GP043AS-036878-RT- 1 579 Page 52 of 290
Lor, L or)
lmdnrr
lmpl4rr
nr.r{ 13!
Ir{i.l Fhrl
1n 3.1 hsa.s
383.j 12q.+
312 .1 3 tt.Y
550.8 560.o
t67l ;+5L,L
/%.{s
G P043AS-036878-RT- 1 579 Page 53 of 290
04\M( )N I R'S h EPA Method 2F Datasheet
PrdettGode o<.*78 lo;rlor{sl:C,tlfttllb L-
dhnt A. .l.-i.ofr)lrrcm:Ufc Pnrgrr: l'lld:7-1.9o R.t
louc:rl.',Ai*.t"' \ilillcElulnl'lGol:-" 14 FrchGondldon
DrE h ro lQ ,mbGlDrAl,btment lt / 15{cqlil ll ct
tunl I loc<l hrtChr*l'll'Ol:>.cr{"L=.{Blrl f,\
$iltftilc:bzi DlooTln::L+i [rolxl
Irrrr- Polnt lPortf olntl
Str*T:np
ml
Yu'Alrtlc
trDrd
VrlodtylPl'H1Ol
rPr+21
PlEhaPrHrol
lPa.Psl Eqrmant$t-l ItO . tz
^)f,?I O.i -4 t5
.3 Itr:ol .\{
4 Iil ?3 ,t77 -t I b9..S a \\
?,L tr I -j ,t5
3 \r t -q . r8
Li tr I .tf
3, -(lo?.-3 lozr4-q .\L
9 toQ -4 .\j
Lt ro9 -3 r5
Ll-t lo'l ID
a
lr ID.J Ll ,lZ
3 log Ll ,t4
tt ln9 , Itl
Schemilc
DlameterlD)=
Pomt Dail. FlDrr gt ctwlll
1
l=
l=
2
3
4
5
6
t
N
Poil lD
A
B
c
D
Reviewed: FPM CPM_
Page 54 of 290G P043AS-036878-RT- 1 579
LdGCtCodc b3c-*78-opcrbr(rl:ArlAit I a Lm
:f,rnG ?...i{j". r F lerom:lrlch:srrt l-Hd:)".9o N.6
buru:U-^^l:-^+^- tl- |HcF!:srrel'HSl:-.? I NrohCodldqr i/
D.IG:Ll- l7T -^19 Prohr lD I Atrbrnrnt ll7 +t35 !Glxl l(,o
ilunl a.lgtChcckPH,OI:l-/Dlrl ?.s
ItaltTlma:e'$$oor[nc:Ls,l rhol*l
EPA iiethod 2F Datasheet
0/i\ MON
,1,
R9:\ b
Revlewed: FPM CPM
Lo* Lr^)
Ireurra Polnt lPortfohfl
St*tT:mp
PH
YrvAndr
lf DGd
VrlodUCPl']lrol
lP1.P2l
Ptidt aP ('Hrol
tFr+51 Eommcttli:
lol -3 o,a
)fiio .Ll o. t3
-3 ,l 6 -3 O 'L-ol tl I -a 6.' L2-l to1 rQ o,t)
-:ll -?otl
-3 lt,-?o.t L
-c1 nl -3 o.tL
3- r tod o.n
-.t tox .l oll
-3 lo nl o.l s
-tl ,oq b.r Ll
Ll- I loz -J o. l,.J to{-a O.rt
-3 l0 <4 o. rY
^Lt loq -:o. lq
Schematc
DiameterlDl=
Pohrt tlrl. Ftqtr std(u,ll
1
fi=
B=
2
3
4
5
6
t
N
Porr lD
A
B
c
D
GP043AS-036878-RT- 1 579 Page 55 of 290
64\ f')t)N I R1;,\ L EPA Method 2F Dahsheet
,tCcclGodc ).3C e 7S orrnts{rh 4r./ Aet (t f-
dlcttc ?^"il:"o r o llrurn:lrlc Pr:lctrru l'!El:f.3. /o lo.
lourcr:ll.,-+1..-l--- tl-l ttrdc Pr:rnrn l'll'Ol:-3.9 PrabGcddhhn
EE:Ll- lD-).1 PrcbetD/Alhnm:ft It7 + g5 !qlrt li o
Rml 3 lrekCh:dl'll'Ol:Llxl a.g
ilrilfhr.:2oO tbpftrte:7rz ilrolrl
L r* l,^J
Ireurne Polnt lPort-Polntl
StrtkTamp
rtl
YewAl[h
lrDd
VclsdtyAPfHrOl
lPr+21
Pldr!Pl'HrOl
lR+Psl Commgntr:
I lo.l -Ll 6.t7
-)l6 .l -3 o ls
-7 llo -Ll Ot7
-Lt ,o -.t o. tc
2-l I ort -Ll 0. tl
-f Ito -rJ 0. trl
-3 ll o -L,o.t7
-1 llo -1 o.rs
J.,I o'z -2 o.o q
-f,lnll O.t 1-J ,o (-e O.tt
-Ll toY "1 Drf
Ll- I to)-f 0.to
--t lo( -q o.t I-t tog -Ll O. t Ll
-1 toK -t o. t 9
Schem.0c
Diameter (D)=
Polntt olri. Frorn S:iedcWatl
1
[=
l=
2
3
4
5
6
I
N
Po.t lO
A
B
c
D
I Reviewed: FPM CPM_
Page 56 of 290GP043AS-036878-RT-1579
ProlcstCodc osbe?t lnnur{sl:ALlts lLL llm
dlcnt { .,olfic. ro brunrtrt Ptrrgrr l'lld:a?. Vrs R.
Sqlrc!:U.l-lia^+.,r.-U- |ffiPnsurrl'll'Ol:-J. q ProbrGqdltbn \/
DeE:Ll - to--;q ProhclD/AlLnmu&tt7 t l3s !Bl$ll, o
iunl Ll Lrrf Chrcll-H'Ol:DITI
ttrrtThnr:7ta SlooTlmc:7st [rolxl
EPA Method 2F Datasheet
6(\ MgN I R,91................h
I
Reviewed: FPM_CPYO'_
!
L*u L, - J
Ireuu:a Polnt tPoil+olntl
Strdrlomp
l'Fl
YrwAndc
ItD.d
VclodtVaPl'Hrol
lP''f2l
Pltdr!P('t{rol
lg.Jsl Comrncntrl
-l to(-j o.tI
-)lo -q o .15
-3 to -l a, tr
-tf r0 -3 o.tc
a.-to(-q o.t I
-2 llo -3 o., y
-j tfo -l D.t-)
\q Ito -?o. t s
3-l lov '(D.to
-t,to(-(a.la
-3 to cl -6 o .t\
-9 lt c/-3 a. rs
vl- |t07 -5 o.le-f to{-.{o t3 v
-J loz - tf o. r ]
-tq lo4 -3 6.,q
Schema0c Polrtt Osl. From SLcf wal
1
Stadt Diameter 1D1=2
3
4
5
6
ft=
l=
i
N
Por{ lO
A
B
c
D
GP043AS-036878-RT- 1579
EPA illethod 2F Datasheet
Prchct@dc p o$eAg Orcrrrorblr fiLltnt t-z f.-
dlmt ?...(i.o..>lrrunrttFruqn l'tld;az. tO fr.
lourtl:tJ.^l;..t--l)- |fficFlrrulll.ll'Ol:-3.1 ,!obcGondldo.t
Detr:'.f - td'-a1 PrubclD/AlLnmrrrt lt7 *tJs Btrl
Nunl s-hek Chrdt I'll"Ol:LHI a.s
ItrrlTtuc:73i llorpTtna:7'lf {rolIl
Lo- Lo^J
Ireurna Poffi tPort Pohfl
SbckTcmp
frt
Yrwltth
It Drrl
vdodtyAPfHrol
lPl+21
PldrAP('Hrol
tPa+sl Canrmrntr;
llo -3 D .,1
-f,.lto -Ll o.lL
-3 la ^3 o. t7
-q lro rl o. r1
2.-l lo q -1 o.t1
-)Iil o.lLl
-3 It -3 O.lr.
-tl -3 o .16
3-l g')-L o.ll
-:.to(-5 O. r3
-3 lo cl -C o. tLl
_Ll t0 cl h td
Ll-|tol -g o.t)
-)t6V -(o.,3
-J lo7 -L o.t r I-rl lo1 -6 o. rt
Schemetlc
DiamcterlDl=
Polntl Ust. Fron Si.d( W![
I
fi=
l=
2
3
4
5
5
Port lO
A
B
c
D
Reviewed: FPM CPM_
Page 58 of 290G P043AS-036878-RT- 1 579
PrrolcctGode bg-g?t hcrbr(sl:ALI AB II E.f,^*
ftnt 9-.'. {.r-or.e lrluncnrlc Pn!'|rrc l'ltrl:43. ,c)L-
5olrr!LI"-11."**^'U-l Itrdc Prsara l'll0l:-3.q PrdtcGodltlott \/
D.ta:rt-tD-.f,et Prcb!lDrAltsnmcnt il7 + )35 ulrl \t
Mnt C-tarkdtcrkl']LOlr Dlral 4.1
lllrtTlmt:T rltl Itoltnc:?sa rLo[r.l
EPA Method 2F Datasheet
64\ M1JN I Rg,st
Revlewed: FPM CPM_
Page 59 of 290
Lo,,,r L.,^l
heYorsa Polnt tPortfohl
StedrTcmp
Itl
Yewldc
lrDGd
VdodtIOP l'HrOl
tPl+21
PhdtaPfHrol
lDa"PSl 0smmontr:
lo7 -?o.t)
-]llo -q o.,.s
-3 I lO -5 6.12
-j l,-q o t)
a-l to a']o.-J to -Ll o.t5
-J -5 0.t 6
-cl ltt -5 o. 17
3-,o 'l -5 a.ll
-.1 lo6 o. t3
-5 toq J fi .1.-l
-rl lo7 -t o. t\
I-l lo7 -3 o.n
.J lo rl -3 o. n
-3 lo6 .3 O ltl
-tl to(-q o.t5
Schsmetc
DiamcGrlDl=
Poht, g3.f!e@r$!f-l!6[
1
fi=
t=
2
3
4
5
5
I
N
Poil lO
A
B
c
D
GP043AS-036878-RT- 1 579
EPA Method 2F Datasheet
rrdrctGodc b<cq.+P,Onrnb(rl;AY lns h-z [r-
trhnc ?^.'L:.^- ^lryomstslcP!:rqrrul'lEl:7?.1tct f,o^
louru:il.,-fl...t-t).I SrdcPrclgrrr l'l{'Ol:- 3..1 hob!Cortdldor
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Itrilfinc:T S'I tuoThnc:f,o3 lrlolxl
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lrausncPdntlPort+oltttl
StectTcmp
|"H
Yrrfih
lrDGd
VrlodtylPfHrol
tPl-Pzl
PhdraPl'llpl
lPa+51
l-l loq - (.f a.t I
llo -3{o.t\
llo -Ll 0.tb
_cl lil -j Dtc
r.- I loQ -L1 o.t1
-f,.ll -cl 0.tr-3 ,r,_.1 o.l b
-1 I -3 o.tL
3-t tov -3 o.ll
-2 lo/-q o. la-3 lo4 -.{o.tLl
-",,on -t o. I q
q-lor -1 0. t I
-2 t6g -5:o.l2'3 lD't a?o. I L.l t
-11 loq -3 c, ts
SchemeUc
Diameler(D)=
Foht, oist. From StadrWell
1
l=
l=
2
3
4
5
6
Pod lO
A
B
c
D
Rev{ewed: FPM CPM_
Page 60 of 290GP043AS-036878-RT-1579
EPA Method 2F Datasheet
rrokctGoda Op:rrtoilrl:,dtxlLl/.i*
clllnt I u, il lt^r e trrorncrrlc Prrunrn l' Hd:7Z 8c:,Ro-
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fn
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VclocltyAP l'HrOl
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lp{.Psl Eommcnts:
lo !-?o t6
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2-l lo -3 o.ll
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l,l-I loX -3 a.tl-t toy -J o.t3
-3 lol -a{o.l .l
lo,t -a O. tr
Schoma0c
Diameter 1D1=
e$et urt. From Strd(wll
1
f,=
l=
2
3
4
5
6
t
N
Poil lD
A
B
c
D
Revlewed: FPM CPM_
Page 61 of 290G P043AS-036878-RT- 1 579
IrdGCtGodr b3G&+g Oprniertl:*L lA9lc r lo
clhft frc.i(icor a luomctlcPttrnrn I'll!l:r3.tro L.
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lun I 4 lcrlChcrlI'H,Olr Ll$t,J
ilrnTlm::9(13 ilooftnc:tAo fiolr3l
Lor.t L. .ol
EPA Method 2F Datasheet
04\ Yllf l,R9)b
Reviewed: FPM CPM-
Page 62 of 290
lrrurrc Po&rt lM-Polntl
SnctTcmp
frt
Yrw'Anfh
lrDGd
lhlodtyOPl'Hr0l
lPr-P2l
PlrdraPl'Hpl
lEaJsl Eommcntr:
^l ,o{-q o.12
-.)no -3 D.t(
^5 lr -?o.tL
^tl tl -?o.lL
a- I lo4 -3 a. la
-f llt -3 o.l,l
-3 IA -3 o.t {
-q il -rl o.r6
3-l tor -3 o.t I
-)ro1 _ql o. t3
-3 t t-t S/o. rs
-.1 lo{-3 (,.,el
lo7 -&r o. tl
lo(-al o. la\3 lo(--3 o. t&l
-Y lo^7 -)o.t5 I
Schcmatc
Diamater 1D1=
Polnl I Ud. Flont St d( tlr.ll
I
A--
l=
2
3
4
5
5
Poil lO
A
B
c
D
G P043AS-036878-RT- 1 579
Appendix A.3. L.2
High-Load Flow Data
GP043AS-036878- RT- 1 579 Page 63 of 290
Client PacifiCorp
Unit lD Huntin6on 1
Load HIgh
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H20)
oz (%vd)
CO2 (%vd)
Vr. Volume of Water Condensed (mL)
V. Volume of Stack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
T. Temperature at Gas Meter ("F)
Calculations
Pm Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ('R)
V,.Gta) Volume of Water Condensed (scf)
Vm(*dl Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B*,,", Saturated Moisture Content (70/100)
B*. Measured Moisture Content (%/100)
B*, Stack Gas Moisture Content (%/100)
23.51 23.6L 23.61
-4.40 -4.40 -4.40
7.5 7.s 7.5
L2 L2 L2
23.61
-4.40
7.5
L2
87.5 87 .5 134.s
49.577 49.577 48.83
0.997 0,997 0.997
t.7 L.7 L.7
84 A4 87
23,74 23.74 23.74
5M SM 547
4.r2 4,72 6.33
38.04 38.04 37.26
50.8 50.5 s0_5
0.762 0.160 0.161
0.098 0.098 0.145
0.098 0.098 0.145
23.61
-4.40
7.5
L2
23.6L 23.61 23.6L
-4.40 -4.40 -4.40
7.5 7.5 7.s
72 t2 L2
134.s 159.5 159.5 159.5
48.83 77.286 77.286 77.286
0.997 0.997 0.997 0.997
L.7 L.7 1.7 t.7
87 87 87 87
23.74 23.74 23.74 23.74
547 s47 s47 547
5.33 7.98 7 .98 7.98
37.26 58.98 58.98 58.98
50.1 49.8 50.0 49.9
0.158 0.155 0.155 0.155
0.14s 0.119 0.119 0.119
0.145 0.119 0.119 0.119
23.6L
-4.40
7.5
L2
104.5 104.5
49,472 49.472
0.997 0.997
7.7 r.7
78 78
23.74 23.74
s38 538
4.92 4.92
38.38 38.38
51.6 50.5
0.159 0.161
0.114 0.114
0.114 0.t14
GP043AS-036878-RT- 1 579 Page 64 of 290
P@b€ rf1 Re: 0 dctroes
P@bef2R^mr 0 degrces
PrcbetlRs@: {J degrce5
Pbbe *:I RsLo: -1.8 dctrees
8.,: 0.1135 l{100
M.: 30.22 lb/b-mole
M.: 28.83 lblltmole
Ph,r 23.51 ln Hg
P.: {.4O ln HrO
P,: 23.29 in Ht
COrt ,2O%
%Ozt 73 %
%CO: 0.0 %
x
High toad Run #1
Locatloni HuntinSton 1
Load (MW)r tA9
D.tei 4lr0l2024
StanTlmr: 14:46
EndTlme: L3122
Probe / Gas Data
Unadiusted Results
fVsec
Qtw: 80,773,467 w*,/ht
Flow RATA Traverse Data
Point lD Prcbr lD
corrccted
StaclTemp YawArde YawAnde Pl.?z
lB ld.rt o fd.d tln H.ol
Unadrustcd R.placcm.nt Point Uscd iWAF
Axlalveloclw Axldveloclty fo, Pointt
v-|ft/r..I v-llt/s.cl WAF? usda
001 2 130 .L 0.8 0.60 0.838 52.015 ala nla
m2 123 .7 4.2 0.73 o-8380 57-038
003 2 131 5.8 0.81 0.83E0 50 lC?
004 2 127 -1 0.8 o.74 0.8r80 57.618
005 1)S oa 0.59 o a3ao s1.361
006 2 123 .1 0.8 0.71 0.8380 56.246 nla
m7 2 123 1 0.8 0.80 0.8380 s9.704 nla nla
008 2 124 6 7g 0.80 0.8380 5S.208
009 2 124 .t -o.2 0,56 o.8380 50.000 nla
010 7 124 .4 -2.7 o.70 0.8380 55.860 nla
011 L24 o7t o a3ao s7.4U
012 2 t24 -1 0.8 o.74 0.8380 57.47L
013 2 t24 -4 2.2 0.60 0.8380 5t.717
014 t24 -4 -2.2 o.70 0.8380 s5.860
01s 1)4 .4 o7q o a?m 57_O4S
016 2 124 -1 0.8 0.74 0.8380 57.47L
lverareS 124.9 -1.3 0.5 0.71 0.8380 56.016 nla nla
G P043AS-036878-RT- 1 579 Page 65 of 290
High Load Run #2
Lcatlon: Huntin$on 1
Load (Mw)r /l89
D.tei 413012024
Stantlmci 15:38
EndTlme: 15:58
Probe / Gas Data
Probe #1 R@: 0 de3'g
Probe *2 Re: 0 det'es
Probe rl RM: .{rl degreB
Prcbe 62 Rs,o: -lJ detrc.s
8",: 0,r.136 %/10{t
Mdr 30.22 lb/b-mol€
Mi: 2E.E3 lbllb.mole
Pb.,: 23.61 in Hg
Pr: 14.40 in H2O
P.: 23.29 ln Hg
%Q,t_!!%
%Ort 75 %
%
Flow RATA Traverse Data
Polnt lD Prcb€ lO StackTemp
(r)
CorEcted
YawAnglc YawAnglc Pl-P2
(des) q"(dcs) 0n H,ol c-
Unadruncd R.placement Point Us€d * WAF
Axlal Vel*tty Axlal Veloclty for points
V-|ft/ecl V-lft/sGcl wAF? U.ed
001 2 tzt ot 0.55 0.838 49.S(M nla
oo7 123 -3.2 0.71 0-8380 56.164
003 724 -2 4.2 o.77 0.8380 56.694
004 2 123 -2 -0.2 o.76 0.8380 58_198
00s t23 -3 7.2 0.55 o.4380 49.498
006 722 -4 2.2 o70 0.8380 5S.765
007 2 174 2,a o.72 0.8380 s6.627 n/a
ooa 2 123 -2 -o.2 o.76 0.8380 58.198
009 2 12t 0 1.4 0.56 0.8380 49.447 nla
010 2 t)1 I 0.8 0.76 0.8380 58.193 n/a
011 2 t23 0 1.8 0.7s 0.8380 57.746
012 2 123 0.8 0.76 0.8380 s8-193 nla
013 123 -1 0.8 0.s6 o.83ao 49.952 nla
014 123 0.8 o76 0.8380 s8.193 nla nla
015 7 124 2 3.8 0.74 0.8380 s7.350 n/a
2 723 -L o.8 o.76 0.8380 58.193
ueraSes 123.0 -1,3 0.5 0.70 0.8380 ss.522 nla
GP043AS-036878-RT-1579 Page 66 of 290
High Load Run fr3
Locatlon: tluntirlton I
Load (Mw)r 490
Date: 4laol2o24
Start Tlm€r 16:14
EndTime: 16:34
Probe / Gas Data
Prcbe lf1 R@: 0 dcgeer
Prcbe f2 ne: 0 drSreet
Probef,l R.@: fi degrees
Prcb. *2 &@: -13 degr.es
&.: 0.097, x/100
Md: :11.22 lb/lb,mole
Mtr 29.03 lb/lb.molc
Pb..r 23.51 In Ht
P,i {.4O in H2O
P,: 23.29 ln Hi
'rCO|,
XrlJ%
%Oi 7S%
XCOi 0.0 X
&r.5 96
Flow RATA Traverse Data
Polnt lO Probe lO
Cor.d€d
Sia.kTcmp YawAngle YawAntle P1-P2
(Fl (des) Q.(d€sl (in H,ol
Uoadiustrd Replac.m.nt Point Us.d ,WAF
Axi.l Vclo.lty Axial Vclorlty for Polnts
V.(ft/eecl V.(ft/sec) wAF? usedc-
001 2 123 1 2.8 0.61 0.838 51.903 nla
@2 2 t23 I 2.4 o.7,0.8380 5S.996
003 124 o.a o76 0.8380 58.047 nla
004 2 L24 1 2.8 0.77 0.8380 58.364 n/a
005 2 L23 I 2.4 0.52 0.8380 s2.327
006 7 123 aa o71 0.8380 55.996
@7 2 L24 I 2,8 0.77 0.8380 58.364
008 2 L24 1 2.4 o.77 0.8380 58.364
ooq 721 2.8 0.55 0.8380 49.200 nla nla
010 2 123 1 2.4 o.72 0.8380 55.389
011 2 124 0 1-8 o.73 o.4380 s6.467
012 1)n o 1.8 0.75 0.8380 57.641
o13 1)a 0 1-8 0.55 0.8380 49.765
014 123 1 2.8 o.72 0.8380 56.389
015 2 124 o 1-A o7q 0.8380 56.867
o16 r24 0 1.8 0.75 0.8380 57.641 nla
lverals 123,4 0.6 2,4 0.70 0.8380 ss.632 nla nla
GP043AS-036878-RT- 1 579 Page 57 of 290
High Load Run rr4
Leatlon: Huntintton 1
Load (MW)r 491
Date: 4FO/2O24
Start Time: 15:50
End Tlmei lltLo
Probe / Gas Data
Prcbe lll R6: g {gg;Eg5
Probe L2 R^E: 0 dcgreei
Prcbe f1 Rs@: {rJ degees
Prcbe f2 RsLo: -lJ dctrees
a,; o,o977 %ltOO
Md: 30.22 lb/lb-mol€
Mt: 29.03 lbllb.mole
Pb./ 23.51 in Hg
Pt: {.40 ln H2O
P,: 23.29 ln Hg
c.Ai l2.O
%Oi f ,5
%COt 0.0 %
%
Flow RATA Traverse Data
Point lO Prcb€ lo
C.rrccted
StackTcmp YawAngle YawAnde Pl-P2
(F) lder) Q"(des) (ln H,0)
Unad.iusted Replacement Point Used SWAF
Axial Velochy Axial Veloclty for poirts
V. lftlsecl V- lfllse.l WAF? U..dc-
001 L23 1 7.A o57 0.838 so.t72
002 123 2.8 0.64 0.8380 53.164
oo3 72X 0 1.8 o.67 0.8380 s4.434
004 724 7.2 0.8380 s6.828
005 120 2.8 0.55 o.a3ao 49.157
m5 !23 2.4 o.64 0.8380 53.164
007 t24 3.8 o.73 0.8380 56.770 n/a nla
008 123 2.4 0.73 0.8380 s6.779 n/a
009 t22 7.4 0.60 0.8380 51.431
010 121 2.8 0.75 0.8380 7 5S1
011 123 O,E o.77 0.E380 58.378
o12 123 o_a o.71 0.8380 s6.0s7
013 111 2.8 0.61 0.8380 1.858 nla
ol4 123 2.8 o.74 0.8380 57.t61
015 124 o.8 0.75 0.8380 s7.6A
016 t1l 0.8 0.8380 56.057lverages 122,9 0.5 2.3 0.68 0.8380 54,7A9 nla nla
GP043AS-036878-RT-1579 Page 68 of 290
Prebe,l1 Rm: 0 degeei
Prcbe *2 Re: 0 degrees
Prcb€ #l Rs: {J d€&eet
PrcbcI2 Rs@: -lJ de$.Gs
B*!: 0.1452 %/100
Md: :D.22 lb/lbmole
M.: 28.45 lb/lb-mole
Ph.: 23.51 ln Hg
P.: {.4O in HrO
Pr: 23.29 ln tlg
%CO2, ILO%
%Ort 73 %
%CO: 0O %
%
High toad Run #5
Locatlon! Huilintlon 1
toad (Mw)! 49t
DatG: 4l3Ol2O24
Start Tlmer ,7t25
End Tlmei
Probe / Gas Data
Unadiusted Results
Va(avtl: 55.38 ft/sec
Qsw: 80,119,155 mcf/hr
Qsd:
Flow RATA Traverse Data
Point lD P@be lD
Corrccted
SteckTemp YawAnde YawAnde Pl-Pz
lrl (derl o- (d6rl lin H,ol
Unadidcd Replaccmcnt Point Uscd SWAF
Axial Velo.lty Axi.l Vel@ity for Points
V.{ft/secl v.lfvsec} wAF? usedc-
001 2 L22 0.8 0.55 0.838 49.797 ala
002 2 t23 o.8 o_59 o-a3ao 55.823
003 2 23 0.8 0.75 0.8380 58.200 ^la0042240.8 0.70 0.8380 s6.275 nla nla
m5 1?-1 o.8 o54 o a3ao 493U
006 2 23 0.8 0.59 0.8380 55.823 nla
007 ?24 0.8 o.14 o.8380 s7.860 ile nle
ma 24 0.8 0.71 0.8380 56.575
o0!)2 123 0.8 0.55 0-8380 49.839
^la0102127-2 4.2 0.69 0.8380 s5.781
011 23 0.8 0.76 0.8380 58.587
012 2 4.2 0.75 0.8380 58.205 nla nla
013 2 0.8 0.54 0.8380 49.142
o14 )?-o7 o10 o 83ao \6.21)
015 2 23 0.8 o.77 0.8380 s8.971
016 2 23 -0.2 0.78 0.8380 59.358
lvents 123.0 -1.3 0.5 0.68 0.8380 55.384 nla nla
GP043AS-036878-RT-1579 Page 59 of 290
High load Run #6
Locatlon: Huntlntton 1
Load (Mw): /|t6
Oate: 4l3Ol2O24
Stan Time: 17:58
EndTim.: 18t18
Probe / Gas Data
Probe Sl RA@: 0 degrecs
Prcbe*2RaN: 0 d€greei
Prcbe tl &D: -OJ d€greei
Pbb.fl2 Rsro: -l.g degrcB
B.!: 0.1432 %/1(x,
Md: 30.22 lb/b.mole
M"r 28.45 lb/lb.molc
Pb.,: 23.61 ln Ht
Pt: 4.40 ln HrO
P,: 2329 In Ht
COlt 12,0 %
%O1: 7,5 %
%COt 0,0 %
%N,r 80.5 %
Flow RATA Traverse Data
Poirt lO Pbb€ lD
Corccted
StackTemp YawAngle Y.wAngle
(r) (dBsl o-(des)
Pt-?2
(ln H,ol
Unadlustcd R€plaem.nt Polntuscd rWAF
Axlal Veloclty Axial Velcity fo. potnts
V,(ft/tec) V.(ft/secl WAF? Usedq
oo1 2 721 0.8 0.56 0.838 50.204
002 722 0.8 o.67 0.8380 54.961
003 2 123 0.8 0.73 0.8380 s7 479
004 !23 0.E o.7?0.8380 58.971 n/a
005 2 L22 0.8 0.55 0.8380 49.797 nla
006 2 121 0.8 0.67 0.8380 55.008
007 L?3 0.8 0.75 0.8380 58.200
008 2 t23 0.8 o.77 0.8380 s8.971 nla
009 2 L23 -1 0.E 0.57 0.8380 s0.737 nla
010 2 122 0 1-8 0.6q 0.8380 54.113
011 2 122 0.8 o.76 0.8380 58.536
012 2 27 4.2 o.71 0.8380 57.375 nla
o13 2 127 .1 0.8 os5 0.8380 49_754
014 2 122 o 1.8 0.6s o.8380 54.113
015 t22 -1 0.8 0.7s 0.8380 s8.1s0
016 z !22 -1 oa 074 0.8380rverages 122.3 .0.9 0.9 0.68 0.8380 55.254 nla nla
GP043AS-036878-RT- 1 579 Page 70 of 290
High Load Run #7
L@tlor: Huntington I
Led(Mwli 62
oate: 4l30l2o24
StartTlme: 18:33
EndTlmG: 18153
Probe / Gas Data
Prob. *1 Re: 0 detr4s
Prcbe *2 R^mr 0 degrcE
Prcb6 *1 Rs: {rJ degrees
Pbb. f2 Rs@: -1.8 dctrc6
Be:........:9:!g%/1oo
Mdr :l{r.22 lbllb,mole
M!: 2t.75 lb/lb-mole
Phi 23.51 ln Ht
P.: {.4O ln H.O
P.:________l431ln Hr
%COrt ILO%
%Ozt 73 %
96CO: 0.0 %
80.5 %
Flow RATA Traverse Data
Point lD Prcbe lO
comcled
stackT€mp YawAntle YawArde Pl-P2
lFl lded O.. Id.!l lin H"ol
Unadlurt.d Rcplaemcnt Pointusld fWAF
Axlal velclty Axial velelty for Points
v-lft/se.l v^lftl.ecl wAF? usedc
00r 119 -1 0.8 0.55 o.838 49.392
m2 2 t27 ,1 0.8 o.74 o.8380 s7.391 nla n/a
m3 122 0.77 o a?co 54.570
004 L22 -2 4.2 o.72 0.8380 56.664
00s t2t -,0.8 0.s6 0.8380 49.925
006 l2t oa o7s o Stao s7.777
007 722 -1 0.8 0.75 0.8380 57.427
o08 122 -2 -o.2 o.71 0.8380 56.269 nla nla
m 1)1 -1 o8 o.4380 48-S70 nlz
010 L27 -1 0.8 0.69 0.8380 55,418
011 721 -1 0.8 0.73 0.8380 57.100
o71 123 o 1-a o.77 o_a3m s8-620
013 122 o8 o54 o tiao 4q 6A
014 L21 -1 0.8 0.71 0.8380 56.215
o15 123 -1 0.8 o.7s o.8380 s7.477 n/a nla
015 t)1 o 18 o76 o 8?ao s8 238
lveraleS t2t.7 -o.9 0.9 0.59 0.8380 55.308 nla nla
GP043AS-036878-RT- 1 579 Page 71 of 290
High Load Run #8
l-o6tion: Huntintton I
Load (MW): 451
Date: 4l3Ol2O24
Starl Tlme: 19:09
EndTlme: 19129
Probe / Gas Data
Adjusted Results
ft/sec
qsw: 79,484,992 ws<ilht
PrcbG f1 R^6:
Prcbc *2 R^m:
Prcbe tl Rs@:
Prcbe f2 RsLo:
0 degrecr
0 deSreer
{rJ d€greei
-1.8 defe.s
8$: 0.1191 %/lqt
Md: 30.22 lb/lbmole
Mrr 28.76 lbllEmole
P!n: 23.61 ln Ht
Pt: {.40 ln H2O
Pt: 23.29 in Ht
aACOz, 72.O oti
%Or, 75 %
"4COt
0.0 96
&,.5 %
Flow RATATraverse Data
Polnt lD Prcbe lD Sta.kTemp
(F)
Corectrd
YawAngle YawArde P1-P2
(der) q"(des) (ln Hro)c"
Unadlustcd Replaccmcnt Point Used
Axialv€locity Axlalvelcity for
V.(ft/secl V.lftlsecl wAF?
* WAF
Points
Us.d
oo1 r22 .1 o.8 0-ss 0.838 49.520
002 2 722 0.8 0.70 o.8380 55.855
003 2 122 -1 0.8 0.73 o 4380 57.051 nla
OM 2 123 0 1.8 o_77 0.8380 s8.620
005 2 119 2.8 0.54 0.8380 48.888
006 2 122 1 ?.8 o.72 0.8380 56.597
m7 2 L22 1 2.4 o.7\0.8380 s1.764
008 2 t23 2.8 o.74 0,8380 57.427
^la0097t22-1 0.8 0.55 0.8380 49.520
o10 2 \22 -1 0.8 o.70 0.8380 ss.866
011 2 122 -1 0.8 0.76 0.8380 58.211 nla
otz 723 0 1.8 0.75 0.8380 s7.854 nla
013 2 72L 1 0.8380 s1.fs nla
014 2 127 2 3.8 0.73 0.8380 56.931
015 2 !22 1 2.4 o.75 0.8380 s7.764
016 2 l2t 2.8 0.74 0.8380 57.427 nlalverages 122.0 O.2 2.0 0.69 0.8380 55.406 nla nla
GP043AS-036878-RT- 1 579 Page 72 of 290
High Load Run #,
l-cation: Huilintton I
load (MWl: 47
Date: 4l1Ol2O24
StanTlm€: 19:il4
EndTim€: 20:(R
Probe / Gas Data
Adiusted Results
Va(avgl: 54.51 ttlsec
Qsw: 79,022,767 wc|/hr
dsct/h.
PEbe fl R@: 0 detr€ei
Prcbe*2Roo: 0 de$ees
Probe 11 Rs: {ll detf€ei
Prcbe f2 Rs@: -r-8 d€&ees
&r: 0.u91 %/100
Md: 30.22 lb/ltmole
M.r 2t.75 lb/lb-molG
Pt.,'_3191in Ht
P.: {,i10 in HrO
P.: 23.29 in Ht
'ACO2t l2,O %
%O,t 7S %
"4Lot
0.0 %
80.s 96
Flow RATA Traverse Data
Polnt lO Probe lO
Cormded
Sta.kTemp YawAnglc YawAngle P1.P2
lfl ld€.| o.ldeil lln H,ol
Unadlu.tcd Rcplac.mGnt Pointuscd *WAF
Axialveloclty Arialvelclty for Polnts
v- lftl*l v- llt/sec) wAF? lJsedc
001 727 -1 o.a o.s5 o 438 49 510
002 2 r22 I 0.8 0.69 0.8380 ss-456 nla
003 2 722 I 0.8 o.76 0.8380 58.211
oo4 121 1.8 o.77 o a?m 56 6aS
005 2 122 I 0.8 0.57 0.8380 50.412 nla
006 2 722 -1 0.8 0.68 0.8380 ss.062
oo7 l??0.8 0.75 0.8380 57.877 nla
008 2 L22 0 1.8 o.72 0.8380 56.636 nla
009 2 121 7.4 0.s4 o-a3ao 4A.972
o10 t21 0.8 0.69 0.8380 55.418 nla
011 2 721 2.4 0.77 o.8380 54.474 ila
o12 2 122 LA o.72 o a?m 55.597
013 2 720 I o.8 o57 o a3ao so 1?6
014 2 L21 t 0.8 0.71 0.8380 s5.216 nla nla
01s 2 122 1 2.4 0.75 o-8380 s7.764
016 12)3-8 0.74 0.8380 s7.320 nla nla
werag6 121.8 "0.2 1.5 0,58 0.8380 55.050 nla nla
GP043AS-036878-RT- 1579 Page 73 of 290
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04\Mt)N I RO.\h EPA Method 2F Datasheet
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EPA Method 2F Datasheet
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EPA Method 2F Datasheet
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EPA Method 2F Datasheet
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EPA llllethod 2F DatasheetI /efi Ml)N I R!))t"
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GP043AS-036878-RT- 1579
Appendix A.3.1.3
Instrumental Test Method Data
1i
G P043AS-036878-RT- 1 579 Page 85 of 290
PROJ-036878
Pe.lfiCorp
Huntln8ton Unlt I
413012024
Run# I
Start llme 14:46
StopTime 7si22
123
E9
19:09 l9itA
19:29 20:04
89
2
15:38
15:58
3
16:14
16:34
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40,773,467 80,318,179 a0,426,770 80,247,470 79,820,977
EPA Method 3A,5C,7E and 10 Data 7 2 3 4 S 5
CO,l%w)
SO, (ppmw)
NO, (ppmw)
No, (ppmw)
cO (ppmw)
M.ss Emhsion Calolatlons (Usln8 EPA Method l9l
10.4
30.2
115.2
0.4
62.9
I
10.4
24.6
Lt4.3
0.5
52.1
2
10.3
24.9
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0.6
43.3
3
10.4
29.7
106.9
0.5
68.4
4
70.7
32.2
107.5
0.6
191.1
5
10.5
34.4
105.0
0.5
108.2
6
9.9
30.0
177.7
0.6
4.1
7
9.9
31.5
11S.0
o.7
s.2
8
9.8
33.1
776.2
0.6
6.8
9
F. scf/mmBtu
SO, (lb/mmBtu)
No- (lb/mmBtu)
cO (lb/mmBtu)
sO, (lb/hr)
Nor (lb/h.)
co ilb/hd
1E00
0.087
0.238
0.o79
406.1
1111.3
369.3
70.6
30-3
405.0
0.085
119.5
o.243
60.3
353.0
o.o74
0.071
0.217
0.065
329.7
t 096.0
304..4
10.5
24.4
328.0
0.069
117.4
0.240
51.1
301.6
0.064
o.o72
0.235
0_055
332.5
1084.5
253.1
10.5
25.4
343.8
0.072
115.5
o.237
46_7
277.O
0.0s8
0.098
0.277
0.135
457.2
1013.3
629.8
0.091
0.256
0.00s
395.9
0.089
LzL.O
0.096
0.2s1
0.007
0.101
0.255
0.009
439.5
1107.2
39.4
0.085 0.090
0.220 0.216
0.086 0.234
391.8
1012.1
394.0
424.3
t028.4
1113.3
399.5 420.5
1126.8 1102.5
24.2 30.6
PlantCEMSDataT21456TA9
unit road (Mw) 489 4A9 490 491 49i 436 46, 46L 467
co2 (%vw)
SO, (ppmw)
So, {lblhr)
So2 (lblmmBtu)
Nor (ppmw)
No- (lb/hr)
No, (lb/mmstu)
co (ppmw)
co (lb/hr)
co (lb/mmBtu)
GP043AS-036878-RT-1579
L0.7 10.9 rO.7 10.0 10.1 10.1
29.8
0.117
t0t.9
0.131
0.098
119.3
t130.6
0.254
7.9
32.7 33.7 29.8 31.1 33.0
395.8 420.3 439,9
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109.0 111.1
4tt.2 434.2
0.092
118.1
1150.8 1138.0 7L27.6 1041.5 1046.5 1023.4 trSS_7 1127.5
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96.4 188.4 108.3
0.259 0.253
7.A 6.2
0.010 0.008 0.010
556.3 1080.1 620.1 45.5 35.8 45.8
0.227
Page 86 of 290
1PROr-{r35878
PacifiCorp
Huntin$on Unit 1
4lr0l2o24
rm CFR Part 75, Appendlx A
06.5.6 pollutent Stratificatlon Test
Port Point Time
Stack Diameter: 323.0"
Stratification Test Point 1: U.2" 14.4%l
Stratification Test Point 2: 47.2" (14,6%l
Stratification Test Point 3: 95.6 " 129.6%l
SO,Cor
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14:48 10.6 31,0
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14:50 10.7 30.3
14:51 tA.l 30.8
413O1202414:57 t0.l 30.8
14:58 lO.7 30.8
14:59 lO.7 30.8
15:00 10.5 29.9
15:01 10.6 30.2
15:02 10.5 30.1
4/3o/2a2a $:o7 x0.6 29.8
15:08 10.6 29.8
15:09 10.5 29.8
15:10 10.6 30.7
15:11 10.6 30,7
75:72 X0.8 31.5
413012024 ts.L1 10.s 29.s
15:18 10.5 29.5
15:19 10.5 29.6
15:20 10.5 29.4
15121 1O.5 28.5
15:22 10.6 29.3
Mean 10.6 30.3
Max Dwiation Frcm Mean 4.2 L.7
Max Devlation (X) 1.7% 5.8%
Shortllne? OK OK
Single Polnt? OK OK
GP043AS-036878-RT-1 579 Page 87 of 290
PROJ{368rt
P4lfrCorp
HuntinSton Unit 1
Ilinl\oa
Teat nun 11
StartTime
Run Length
StopTime
14i46
24
15122
PRO-0358r8
Pacmcorp
Hundntbn Untt I
4lr0l2t24
taat nun *2
StanTtme
Run Len8th
Stop Ime
Uncorrcded Analyzer oata
15:38
2t
15:S8
Uncorreded Analyzer oab
Mindc
1
2
3
4
5
6
7
8
9
10
77
72
13
14
15
17
18
19
20
21
22
2?
24
llme
14:46
L4i47
14:48
14r49
14:50
14:51
14i57
14:58
14:59
15:00
15:01
15:02
15:07
15:08
15:09
15:10
15i11
15r12
15:77
15r18
15:19
15:20
1Sr21
!5t22
cor 50: ilq co f,or
*w prlrw ppfrw ppmw ppmw
10.5 31.1 1L2,3 17.3 0.3
10.6 31.S 113.0 90,0 0.5
10.6 31.0 112.5 7A.2 0.3
10.6 30.8 Lt2.4 85,4 0.s
lo.7 30.3 111.9 78.8 0.2
to.7 30.8 112.9 99.0 0.3
70.7 30.8 x12.9 A7.4 0.S
10.7 30.8 Lt2.1 92.9 0.1
10.5 29.9 tL4.4 52.4 0.2
10.5 30.2 113.3 69.8 0.4
10.5 30.1 113.1 54.1 0.5
10.5 29.5 1t1.2 48.3 0.4
10.6 29.8 115.8 ,$.7 0.5
10.5 29.8 1t7.3 34.2 0.3
10.5 30.3 116.8 30.4 0.5
10.6 30.7 117.A 46.1 0.6
10.7 30.5 115.9 72.O 0.6
10.8 31.5 115.4 110.9 0.3
10.5 29.5 119.1 30.4 0.4
10.s 29.5 118.2 30.8 0.5
10.5 29.4 119.0 27.A 0.2
10.5 28.5 119.4 45,2 0.4
10.6 29.3 118.0 67.6 0.5
10.6 29.1 119.0 52.6 0.7
cor sor t{o, co toz
Tihe %w ppmw ppnw pnmw ppmw
15i38 10.6 27,1 115.0 72,3 0.3
15:39 10.6 26.3 114.9 55.5 0.5
15:40 10.S 25.O 114.5 45.9 0,4
15:41 10.5 26,4 11a.5 46.3 0.4
LS:42 70.7 26.6 113.2 52.0 0.5
15143 10.6 25.8 113.8 49.3 o.4
15:44 10.6 25.4 113.8 s3.1 0.5
15:45 10.6 25.3 113.3 58.6 0.4
15:46 10.5 24.9 113.8 41.4 0.5
15:47 10.5 2S.3 112.6 78.4 0.4
1s:48 10.S 24.5 114.s 58.7 0.s
15:49 10.5 24.0 114.9 35.8 0.5
15:50 10.5 23.9 115.4 29.8 O.7
1s:51 10.s 23.4 L14.4 4L,7 O.7
15:52 10.5 23.O 114.6 36.6 0,6
15:53 10.5 22.7 115.7 29.O 0.4
1S:s4 10.5 22,8 115.4 36,5 0.9
15:55 10.5 23.4 L14.2 52.4 O,7
15:55 L0.7 23.9 , 2.A az.s 0.6
15:s7 10.5 23,s 115.0 52.7 0.5
10
72
13
L4
15
16
L7
18
10.5 30.2 115.3 52.9 0.4
o.1 {,2 -0.3 0,7
0.1 4.2 0.0 -1.1
0,1 -o.2 {r.2 -0.2
9.1 26.8 170.3 145,7
9.1 26.9 170.1 144.5
9.1 25.9 1rO.7 1'!4,9
8.9 26.9 170.0 144.5ffi
21 15:58 10.6 23,1 114.4 62,0 0.4
ArcEg. 10.6 21.1 114.3 S1.5 0.5
0.1 4,2 0.0 -1.1
0.2 0.0 -o.2 -1.0
0.2 {.1 {.1 -1.1
9,1 26.9 170.1 L44.6
9,1 26.9 170.1 144.6
9,1 26.9 lro.l 1ild5
8.9 26.9 170.0 1i14.5@
19
20
Avanlr
g
c.
Corc&d Av6Ete:
q
c.
Codcd Awral!:
G P043AS-036878-RT- 1 579 Page 88 of 290
Pnor{358rt
P..ifiCorp
Hundntbn unlt ,
4130lzOU
T.st Run fl3
Stad Tlme
Run tenSth
Stop Time
PROr-036818
P.clficorp
Huntiutd Unlt I
ti3ol2oz4
T6t Run g
StartTlme 1550
Run tength 2L
StopTime 17:10
Un@rreded
16r14
2L
16:34
Dab
Mlnm
1
2
3
4
lim.
16:14
16:15
16:16
16:17
16:18
16:19
16:20
L6.2!
16i22
!6t23
16:24
16:25
16:26
16i27
16:28
16:29
16:30
15:31
L6.32
16:33
16:34
cor so, ilo, co xor
t{w ppm FpM ppmw pphw
10.4 23.7 114.7 28.4 0.6
10.4 23.8 114.2 26.1 0.5
10.4 24,r 113.8 31.2 0.5
10.4 23.9 115.4 25.2 0.7
10.4 23.1 114.s 2s.8 0.6
10.5 24.L LL3.2 43.3 0.7
10.4 24,6 t14.7 48.6 0.6
to.4 23.9 rL4.7 28.3 0.5
10.5 24,a 113.3 51.3 0.6
10.5 25.2 114.2 50.5 0.8
10.5 25.1 113.4 3s.4 0.7
10.5 25.3 113.3 39.4 0,5
10.5 25.5 112.6 30.9 0.5
10.5 2s.6 111.1 59.5 0.3
10.5 25.1 112.0 51.6 0.5
10.5 24.7 110.5 38.8 0.4
10.6 25,9 110.7 s8.1 0.S
10.6 25.4 111.6 40.4 0.5
10.6 25.5 t1t.2 59.5 0.3
10.s 25,2 Lr7.8 53.1 0.4
10.6 25.5 110.8 53.0 0.7
co" sor f,o, co tor
Tlma Xw ppfrw pp|w p9mw ppmw
16:50 10,4 28.0 110.x 33.2 0 s
16:51 10.5 27.7 112.6 24.7 0.7
15:52 10.5 28.0 113,4 4.3 0.3
15:53 10.5 28.5 112.3 72,4 0.5
16:54 10.6 78.4 111.3 7a.7 0.6
16:55 10.6 2a.6 110.9 81.4 0.4
16:55 1o-s 28.4 105.3 57.6 0.4
15:s7 10.5 2A.4 105.0 s6.2 0.5
16:58 10,5 28.6 105.4 44,2 O.1
15:sg 10.4 28.5 105.5 4?.2 0,4
1716
10
11
12
13
14
15
16
17
18
19
20
21
10
11
12
13
74
15
16
L7
18
19
L7toz
17:03
t0.5 29.0 106.4 31.2 0.s
17:01 10.5 29.S 106.5 45.4 0,4
r0.7 30.1 105-7 59.5 0.5
10.7 30.6 105.9 38.6 0.6
r7,U 10.6 32.0 105.8 56,1 0.6
u:05 10.7 32,3 105.3 72.2 0.7
17:06 10.9 33.0 104.5 108.7 0.3
10.8 32.1 104,0 104.9 0.517 t07
AEaa3a
co
c.
c."
comdcd Arcaa8!:
o.2 0.0 4.2 -1.0
0.1 -o.2 {.3 "1,1
0.2 {.1 -0.3 -l.t
9,1 26.9 170.L 1i14.5
9.1 26.7 110.2 144.3
9.1 26.8 170.2 1'!1.5
8.9 26.9 77o.o 1tt4.5ffi
17:oa 1O-8 30.5 103.4 94.9 0.4
20 17:g) 10,9 30.6 102.1 732.7 0.2
2L 17t7O 10.8 29.A 101.6 177.7 0.6
AwBc 10,6 29.7 105.9 66.t 0.5
0.1 {.2 {.3 -1.1
0.1 {.2 -0.3 -2.8
0.1 {.2 {.3 -2,0
9.1 26.7 170.2 t&.1
9.1 26.9 170,1 L42.6
9.1 2G.A 170.2 14!.5
8.9 26,9 170.0 t44.5@
c.
cr
Corrcdld AE6ga:
GP043AS-036878-RT- 1 579 Page 89 of 290
PRO,|.O358r8
P.clfiCo.p
Huntinlbn unlt 1
r/3ol2024
Td Run lS
StafrTlne 17i25
Run Length 2L
Stop Time !7i45
Uncoraded Analyzer Data
PROr-036878
P..tfiCqp
xuntlnlbn Unitl
4l?012024
Td Rh 116
StartTlme
Run Length
Stop Time
17:58
21
18:18
Uncorred.d AnalEer oata
10
72
13
14
15
16
77
18
19
20
21
10
11
13
14
15
1?
18
19
20
2L
Tlma
17:25
L7i26
L7t27
Ll128
L7t29
17:30
17:31
17 i32
U:33
L7 t34
17:35
17:36
L7t37
17:38
17t39
17:4O
17t41
!7.42
17:43
17t44
17i45
coa so. iro, co Nor
,6w ppfrw ppmw ppmw ppffi
10.9 31.s 104.8 779.7 0_3
10.8 31.7 105.4 175.5 0.5
10.8 31.7 105.9 182.4 0.8
10.1 30.9 107.1 151.0 0.5
10.9 3L.1 707.0 L52.2 0.s
10.9 32.5 L07.4 182.8 0.8
10.8 32.s tO7.2 182.6 0.s
L0.7 32.O 108.s 142.9 0.7
10.7 31.3 107.5 129.8 0.5
10.8 31.5 105.0 1il.8 0.6
10.8 32,0 105.8 191.2 0.6
10.8 31.9 107.5 202.A 0.5
10.9 32.5 106.1 271.5 0.6
10.8 32.3 108.7 211.6 0.6
10.9 32.3 107.9 188.3 0.6
10.9 32,7 107.3 239.3 0.5
10.9 32.4 108.3 233.5 0.5
10.8 31.9 108.5 239.9 0.5
10.9 31.6 r07.t U.r.A 0.6
10.8 32.7 108.6 191.6 0.8
10.8 33.4 108.1 164.0 0.6
cor sor ilo, co No,
Xw ppmw ppM pFnw ppmw
10.7 34.3 104.6 183.5 0.4
LO.? 33.3 102.6 215.2 0.2
10.8 34,2 103.7 L8/'.6 0.5
10.8 34.5 105.9 L49.7 0.5
10.7 34.0 107.5 132.5 0.8
10.8 34.6 106.8 176.5 0.5
10.8 34.4 108.0 r77,O O.5
10.8 34.7 106.3 163.6 0.5
10,9 36.6 103.9 153.6 0.4
10.9 36.5 101.6 119.9 0.8
LO.1 3s.1 101.5 73.9 0.2
10.9 35.8 101.2 109,8 0.6
11.0 36.4 102.8 173.0 0.5
L0,7 36.0 108.7 106.4 0.8
10.7 34.8 110.4 53.4 0.6
10,5 34.S 110.0 32.5 0.3
10.4
'2.7 108.7 15.2 0.5
10,3 32.5 106.1 5.9 0.3
10.2 31.2 105.2 0.2 0.7
70.2 30.8 103.0 0.4 0.4
10.1 29,9 107.4 -1.5 0.8
nma
17:58
17:59
18:00
18:01
L8:02
18:03
18:04
18:05
18:06
18:07
18:08
18:09
18:10
18:11
LBil?
18:13
18:14
18:15
18:16
18:Lj
18:18
c.
c.
c,.
Coil*d ArcEtc:
0.1 4.2 -0.3 -2.8
0.1 -o,2 -0.2 -1.0
0.1 {.2 -0.3 -1.9
9.1 25.9 170,1 142,6
9.0 26.6 L69,2 140.8
9,1 26,8 169,7 141.7
8.9 26.9 170.0 L44,5@
to7-2 188.0 0.6 AYeESe
c.
q
Comatcd Alwlal
10.6 34.1 105.5 105.0 0.5
0,1 -0.2 -0.2 -1.0
0,1 -o.2 -0.2 -3,4
0.1 4.2 {.e -2.2
9.0 26.6 169.2 1&_a
9.1 26.7 159.4 143.6
9.1 26.7 159.3 L42.2
8.9 26.9 170.0 1i14.5@
G P043AS-036878-RT- 1 579 Page 90 of 290
PROr{358rt
P..if,CoO
xuminabn Unit 1
qnl2074
Td Run f7
ShrtTime
Run Len8ih
StopTlme
PROJ{36tr!
Pacncor,
HuntlnSbn unlt 1
qinlma
Ta3t Run m
StaftTime
Run Length
StopTime
18:33
21
18:53
19:09
21
L9i29
Uncorreded Analyzer Dab Uncoreded Analwer Dab
10.1 30.3 115.4 1_5 0.s
18:36 10.1 30.4 L15.7 0.3 0.4
18:35
18:37
cor Sor iror co Nor
llm. ,6w Fpfrw pDmw ppm pptw
18:33 10.0 29.9 LL8.7 -1.3 0.4
18:34 10.1 30.5 115.8 0.3 o.7
cor sor to, co No,
Xw ppmw ppnw ppnw pphw
10.1 32.S 114.2 0.7 0.6
10.0 33.0 115.1 -0,1 0.8
10.0 34.S 114.6 2.8 0.5
10.1 33.5 113.5 4.0 0.5
10.0 32.8 LL4.1 0.7 0.2
9.9 31.8 115.4 -0.6 0.8
10.0 31.5 115.0 -0.3 0.7
10.0 30.8 113.6 3.5 0.6
10.1 30.8 113.8 -1.0 1.0
10.1 31.0 113.4 4.9 0.5
10.0 30.4 114.4 0.1 0.8
10.0 29.8 1L3.7 -0.2 0.8
10.1 30.3 1L3.7 -1.5 0.8
10,2 31.2 112.8 1.5 1.0
10.1 30.7 116.1 -2.L 0.5
10.1 30.6 115.9 -1.1 0.6
10.1 30.9 115.6 3.7 0.9
10.2 30.5 113.4 1.7 0.5
10.2 31.3 113.5 3.5 0.7
10.0 30.s 114.5 7.9 0.6
10.0 30.5 115.2 0.6 0.5
Tima
19:09
19:10
19:11
19:12
19:13
19:14
19:15
19:15
19iL7
19:18
19:19
t9:20
19:21
19:22
19:23
19.24
19:25
L9.26
L9.27
19:28
19:29
10.0 30.3 118.7 -1.1 0.3
18:38 10.0 29.4 118.6 -1.9 0.5
18:39 10.0 29.3 118.1 O.7 0.s
18:40 10.0 29.0 118.1 -3.3 0.2
18:41 9.9 28.5 119.9 -1.8 1.0
18:42
18:43
18:44
18:45
10
11
13
14 18:45
15 18:47
16 18:4E
17 18:49
18 18:50
19 18:51
20 !a52
10.0 2a.4 119.1 -1.1 0_4
10.1 28.5 118.0 ,1.9 0.7
10.0 28.6 119.7 {.8 0.5
10.1 28.3 119.2 1.1 0.5
10.0 28.1 118,8 1,0 0.6
10.1 28.0 115.9 -O.2 0.7
10.1 29.6 115,0 -0.8 0.3
10.1 31.S 114.4 4.4 0.4
10.1 33.5 115.1 5.3 0.9
10.1 32.2 114.4 1.5 0.8
10.2 31.r. t12.2 4.9 0.8
10
11
12
13
14
15
15
t7
18
19
20
2t21 18:53 10.1 30.4 114.5 -1.3 0,7
Av.r.t. 10,0 29.t 117.1 O.2 0.5
0.1 -o.2 4.2 -3.4
0.1 -0.2 -o.2 -4.5
0.1 -o,2 -0.2 -4.0
9.1 26.7 169,4 143.6
9.1 26.7 169.2 141.3
9.1 26.7 169.3 14t.5
8.9 26.9 170.0 144.5ffi
c.
c.
ctu
Coredcd Avet!:
q
c.
c,.
Cor€tud AYC]aSG:
0.1 4.2 -0.2 -4.5
0.1 -0.1 -0.3 -3.3
0.1 4,2 {.3 -3.9
9.1 26.7 169.2 141.3
9.1 26.4 159.4 140.9
9.1 26.8 159.3 141,1
8.9 26.9 170.0 L44.5ffi
GP043AS-036878-RT- 1 579 Page 91 of 290
Pio{:r6t t
P.dllc0rt
Huntlnttoo Unlt I
4lnlNA
Tl't Rsn 19
S&rt Tlme
Run L.ngth
Stop Tlhe
Un@ftctrd Analyzai Data
co2 so' t{or co xor
Mlnula TlD. taw perm ,FW FCow ppltw
1 19:44 10.1 34.2 1L4,7 5.0 1.0
2 t9:45 1o.1 }ts 114.1 t.1 0.6
3 19:45 10.0 33.8 115.6 L.4 0.3
4 19t17 10.0 3S.2 116,1 5,4 0-4
5 19148 1O.O 33.s 11s.4 3.2 O.,l
5 19:49 10.0 34.0 112.2 6.3 0,7
, 19:50
8 19:51
q
q"
cpdlcld aEr..rl
9.9 33.6 112,6 9,5 0.5
9.9 32.9 11s.1 3.5 0.8
19:il4
2l
20:04
9 19152 10.0 32.1 115.3 3.s 0.E
10 19:53 10.1 33.0 115,4 2,6 0,5
U 19154 10.0 32.3 118.3 {5 0.6
12 19:55 10.1 32.5 116.1 3,1 0.7
13 19rs5 10.0 32.0 117.5 0.9 0.E
14 t9:57 10,0 32.0 117.0 -1.4 0.6
15 19:5E 10.0 33.1 116,5 1.5 0,7
16 19159 10.0 33.6 115.0 2.5 O.5
17 20:00 10.0 333 115.0 1.2 o.7
18 iO:01 1(I0 32.9 116.9 1., 0.!
19 20tOZ 10.0 33.0 1163 {.6 0.6
20 20:03 9.9 32.3 7L7.7 1.5 0.6
21 2CO{ 10.0 33.1 115.7 4.8 0.5
Aw.ta ,OL3.2 115.8 1.2 0.6
0.r {}.1 -03 -3.3
0.1 {}.1 {.3 -3J
0.t {.1 {.3 -3.5
9.1 26.A 159.4 1,10.9
9.1 77.1 169.? 1i10.3
,.1 27.O 16t.6 tao.5
8.9 25.9 170.0 !44.5ffi
q
I
li
ii
GP043AS-036878-RT- 1579 Page 92 of 290
Appendix A,3.2
Unit 2
I
I
Appendix A.3.2.L
Low-Load FIow Data
Page 94 of 290
client PacifiCorp
Unit lD Huntington 2
Load low
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H2O)
02lo/ovdl
cO, (%vd)
Vr" Volume of Water Condensed (mL)
Vd Volume ofStackGas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
T. Temperature at Gas Meter ("F)
Calculatlons
Pn Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ('R)
Vwc(std) Volume of Water Condensed (scf)
Vm(std) Sample Gas Volume (dscf)
Stack Gas Temperature ("C)
B*.,", Saturated Moisture Content (%/100)
B*, Measured Moisture Content (%/100)
Bs Stack Gas Moisture Content (%/100)
2?.87 23.87 23.87
-4.30 -4.30 -4.30
888
11.5 11.5 11.5
73.7 73.7 73.7
33.289 33.289 33.289
0.997 0.997 0.997
1.8 1.8 1.8
74.3 74.3 74.3
24.00 24.00 24.00
534.3 534.3 534.3
3.47 3.47 3.47
26.30 26.30 26.30
44.3 44.9 45.6
0.115 0.119 0.L24
o.Ll7 0.7L7 0.LL7
0.116 0.L77 0.tL7
23.87 23.87 23.87
-4.30 -4.30 -4.30
888
11.5 11.5 11.5
109.4 109.4 L09.4
49.826 49.825 49.826
0.997 0.997 0.997
1.8 1.8 1.8
81 81 81
24.00 24.00 24.00
541 541 541
5.15 5.15 5.15
38.88 38.88 38.88
43.8 44.8 44.6
0.113 0.119 0.118
o.Lt7 0.1L7 0.LL7
0.113 0.1L7 0.117
23.87 23.87 23.87
-4.30 -4.30 -4.30
888
11.5 11.5 11.5
109.4 109.4 109.4
49.826 49.826 49.826
0.997 0.997 0.997
1.8 1.8 1.8
81 81 81
24,00 24.00 24.00
s4L 541 541
5.15 5.15 5.15
38.88 38.88 38.88
43.9 44.2 Ms
0.113 0.115 0.120
o.1L7 0.rr7 0.LL7
0.113 0.115 0.L77
GP043AS-036878.-RT- 1 579 Page 95 of 290
Low Load Run #1
Leation: Huntlngton 2
Load (MW): 206
Date: 417U2024
Start Time: 11:50
End Tlme:
Probe / Gas Data
Adjusted Results
Va(avgl: 24.19 ft/se<
Qsw: 35,947,468 wscf/hr
163
Pobe #1 RADo: 0 degrel
Prcbe;2 Ram: 0 deSrees
Prcbe#l Rsb: -01 detree3
Prcbe il2 Rs o: -lJ degre.i
8*,: 0.1162 %/10{l
Md: :Nr.16 lb/lh,mole
M,: 28.75 lb/lb-mole
Pb.i 23.87 in Ht
Pr: 4.m in H2O
P,: 23.55 ln tlg
CO2t l,-,5
%Or: E.0 %
'lCOt 0.O %
%
Flow RATA Traverse Data
Point lo Probe lD
corected
Sta.kTemp Y.wAngle YawAnde
(Fl (degl q(des)
PI.P2
(ln Hro)
Unadjusted Rcplament Point Used f WAF
Axlal Velocity Axlal Velcity for Points
v,(ft/iec) V"(ft/s*l wAF? t iedq
o01 110 7 1.1 0.11 o aoq zL.o42
002 I 110 -4 -3S 0.13 0.8090 22.426
003 I .A .3.9 0.15 o.8090 24.562
OM 3 4 .3.9 0.15 o mqo 24.s84
005 1 -4 -3.S o12 0.8090 21.9S0
005 1 1A .4.9 0.15 0.8090 24.572
007 1 t4 -3 .2,9 o 80go 25.439
008 1 t4 -3 2.9 0.16 0.8090 25.439 n/a
00!)108 1 2.a 0.11 0.8380 2r,736
010 2 109 -o.2 0.15 0.8380 25.43s n/a
011 2 -4 -2.2 0.16 0.8380 26.296 n/a
012 2 -0.2 o.t7 o.a3a0 27.772
013 2 12 -4 -2.2 o ro 0.8380 20.807
014 2 -1.2 0.15 0.8380 25.519
015 z -3 0.16 0.8380 26.355
016 2 t2 .7 -o7 0.77 0.8380 27.149
lveraSes 111.8 -2.8 -1.9 0.14 0.8235 24.430 nla nla
G P043AS-036878-RT- 1 579 Page 96 of 290
Low Load Run #2
Loetlon: Huntlngton 2
t@d (Mur)r t97
D$er UWm24
St.,ttimer 12:01
Endllme: 12108
Probe / Gas Data
Adjusted Results
va(avtl: 24.07 ftl*c
Qsw: 95,718,974 wxtlht
PtobatllRDo: 0 dlt'err
Prob!*2Reo: 0 deSre$
Probe fl RsE: -lrl deires
Probe #2 &Lo: -1.8 dcgres
8-: 0.1165 %/100
Md: 30.16 lb/lb-mol.
M!: 28.A lb/lb-molc
Pb,: 23.87 lnHg
P.r -4.:m in H2O
Pr: 23.55 in H8
%COr: UJ %
%Oi 8.0
"$%COt 0.0 ,6
&r,5 t6
Flow RATA Traverse Data
Point lD Proba lD
corectad
StackT.mp YawAngls Y.f,Anglc ?l-Pz
(F) (dEl (L {de) (in }Lol
Unadlusted Rlpl.cemcnt Point Usrd * WAf
Axlalvelodty AxiElVelGiV lbr Polntt
v.lftlxcl v. (ft/sl wAF? usedc-
001 109 4 -3.9 0.10 0.809 20.0o4
oo2 1 109 -3 o1 o aos 22.432
003 -5 4.9 0.16 0.8090 25.336
004 L4 4 o.t7 0.8090 26.196
005 172 -s {.9 o.11 o aos )1 001
offi 15 -2.9 0.15 0.8090 24.654
007 14 4 -3.9 0.15 0.8090 24.607
008 14 -4 -3.9 0.16 o.aos )s 414
009 roq {0.10 0.8380 20.754
010 10 4 -2.2 0.15 0.8380 25.440
011 14 .3 -1.2 o.17 0 mao n/a
0 l4 0.8 0.77 0.E380 27.L96 nla
013 14 -1 0,8 0.11 0.8380 21.476
014 14 1 2-8 0.13 o.Ba0 23.756
015 15 oa 0.1 0.8380 25.568 nla
o15 15 4 -2.2 0.L7 0.8380 27.202
lverages 112.8 -3.1 -2.1 0.14 o.8235 2t .315 tla nla
G P043AS-036878-RT- 1 579 Page 97 of 290
Low Load Run #3
Lo6tlon: Huntlngton 2
Lod (MW): 189
D.te: 4ll7l2024
StErtTime: 12:10
EndTime: l2tlt
Probe / Gas Data
Adjusted Results
fVec
Qsw: 35,157,133 wct/hr
Probe *l RM: 0 degr.cs
Proln #2 Rp6: g 6lgfgg3
Prob€rn&rc: {rl defeCs
Prob€S2RsLo: -1.g degrees
Bt r 0.1165 %/100
Mo: iO.15 lb/lb-mole
M,: 28.74 lb/lb-molc
Phrr 23.87 In Hg
Ptr 4.:lO ln H2O
Pr: 23.55 In Hg
%COzt 1L5'6
Kr:__3*
%CO, 0.0 96
80-5 %
Flow RATA Traverse Data
Polnt lD Probe lO
Coricctcd
Stacl Temp YawArylc Yaw AntlG
(F) (dG8l o,(desl
PI.P2
(ln H,0)
UnadlGtad Repkcmcnt Po,nt U*d f WAF
tui.l velcity AI|d Velocity for potrtt
v.(ft/*cl V.(ft/sGcl WAF? lrsedq,
oo1 110 .5 4.9 0.1t 0.809 20.971
002 I 113 4 -39 0.13 0.8090 22.SAA
003 I 114 2.9 0.15 0.80{24.633
OM I 115 4 -3.9 0.16 0.8090 25.436
00s 1 113 4 -39 0.10 0.8090 20.o74
006 116 J 3.9 0.15 o 8090 24.650
o07 1 115 -3 2.9 0.15 0.8090 24.654 n/a
008 1 116 -5 .4.9 0.15 0.8090 14 617
009 -3 -t.2 0.11 o Seao 21.835
010 2 114 4 -2.7 o-14 0.8380 24.64 n/a
011 2 774 4 0.15 0.8380 25 529 nla
o12 -3 r.2 0.15 o a3a0 25.565
013 2 113 -3 1.2 o_ 10 0.8380 20.437
014 2 -4 0.14 0.8i:|80 24.685
15 {-2.2 0.1s o aSao 25.5S2
016 2 115 4 2_2 o17 0.8380 27.202
lverateS 114.1 -3.E -2.9 0,14 0.823s 2e.9A7 nl^ alt
GP043AS-036878-RT- 1 579 Page 98 of 290
Low Load Run #4
letion: Huntington 2
Lo.d(Mwlr 190
Date: 4ltu2o2e
StanTim€r 12t28
EtrdTime: ,j2,36
Probe / Gas Data
Probc *1 Reol 0 dcSrees
Probe #2 RDo: 0 defees
Probe rn &e: .01 dcgeer
Prob€f2Rsro: .13 defret
B-: 0.u29 %/100
Mdr :10.16 lb/b-mol.
M!: 2E.79 lb/b-mol.
Pb,: 23.E7 ln Hg
P,: {.:}0 ln HrO
P!: 23.55 in H8
XCO!: us %
ffii4%
9{CO: 0O X
Adiusted Results
avgl: 23.40 ft/sec
Qsw: 34,834,77L wtdlhr
Flow RATA Traverse Data
Point lD Probe lD
Correctcd
StackTemp YrwAngli YrwAn8lc
lFl lddl o. rderl
PI-P2
lin H-Ol
UnadrustGd Raph.m€nt Point Usld * WAF
Axlal velocity tuial Vclclty for Points
V- lftls.l v- lltlmcl wAF? U3.dL
001 10 4 -3.9 0.10 o.ao9 20.006
o02 10 {-3.9 o.r2 0.8090 21.915
003 10 0.1 0.8090 )t s)2
004 1 4 -3.9 0.15 0.8090 24.524 nlz
005 1 10 .3 -2.9 0.11 0.8090 21.004
om -39 01 o 80go )) 470
007 1 4 -3.9 0.15 0.8090 24.524 nla
008 1 1 4 -3.9 0.15 0.8090 24.524
o09 10q -))0.1 0.E3E0 I 7qO
010 2 10 .4 -2.2 0.t2 0.8380 22.737
011 2 10 1 0.8 0.15 0.8380 25.437
ot)-o?o1 o a3ao
013 2 1 2 -o.2 0.10 o.8380 20.749
014 2 13 -3 -t.2 0.14 0.8380 24.636
01s -12 0.15 o &330 )\ n79
016 2 1 3 -L.2 0.16 0.8380 26.291
{vetaaB 110.8 -3.3 -2.3 0.14 0.8235 23.633 nla nla
G P043AS-036878-RT- 1 579 Page 99 of 290
Low Load Run #5
location: Huntin8ton 2
t@d (Mwlr 190
Date! 4ll!2024
Strt Time: 12:38
EndTime: 12:4li
Probe / Gas Data
Probe f1 Roo: 0 defees
Probe *2 R-o, ---------J degrees
Probe #1 Rao: -0J degrecr
P.obe #2 R5ro: -1.8 dlt,ecs
B*: 0.U59 %/100
Mdr 30.15 lb/Emolc
M.r 2E.74 lb/lb-mol.
Pbi 23.67 ln Ht
P.: .4.:m in H2O
P,: 23.55 in Hg
%COzt 11.5 %
.AO2t 8.0 %
%CO: 0.0 %
80.5 %
Flow RATA Traverse Data
Polnt lD Probe lD
CorEcted
StlckT.mp YawAnglc YawAngle P1-P2
(Fl (desl q" (des) (ln H,ol
Unadiust.d Repl.cmcnt Potnt Usd f WAF
Axi.lveloclty Ari.lvelclty fo. potnts
%(fvtec) v.(tV*cl wAF? uscdc.
001 10s 4 .3.9 0.09 0.809 18.979
oo2 2 4 .3.9 0.13 o aos 22.470
003 t2 3 -)9 0.15 0.8090 24.592
004 1 2.9 0.14 0.8090 23.779 nla
005 2 -4 .3.9 0.10 0.8090 20.058
006 14 -5 Jq 0.13 0.8090 22.A79
007 -4 ,3.9 0.1s o_4090 24.588
008 -3 .2.9 o.1s 0.8090 24.6L3
009 10 ,0.0.10 0.8380 20 749
010 0.13 0.8380 23.745
011 13 -2 o.o 16 0.8380 26_365
o72 1A -0.0.15 0.8380 26 348
o13 4 -2.2 0.11 0.8380 2L.826
014 14 -3 0.14 0.8380 24.679
015 7t -!0.15 0.8380 25 q4q
016 !4 -3 0.15 o 83AO 25.545
lvelages 112.6 -3.2 -2.2 0.13 0.8235 23.578 nla nla
GP043AS-036878-RT-1579 Page 100 of 290
Low Load Run #5
Location: Huntlngton 2
to.d (MWl: 192
oate: 4lt!2024
StanTim€: t2t47
EndTime: 12:55
Probe / Gas Data
ProbaflRDo: 0 dcgr6.s
Ptobc f2 Reor 0 deg.ees
Prob€#l &e: .01 defees
Prob€*2Rao: -1.8 degrees
B-: 0.u69 %/100
Md: :,0.16 lblllmole
M,: 28.A lbllEmol.
Pb,: 23.87 in Hg
P,: -4.:X) in H2O
Pt: 23.55 ln H8
%COrr us %
%Oi 8.0 %
%CO: 0.0 %
%
Flow RATA Traverse Data
Point lO Probe lO
Colrcctad
StackTemp YrwAnde Y.wAntle Pl-Pz
(tl (der) o-(der) (in H,ol
Unad,usted Rcplacemcnt Point Used #WAF
Axialvelocity Axialvelocity for Poiirtt
v. (fvsec) v. (fri/scl waF? Usedc-
001 4 -3.9 0.10 0.809 20.047
ool I 113 4 -39 o1 o aom 21.997
003 14 2.9 0.15 0.8090 24.635
004 14 4 .3.9 0.15 0.8090 2S.415
005 -4 -39 o10 o 8090 20.osa
006 4 0.13 0.8090 22.A90
007 13 -3 -2.9 0.15 0.8090 24.6t3
00a 14 -3 o1 o aom 24 63\
009 10 -0.2 0.09 0.E380 19.722
010 -3 -1.2 0.13 0.8380 23.7t9
011 4 -22 01 0 $40 25 510
012 4.2 0.15 0.E380 25.S2A
013 10 {-2.2 0.11 0.8380 27.7a4
014 4 -2.2 0.14 0.8380 24.602
015 0.1 0.8380 )\ L79
016 -L.2 0.15 0.8380 25.523
lvetaECs t12.3 -i1.4 -2.4 0.13 0.823s 23.509 nla nla
GP043AS-036878-RT-1579 Page 101 of 290
Low Load Run #7
Locatlon: Huntlnttor 2
lo.d (Mw): 190
Date: 417il2024
Startlime: 72t57
End Time: 13:04
Probe / Gas Data
Prcb€rnRoor 0 de$ees
Probe;2 RDoi 0 dcgr€es
Probe fl &d {r.1 d€gr€es
Prcbc f2 Rsro: -1.8 deg..es
8s: 0.u33 %/r.00
Mo: i10.16 lb/lb-mole
M,: 28.78 lb/lb-mole
Pb,! 23.E7 ln Hg
P.: -4.m ln H2OPr:-31:1lnHr
%COz: 11.5 %
Ot t.0 ./"
/{Ot 0.0 %
80.5 %
Flow RATA Traverse Data
Polnt lD Probe lO
Corr€ctcd
St.ckTemp YawArEle YawAngle Pt-Pz
(F) (des) q(desl (lnH,o)
Un.dlustcd R€!ilacment Polnt Used fWAF
Arialvelcity Arlrlvclocity for polnts
v. (fv*c) v, (fV*cl wAF? t sedc"
o01 109 4 -3.9 0.09 o aog 18.964
002 111 ,5 -4.9 0 0.8090 2t.907
003 t72 .5 -4.9 0.14 0.8090 23.683
ou 4 -3.9 0.15 0.80s 24.s69
005 109 4 3S 010 0.8090 19-990
005 4 3.9 0.72 0-8090
oo7 113 -3 -2.9 0.15 o aoso 24.594
008 113 -5 {.9 0.1s 0.8090 24.536
009 t0 4 2.2 0.11 0.8380 )1 771
010 l0 4 2.2 0.13 o Saao 23.667
011 l -2 -o.2 o.15 0.8380 25.4U
012 4.2 0.16 0.8380 26.322
013 109 {-2.2 0.11 0.8380 2L.752
014 110 4 0,13 0.8380 23.667
015 111 -2 4.2 0.16 0.8380 26.299
015 111 -2 -o.2 o_16 0.8380 26.299
lverates 110.9 -3.5 -2,7 0.13 0.823s 23.464 nle ^l^
GP043AS-036878-RT- 1 579 Page 102 of 290
Low Load Run f8
Lqtion: HuntirBton 2
load (Mlirlr 190
Date: 4hU2O24
StanTime: 13:05
EndTimer 13:u
Probe / Gas Data
Adjusted Results
va(avgl: 23.93 ttlsec
Q5w: 35,574,071ws<tlht
Probo rll Reo: 0 degreci
Prob!#2Reoi 0 dGgees
Probe #1 R$o: .01 deSree!
Probc*2q@: -1.8 degrr€s
B-:_______-tglM%/10o
Md: 30.16 lb/lEmol.
M.: 2E.75 lb/lb-mole
Pbi 23.87 in H8
Pr: 4.:10 in H2O
P.: 23.55 in Ht
%COr: u.s %
%O2t 8i 'h
l"COr 0.0 %
80.5 96
Flow RATA Traverse Data
Point lO Probe lD Stack Tefip
(Fl
CorEctrd
YrwArglc Y.wAnde Pl-P2
(dHl O-(derl lin H,ol C
Unadiusted RepaGment tointused SWAF
Axlll V€lGity tulal Vcl@ity lor Points
v.(ftlsecl v^(ft/se(l wAF? Used
001 109 -5 4.9 0.10 0.809 19.973
oo)10 -)q o aos 21.SS1
003 t2 .3 0.15 o.aos 24.585
004 12 .3 -2.9 0.15 0.8090 24.545 nla
oos 10 4 0.09 o aos t8 990
t2 4 -3.9 o.12 0.8090 2L.966
007 1 111 4 -3.9 0.1s 0.8090 24.534
008 -4 -3.9 0.15 0.8090 24.559
009 109 -5 -3.2 0.12 0.8380 22.771 n/a
010 2 110 6 -4.7 o_ 1s 0.8380 25.385
011 -s -3.2 o.t7 0.8380 27.103
012 13 5 4.2 0.17 0.8380 27.096
013 12 -5.2 0.12 o.8380 22.713
4 14 -1 -s2 o1 o.a3a0 27 _Oat
015 14 -6 -4.2 0.16 0.8380 26.310
015 14 -5 -2.2 o.t7 0.8380 27.150
wGra8es 111.5 -4.8 -3.9 0.14 0.E235 24.t5a ala nla
GP043AS-036878-RT-1579 Page 103 of 290
Low Load Run f!)
locatlon: Huntlngton 2
toad (MWlr 190
Date: 4lttl2024
Start Tlm€: 13:13
End Tire: 13:18
Probe / Gas Data
Prcbc fl Reo: 0 degraes
Prob! f2 Reo: 0 degrees
Probe fl &E: .01 degrces
Probe f2 Rsro: -1.8 degicGs
Bs: 0.1169 %/100
Md: :10.16 lb/lEmol.
M.: 28.A tb/tb-motc
Pb,: 23.E7 in Hg
P.i .4.30 in H2O
P,r 23.55 ln Hg
<t6CO2t l,-.5 "A
%Ozt 8.0 %
%COr 0.0 %
80.s %
Flow RATA Traverse Data
Point lO Piobe lD
Coirccted
StackTsmp YlwArBle Y.wAnglc ?t-Pz
(F) (des) q, (desl (in x,o)
U6adj6ted Rlplaem€nt Point Ured S WAF
Arirl Velfiity Axial Velcity for potnts
v. (fVec) v. (wilc) wAF? r.rtedq
001 110 -5 4.9 0.10 0_809 19.996
oo2 l3 4 -3.9 0.13 0.8090 22.890
003 113 5 49 0.16 0.8090 25.360
004 714 3 2.9 0.16 o aos 25.443
00s r72 4 -3.9 0.11 0.80q1 21.037
006 113 4 0.13 0.8090 22.890
007 4 3.9 0.15 0.8090 25.416
008 3 -2.9 016 0.8090 15.U?
009 10 -4 2.2 0.12 o_Bao 22.751
010 2 -5 .3.2 0,15 0.8380 25.466
o11 3 {4.1 o 17 0.8380 27 7M
072 14 -3.2 0.19 o.4380 24.1t7
013 2 4 .2.2 o.74 0.8380 24.623
074 t4 -5 0.15 0.8380 25.511
015 t14 0.18 o.4380 27.946
o16 L4 4 -2.2 0.1a 0.8380 21.969 nla
rverates 112.9 -4.4 -3.4 0.15 0.E235 24.910 nla nla
GP043AS-036878-RT- 1 579 Page 104 of 290
EPA Method 4 Datasheet
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GP043AS-036878-RT-1579 Page 105 of 290
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GP043AS-036878-RT-1579 Reviewed: FPM CPMf'-rU6 of 29U-
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EPA Method 2F Datasheet
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GP043AS-036878-RT- 1 579
Reviewed: FPM CPM80ilU7 of 29Il-
0vt M .,N I RU.\ b EPA Method 2F Datasheet
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hurca:ll--li-L-. tl'l Strtilc Ptrrcutu I'l{'Ol:- Lt.3 ProDa Condldon
Dete:L, - il- lr{ProDc lD/Allnmcnt r't) / t39 cqln tr. <
lun I 3 llelChcdrl'lLol:Llxl ?.,C,
itertTlmc:lXlo ItooTlma:t2, tl [eolxl
Lou L",- J
lnwrsc Polnt lPo]t-Polntl
StrclTemp
{oFl
YewiArtlc
Itll€d
UclocltyAP('Hpl
lPl-P2l
Pltch AP ('H2Ol
lP4+st Commcnts:
-l llo -e a.I
-:.,13 -q o.t3'3 tll -f o.15-
-q ,,5 -Ll o.lLt-ll3 -t;o.,o
-{llc.-rl O.rS-3 It .3 O.t5-q llb -_q e). l_t
3-l ,,4 -3 O.t t
^i lt 't -(,O.t",l
-3 ,l'-tJ O.t(
-Lr lr.Y -3 o.t 5
L,-,13 -e 0.to
-J ,,s ^ (.{o.lLl
-J lls -Ll o.tf I
r(4 Irs ^(l o,, )
Schemedc
Diameter (D)=
Polnt t Olst. From Stsd( Well
1
[=
l=
2
3
4
5
6
t
N
Pon lO
A
B
c
D
GP043AS-036878-RT-1 579 Reviewed: FPM CPM6g'ilU8 of 29ff
lrolcciCodr d%ga8 Oocrrtrld:ALIAn/. L lo
trknt ? o r:tiuarp brunrilrlc Pnrrrttr l'Hrl:)3.17 il..
lourca:d..l:-l*- 0-t ttrdcFlcrorul'lfiOl:- Lt.s Pro!:Godltlon
DTE;Q-rt -lrf Prub:lD/Altsmcnt It7 ./ t 3s-tBl$rl <
tunl L{Lark Chec* l'lLOl:t/Llxl Ec)
il.ilflmr:lf.a s lboTlmc:lf,3G &olrl
EPA Method 2F Datasheet
64\ YOl lR,u)!
L orn L"oc)
Inyrrrc Pdm lPort+olntl
StsctTrmp
l"fl
Yrw'And:
lrDttl
UclodtyaPfHlol
IPr+21
PhdraPl'Hpl
19.+51 bmmcnts:
l- (l,o -q a.to I
-)lto - t.,o.t\
-3 ,lo -3 n.r5
-Y n _rl o. ts
2-lo -3 D.t
-)t3 -q O. ,3
-3 ll -Ll o. t5-q nI -Lt o.ls
?-l0.t -q o.l
-)lro - r"l o.t l
-3 llo a. ls
-q I -f 6 t7
Lt-ill -a o- to
-a tt3 --1 b t.{
-3 ilL -'1 O. t5
-rl I -3 o.tL
Schema0c
Dlameter (DI=
Polntf Dltl. Fun Shd(Wrl
I
fi=
$=
2
3
4
5
5
t
N
Pod lO
A
B
c
D
G P043AS-036878-RT- 1 579
Revlewed: FPM CPM
Eg-e-fUg of 29U-
EPA Method 2F Datasheet
PrdcctGodc bSLF*e Cnrrerrkl:ALla n / r-r-tm
dIGnG P-,-i(ir-., o lelrrnrtlc Pnrrur: l'lld: >1. y-z Lo
hsru:[.,-&.1o.'tJ'-)S*Plrrsnl'tLol:t{.3 ProbCcondlUon
h:u-'-a I Probc lD/Alhnmnt l> / rsf 0(Ll$(4
tun I 5 LrrkChcclPlLOl:tr q($E, C,'
ItertTlme:la3,itooftnr:laI 5 Hp(xl
L o.^l L ""r, d
Inucrrc Pdnt IPoGPo[rtl
StrtTrmp
frt
Yrw/l4le
ItDreI
VebdtyOPl-l{rol
lpl-P2l
Phdl6PrHrol
tP+Pst Eunmcntr:,-l lo c\-Ll o.o .l
-&t2 _({o. t3
-3 ,,I -f,D.,S
r{r3 -a o.t1e-l ,tl_-tt o.to
-f ,Lt -e o.l3
-3 ,ta _Lf 0.,s
-Ll lll -5 O. rf
t-tlo -.1 o, lo
--}lta.-I o. t3
-3 ta -.L o .16
-.1 I tl -l rt lL
ry-r ilf r{o.t I
-l ,lc{-.3 o .ttl
-3 lrl -f, o.t 5
-q , lG{-3 D. t 5
SchemeUc
Diamater 1D1=
Polntt Uct. Fronr Strd( mll
I
l,=
l=
2
3
4
5
6
t
N
Po.l lO
A
B
c
D
GP043AS-036878-RT- 1 579 Reviewed: FPM CPMPEgtrlO of 29CI--
,6A llll N I RgS lr EPA Method 2F Datasheet
,rolcciCodG o368:7#Oocnodrlr ALIAR / tL L-
Ilctrt ?^.'.Liu.e p hrumalcPrwur [']ld::r. ur f..
bura:tl.,Jr^^le.- D-l ilrdcPlaram l'll0l:- 9.3 lrobaCddlddt
lrb:- 711Lt-Probc lD / AlltmGnt tt'? / t3{sq($rr5
lun I L lrrkChetll'll'Ol:Llrl 8."o
tnrnfhrc:I 1r.17 ilooTlmr:la.s q iLofil
L or^t Lro,c)
lrrter- Polnt lPortfolntl
SledrTcmt
t'Fl
Yrw'Atrjlc
I+ Ded
VdodtyoP('Hrol
lFl-D2l
Plich AP fHrol
lna.Psl lomncnts:
-t llt -(l 0,to I
-).t3 -q o. l;
-3 t{3 O.rf
-q , ltl -c{o t6
<ilx -q o.t o
-.)lt3 -Ll o.t 3
-E 1,3 -(o.t5
-q Irq -3 O.l s
t-t,o -f o 01
-)t,-3 (1.1a,
'3 r3 -q 6.tf,
-q t3 -:.o. 15
v-llo -q fr.ll-J il - Crl o. l'l
-3 I lr -3 o.ts
-Ll n3 -3 r)ts
Schematc
Diamaerlol=
Polntl Dbl. Ftom Slrdr W![
1
f,=
B=
2
3
4
5
6
1
N
Port lO
A
B
c
D
GP043AS-036878-RT- 1579 Revlewed: FPM CPMEgETIT ol 29lJ-
PnilrctGodr t>3L? ?ft 0ecraukl:[l-lan. )u^[*
0hnG t^ .'.f:, --o luunrclcPruarrr flld:)-r.ff)lo.
bure:U..^{:-^r'-- l)-f Stlt Ftunrtr l'll'Ol:-Gt 3 ProbrGodllhn v
Drte:Lt-
'l - .)rt hobrlD/Albmrnt lt7 / 139 EGIII lr.5
iunl -)L:et Chccl lrH'Ol:DTTI 8.a
ileililme:tesf !!ooTtnc:'l3o {[2o(xl
EPA Method 2F Datasheet
64\ Mgfi r,Rplh
L
L od LrnJ
Ireucnc PomlPortPohrtl
SteckTrmp
fFt
YrwAluh
IrDrd
VclodtyAPfHlOl
lPl+21
PftdraPfHrol
IPa+51 iommctils
loA -q o.o q t
-.1 eJ 0.1
-3 t -5 o.1,1
-cl t?-4,d rs
)-t lot -1 O. to
-2 ,t I -Ll o.re
-3 lt3 -3 o.to-
-.1 r3 -9
3-l rl0 -c{O.t
-f.l,o -q o.ts
-3 -.l-o. It
-({lr2.-1.O.t t
U-l to1 -q o
-)tlo -tl D. r3
-?ltt -a o -ll
-Ll tt -a e,*d*Y I
Schemrtc
Diameter (D)=
cgA=
ce B=
Pohll Olst.Fromsledw.ll
1_
2_
a_
A-
q_
6
PdTlo
A
B
c
D
GP043AS-036878-RT- 1 579
Reviewed: FPM CPMfrd€'ITZof 29V
,e4\MO N I R,S L, EPA Method 2F Datasheet
,rdcctGadc osL? 7&Dpcrrbrkl:LLtns lzt [^-
trhnE l-.t f'.c.r a llrun:lrlcPnsuru('l*l:)?- x7 L.
lilrE!:U.,rll-L. - U'{Strdc Prusut: l'll{l:-Q.3 Prubrcordldotr ,J
hr:tl-il-)9 Probr lD / llkrunrnt n'7 L 3.f BGIXI rr. {
lunl <l l,:rt Chcdr l'lL0h ,7 Llxl fl.c,
illilnmG!t30 L ilooTlmc:t3 t,ll,ol$
Lcwt L"^)
Irrycru PolmlPortPoml
StrkT:mp
tTr
Yew'Ar5lc
l+ Dltl
VdodtVAPl'HrOl
lPl42l
PhdtaPfHpl
lPil.Dlrl Conuilntr:
lool O.lo
-:I lo -)b lf,
-3 r?--3 O.r.f
-Ll ,,2 -3 D..l s
J-lo _Ll 6.o't
-J lrt r{o. t1
-B ilI -Ll 6. l5
-l{ta -q o.l t
3-,ol -s D. ra
-J lo --5 O, tS
-3 It2.O. t7
-cl il3 -e /)t2
Ll-t2 -7 o. tA
-.I l rr.l -)O t'?
-3 I tt{nl o.l6
-c{,I1 -6-o. 12
Schematlc
DiamAerlD;=
Poh I lllrt. Fmm Siadt Wel
1
l,=
t=
2
3
4
5
5
I
N
Port lD
A
B
c
D
GP043AS-036878-RT- 1 579 Revlewed : F rM-rS_rrrCfrY-
O4\ MII N I R0.\ L EPA Method 2F Datasheet
PralrctCodG n\A?.AF Dsrnta{rl:AEJAE II T,L-
dhrt P.rf .rtr t,lrmmticPrrrarn trlld:le.v:t.
lqrrc:l [..-[ie-la, - l1-)ffiFlrrcunFHfl:- q.3 hobrGonddor
DeE:U- il-rLr Frtd:lDlAlhtm:at D / t35 !Gt$ll 5
Rml q lret Chccl l'll,Ol:
'L/Llxl ()C. LI
ttertTlna:l313 ftosftnc:,3t([ro lrl
Lo,.) Lo ^c)
I;rvrrs Polnt lPortfolntl
Slecklcmp
frt
Yrw'Arth
l+ Dlrl
vdodty.PfHpl
lDl+21
PhdrAPl'Hpl
lPa-Psl Commcnts:
lo -q 6.1 er
-e t3 _e,o. r3
-,t3 -s a t6
-Ll ,.{-3 a t6e-l ilf.-c{0. tt
-.2 il3 -cl o.t3
-3 f lq -Ll o.lb
-Ll f'1 -3 o. t 6
3-llo -Ll o.l7
-)trf.-5 A. r5
-,ll3 -c 6. l-7
^t{llul (> lt
rt- I lr?--Ll o. ,"{
-t I lal ^S o.ts
-?ll.l -c;o. l6
-H ,, LI -4t o .la
Schematc
Diameter (D)=
Polntl pEt E!gnSEA$|!|l!
1
fi=
fl=
2
3
4
5
6
I
N
Port lD
A
B
c
D
GP043AS-036878-RT- 1 579 Reviewed: FPM CPMPtEsTI4of 2Xl-
i
Appendix A.3.2.2
High-Load Flow Data
Client PacifiCorp
Unit lD Huntlngton 2
Load High
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H20)
O, (%vd)
CO1(/ovdl
Vr. Volume of Water Condensed (mL)
V. Volume ofStack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
T. Temperature at Gas Meter ('F)
Calculations
Pm Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ('R)
Vwc(std) Volume of Water Condensed (scfl
Vm(*d) Sample Gas Volume (dscfl
Stack Gas Temperature ('C)
Bwssat Saturated Moisture Content (%/100)
Bs Measured Moisture Content (%/100)
B*" Stack Gas Moisture Content (%/100)
23.87 23.87 23.87
-5.30 -5.30 -5.30
566
L2.5 12.5 t2.s
23.87 23.87 23.87 23.87 23.87
-s.30 -5.30 -5.30 -5.30 -5.30
66566
12.5 r2.s t2.5 t2.5 12.5
126.5 126.5 133.8
50.358 50.358 s0.s3
0.997 0.997 0.997
1.8 1.8 1.8
73.2 73.2 77.3
23,87
-s.30
5
72.5
24.00 24,00
533.2 s33.2
5.9s 5.95
39.87 39.87
46.3 46.s
0.129 0.130
0.130 0.130
0.129 0.130
133.8 L21.2
50.53 50.546
0.997 0.997
1.8 1.8
77.3 80.2
24.00 24.00
537.3 540.2
5.30 5.70
39.70 39.50
45.5 46.4
0.123 0.729
0.137 0.125
0.723 0.726
L2!.2 131.8
50.545 50.s34
0.997 0.997
1.8 1.8
80.2 82.2
24.00 24.00
540.2 542.2
5.70 6.20
39.50 39.34
46.7 46.0
o.r37 0.127
0.126 0.135
0.126 0.L27
131.8 87.7
50.534 34.045
0.997 0.997
1.8 1.8
82.2 83
24.OO 24.OO
542.2 543
5.20 4.10
39.34 26.47
46.7 45.9
0.131 0.126
0.136 0.134
0.131 0.t26
24.00
537.3
6.30
39.70
45.6
0.131
0.137
0.131
GP043AS-036878-RT-1579 Page 116 of 290
High toad Run #1
Location: Huntington 2
Load (M!ir): 43,
Datc: 417,/2024
StanTlmer 14:42
EndTlme: 15:19
Probe / Gas Data
Prcb.ll Re: 0 degrer
Prcbe f2 Re: 0 dcgrei
Prcb€ *1 Rs: {J detEes
Prcb€ rD Rs@: -13 drtres
Be,t 0,128, %llgJ
Md: :Nr.24 lb/lb'mole
M.: 2t.55 lb/lb-mole
Ph.: 23.87 In Hg
P.: -5.30 ln H2O
P,r 23./18 ln Hg
COrt I2-S cfr
%Or: 5.0 %
%CO: O.O 96
Adiusted Results
Va(avgl: 47.25fttsec
Qsw: 69,595,t148 rcc/hr
Flow RATA Traverse Data
Point lO Prcbe lO
correded
StackT.mp YawAntle YawAnglc PL.P2
(fl lder) o-(d!rl (ln H,ol
Un.dlustcd Rcplacrmlnt Point Urld * WAF
tul.l Veloclty Axlal Veleity lot Points
v.lftlecl V.(ftlsecl wAr? Usadc.
001 115 -3 -1.2 o.4l 0.838 a2.390
m2 174 0.53 0.8380 48.059 nla
003 116 L 5.8 0.57 0.8380 49.740 a/a nla
004 115 5 5.8 0.s7 0.8380 49.6e
00s 11q 0.8 0.3E 0.8380 40.815 nla nla
006 115 2 3.8 0.54 0.8380 48.553 nla
007 116 2 3.8 0.58 0.8380 s0.362
o08 116 0.56 0.E3E0 49.485 nla
009 1L4 0 1.8 0.40 0.8380 4r.422 ala
010 115 -0.2 0.56 0.83m 49.SS2
011 11S -1 oa om 0.8380 57.287 nla nla
01)116 0 1.8 0.50 0.8380 s1.311 nla nla
013 114 -o.2 0.37 0.8380 4.243
014 116 0 1.8 0.59 0.8380 50.a81
o15 115 -l 0.8 0.52 0.8380 47.747 ala
016 116 4.2 0.61 0.8380 s1.762
lverat$115.3 0.3 2,1 0.52 0-4380 47.736 nla ale
G P043AS-036878-RT- 1 579 Page lL7 of 29O
High Load Run #2
Location: Huntlngton 2
Load (MW)r 435
oate: 4lttl2024
StanTlmc: 15:32
EndTim.: 15:52
Probe / Gas Data
Prcbe fl RMr 0 detr€
Prcbe r42 Reoi 0 degres
P.obe*1 Rs@: .OJ detrees
Pbbe 12 RsLo: -l.8 d.trces
fu: 0.1299 %/100
Md: 30.A lb/lb-mole
M,: 2E.65 lbllb-molc
Pb.,: 23.87 !n Ht
P.: -5.30 ln HrO
P,: 23.48 in Ht
%COr: 12.5 9(
%Or: 6.0 %
81-S
Flow RATA Traverse Data
Point lD Pbbe lD
Corrcd€d
StaclTemp YawAngle YawAnglc P1-P2
(F) (ded q (der) (ln Hro)
Unadlustcd Rcplacement Point Us.d |WAF
Axlal Velo.ity Arial Velcity lor Points
V.(ft/tec) V.(ftlsecl WAF? Us€dc-
001 2 13 -2 -o.2 0.38 0.838 40.758
002 7 15 4,8 0.53 0.8380 48.092
003 2 3 4.8 0.5s 0.8380 49.033
004 2 3 4.8 om 0.8380 51.214
00s 15 2 3-8 0.35 o.8380 3S O98 nla
006 2 2 3.8 0.s3 0.8380 48.797 nla
007 2 3.8 0.58 0.8380 s0.419
008 2 4 5.8 0.58 o.4380 50.271
009 2 15 0 1.8 0_3a 0.8380 r10.809
010 2 ta 4.8 0.54 0.8380 48.4S9
olr 16 3 4.8 0.55 o aaao 48.991
ot2 2 15 3 4.4 os7 0.8380 49.473
013 2 t4 4 5.8 0.36 0.8380 ?q so3 nla
014 2 115 2 3.8 0.52 0.8380 47.657
015 2 115 4 5.8 0.54 0.8380 48.465 nla
016 116 4 5.8 0.55 0.8380 48.911
lveraSes 115.7 2.5 4.3 0.51 0.8380 tt5,859 nla nla
GP043AS-036878-RT- 1 579 Page 118 of 290
Prcbe *1 RM: 0 degrees
Probc #2 R@: 0 degrees
Probe S1 Rs@: {l detrees
Probe #2 Rs@: -tJ degrees
4,,:___g_1!91%/1@
Md: 30.24 lb/lb-mole
M.: 28.64 lb/lb-mole
Pb.i 23.87 in Hg
Pr: -5.30 ln HrO
P,: 23.'18 ln Ht
tr.olt lz"s
Ori 6.0
96CO: 0.O %
81.5 %
High toad Run #3
Loetlon: Huntintton 2
Ioad (Mw)r 435
Date: 417112024
Start Tlme: 15:05
EndTlmer 16:25
Probe / Gas Data
Unadiusted Results
lavgl: 47.3zftlscc
Qsw: 69,617,5t14 wcflhr
Adiusted Results
qsw:
Qsd:
46.85 ftlsec
68,921,368 mct/hr
Flow RATA Traverse Data
Point lO Probe lo
Corrccted
StackTemp YawAngle YawAnglc P1.P2
fFl ld€sl (Lld€rl lln H,ol
Unadlustad Rcplft.meni Polnt Used f WAF
Ail.l velocaty Axial v€leitv for Points
v.(ft/*cl v,(ft/secl wAF? usedC
001 1t4 -3 -1.2 o.37 0.838 &.252
002 2 115 3 4.8 0.54 0.8380 48.510
003 2 3 4.8 0.58 0.8380 50.319 n/a nla
o04 16 4 5.8 0.60 0.8380 s1.096
005 2 16 2 3.8 0.40 0.8380 4L.842
006 2 4 5.8 0.55 0.8380 /r8.963
oo7 58 osa o 4380 50.184
008 2 16 4 5.8 0.5s 0.8380 48.921
009 2 2 3.8 o.37 0.8380 40.208
o10 15 18 o5?o atm 44.12)
011 2 16 4 5.8 0.s6 o.E380 49.353
012 2 2 3.8 0.58 o.8380 s0.385
013 2 1S 2 3.8 0.38 0.8380 40.747
16 5.8 o.s2 0.8380 47 568
015 2 3 4.8 0.57 0.8380 49.926 nla ola
016 2 711 4 5.8 0.s9 0.8380 so.7t2
tveraSeS 115.9 2.4 4.5 0.52 0.8380 47,320 nle nla
GP043AS-036878-RT- 1 579 Page 119 of 290
High Load Run rr4
LG.tion: Huntintton 2
Load (MW): 435
oare: 4l1ll2o24
StartTlm€: 16:37
EndTimc: 16t57
Probe / Gas Data
Adiusted Results
Va(avg): 46.77 ttlsec
qFw: 69,059,001 wct/hr
Gd:
Probe *r, R@: 0 deg@!
Probe f2 R@: 0 de8@s
Probe {1 Rs: {rJ degrecs
Prcb€ *2 RsLo: -1.8 dcgrr€s
B*r: 0.1234 %/100
Md: 30.24 lbllb-mole
M,: 2E.73 lb/lb",mole
Ph.: 23.87 ln Hg
Pt: -S.30 in HrO
P,: 23.48 ln Ht
96CO2i lLs
Ozt 60
%COr 0.0 %
81.8 %
Flow RATA Traverse Data
Point lD Probe lD
corrcqttd
StackT€mp YawAntle YawAntle P1-?2
(rl (der) q(der) (h Hrol
Unadiust.d Replacement Point Used # WAF
Axialveloctty Axlalvel@ity lot point!
V.(ft/secl V.ff/iec) WAF? Lr6edc"
o01 113 .3 -1.2 0.38 0.838 40,692
002 2 174 2.8 0.52 0.8380 47.597 n/a
003 114 4.8 0.58 0 a380 50.152
004 2 114 2 3.8 o5q 0.8380 50.648 n/a
005 2 113 2.4 0.38 0.8380 40.653
oo6 tl4 3 4.8 0.s2 0.8380 47.487
007 2 115 4A 0.56 0.8380 49.122 n/a
008 2 11S 2 3.8 o.s8 o 83ao 50.261
009 113 0 1.8 0.35 0.8380 39.042 n/a
010 2 113 2,8 0.53 0.8380 44.011 nla
011 tL4 2 3.8 0.55 0.8380 48.901
0L2 2 t74 7 3.4 0.61 0.8380 s1.500 nla
013 2 t13 2 3.8 0.40 0.a380 47.667
01!2 LL4 2 3.8 0.55 0.8380 48.901
015 2 714 4.8 0.58 0.8380 50.152
016 2 L4 !5.8 0.60 o.83ao s0.926
rverates 113.8 1.8 3.5 0.52 0,8380 47.245 nla nla
GP043AS-036878-RT- 1 579 Page 120 of 290
High Load Run #5
Locatloni Hlntinlton 2
Load (Mwl: 436
Date: 411,/2024
Stan Imer 17:10
EndTlme: 17:30
Probe / Gas Data
Prcbe 11 i@l 0 detrect
Prcbe *2 &e: 0 degees
Prcbc *1 Rs: .01 detrees
Prcb! i:l Rsro; -13 d€gr.es
B*, ________9:1391 %/1m
Md: :Ir.24 lb/lh,mole
M,: 28.70 lb/lb-mol€
Phr: 23,t7 In Hg
Pr: .5.30 ln HrO
P,: 23.48 ln Ht
COri ,'2.5
%O,t 6.0 %
96CO: 0.0 9(
81.S %
Flow RATA Traverse Data
Polnt lO Probe lO
CoJrcctld
StackTcmp YawArlle YawAntle P1-P2
(F) {dql O(drsl (ln H,ol
Unad.iusted R.placrmrnt Point Us.d # WAF
Ai.l Ve lcity Axial Vclo.lty for Pointt
v.lftlEc) v.(ft/secl wAF? usedc-
001 114 -4 -2.2 0,37 0.838 40.192 nla
002 115 -2 -o.2 0.so o.a3ao 46_797
m3 tt7 3 4.8 0.57 0.8380 49.877 nla nla
004 7L7 4 5.8 0.s9 0.8380 so.662
00s 7 11S 4 o.37 0.E380 40.115
006 7L7 3 4.8 0.54 0.8380 1t8.547 n/a
007 717 4 5.8 0.s9 0.8380 s0.662
oo8 117 4 0.60 0.8380 51.090
@9 115 2 3.8 0,37 0.8380 40.168 nla n/a
010 1t4 4 5.8 0.53 0.8380 47.Aq7
011 2 11S 3 A o57 o a3ao 49 790
o12 115 4 5.8 0.59 0.8380 50.574 n/a n/a
o1a 114 2 3.8 0.38 0.8380 40.672
014 11S 0 1.8 0.s5 o.8380 49.0S7
01s 11S 6.8 0.55 0.8380 49.117 n/a
o16 115 5 6.8 0.61 0.8380 s1.326 nla
lverales 115.4 2.5 4.3 0.52 0.8380 47.247 nla nla
GP043AS-036878-RT- 1 579 Page 121 of 290
High Load Run #6
Lqtlon: Huntintton 2
Load (MW): 436
Datei 4l7tl2024
StaftTlme: l7{A
Endllme: 18:04
Probe / Gas Data
Probe f1 RM: 0 degrei
P.obe f2 Rrm: 0 degrees
Probe f1 Rs@: -Ol detreer
Prcbe #2 Rno: -1.8 d€tre.s
8',: 0.1252 %/ltx)
Md: 30.24 lbllbmole
M,: 2E.70 lb/lb.mole
P6r:_4gln Hr
P.: -5.30 in H2O
P,: B.iA ln Hg
'kGozt 12.5 *
%Or: 6.0 %
%COt 0.0 %
%
Flow RATA Traverse Data
Point lO Prcb€ lo
Corractad
Stack1emp YawAngle YawAryle Pl-Pz
(F) (der) a,(dee) (lh Hro)
Unadiusted Replaccment Pointurcd ,WAF
Axial Velctty Axial Velo.itv for Polnrs
V.(ft/sec) V.(ftlse) WAF? Uredq
001 t4 ,1 o.8 0.33 0.838 ,7.9A1
002 \6 6.8 0.56 0.83&)49.770 n/a
m?16 4.6 0.59 0.a380 50.700
004 16 4 5_8 0_50 0.8380 51.046
005 1S 4 5.8 0.35 0.8380 3a.953
oo5 7 4.E 0.s7 o 4380 49.477
007 7 3 4_8 o.sa 0.8380 50.313
008 16 4 5.8 0.50 0.8380 I 046
ms 1S 4.8 o.37 o.83ao 40.115
010 16 2 3.8 0.55 0.8380 49.015
011 5 6.8 0.59 0.8380 50 s6s
o!2 Lrl 4 5.8 0.60 0.8380 51.090
013 l5 3.8 0.39 0,8380 41.239
014 7 4 5.8 0.s5 0.8380 48.915
015 7 2 3.8 o\7 0.8380 49.942
016 t1 4,8 0.62 0.8380 s2.019
verages 115.1 3.1 4.9 0.53 0.8380 17.627 nla nla
GP043AS-036878-RT-1579 Page t22 of 290
Hith load Run f7
Location: Huntintton 2
Load (Mw): 434
Date: 4ltll2o21
StartTlm.: 18:17
Endlim.i L8t37
Probe / Gas Data
Prcbc ft RDor 0 detre€r
P6bef2R&o: 0 degrees
Probe 11 &6: -{rl degrees
Prcbe 12 RsLo: .13 dett*s
8.,: o1267 %ll0/J
Md: t0.24 lb/lEmole
M,: 28.69 lbllb-mole
Pbr:-3lginHs
Pr: -5.:}0 ln H2O
Pt: 23.'18 ln Hg
%C.Or, l2.5
"4%Or: 5.0 %
%CO: 0.0 X
Flow RATA Traverse Data
Polntlo PrcbelD StackT€mp
(Fl
CorGCted
YawAnde Y.wAntle Pl.?2
lded (Llded (ln H,ol c
Unadrustcd Replaem.nt Pointuscd *WAF
Arhlvelo.lty A{alvelocity for Points
V-(ft/secl V-lft/ssl WAF? Used
001 113 -2 -o.2 0.35 0.838 39.089
oo2 11t -)4.2 7 0.8380 49.927
003 t14 1 2.8 o.37 0.8380 49.868 n/a
004 174 2 3.8 0.58 0.8380 50.2S3
ms 115 3.8 0.36 0.8380 39.626 nla
006 115 3 4.8 0.55 0.8380 48.915 nla nla
oo'l 114 0 1.8 0.s8 0-8380 s0.33s
008 114 4 5.8 0.58 0.8380 50.106 nla
009 115 0 1.8 0.37 0.8380 40.247 nla
010 114 3 4.4 0_s4 o.83m a8.476
011 115 1 2.4 0.57 0.8380 49.9L2 a/a
012 116 3 4.8 0.61 o.8380 51.558
013 115 3 4.8 0.41 o.8380 42.233
014 116 ?.4 os7 o.8?ao 49 cos
015 116 3 4.4 0.58 0.8380 50.274 nla
016 115 2 3.8 0.50 o-8380 51.201
veraSes 114.E 1.6 3.4 0.52 0.8380 47,6L7 nla nla
GP043AS-036878-RT-1579 Page 123 of 290
High Load Run #8
tMtloni Huntington 2
Load (MW): '(l4Datei 4il712024
St.rt Timer 19:01
EndTimer 19.21
Probe / Gas Data
Prob€ *1 R^s: 0 detr.€s
Pobe #2 R^m: 0 detrces
Probc #1 RM: {l deg@s
Prcbe #2 RsLo: -1J degr.cs
B*,: 0,1315 %/1(x,
Md: 30.24 lb/lb,mole
M.: 28.63 lb/lb-mole
Pb,: 23.E7 ln Ht
Pr: -5.30 ln HzO
P.:_4qlnHr
eACO2t I2.S %
%Or: 6.0 t6
',6COt 0.0 %
81.5 96
Flow RATA Traverse Data
Polnt lD Probe lD Stack Temp
{r}
Corrrcted
YewAngle YawAntle P1-P2
lder) Q (des) fin Hrol q
Unadiurtcd Replacement Point Used ,WAF
Axlal Velclty Axi.l Vclslty for Polnts
V,(ft/ses) V,(ft/secl WAF? Us€d
001 L74 1 2.8 0.39 0.838 lt 2s)nla
002 115 I 2.4 0.ss 0.8380 49.078
003 2 116 4.8 0.56 0.8380 49.451
o04 tL7 3 4.8 0.58 0.8380 50.370
005 116 3 4-8 o37 0.8380 40.195
005 2 117 2 3.8 0.55 0.8380 49.114 nla
o07 2 7t7 2 3.8 0.s6 0.8380 49.559
008 2 117 5.8 0.58 0.8380 50.191 nla
009 t15 1 2.8 0.38 0.8380 N.194 nla
010 115 2 3.8 0.53 0.8380 48.129
011 2 t15 3.8 0.s1 0.8380 49 955
012 2 t77 3 4.8 0.59 0.8380 s0.802
013 2 115 3 48 0.3s 0.8380 39.060
014 116 3 4.8 0.55 0.8380 a9 007 nla
015 2 r!7 2 3.8 0.s6 o.8380 49.559
016 2 t7)0.59 0.8380 s0.869lverages 115.1 2,4 4.2 0.52 o.8380 47.r39 nla nla
GP043AS-036878-RT- 1 5 79 Page 124 of 290
P@b€ *l RM:
Probe f2 R^m:
P.obe tl &6:
Prcbe *2 RsLo:
-------------.lL deSEes
0 drgres
{lJ detrces
-lJ dGtrc.s
8",: 0.1262 x/100
Mdr :D,A lbllb.mole
M,: 28.69 lb/lb-mle
P!.,:-----:4qin Ht
P.: -5.30 ln HrO
P.: 23./8 ln Ht
%cor: l2.5 96
Ori 6.0 %
COt 0.O %
High toad Run #9
L@tlon: Huntln$on 2
load (MW): 'tjrsDate: 411u2024
StaftTlmo: 19:33
End Tlme: 19i53
Probe / Gas Data
Unadiusted Results
iavgl: 47,56 tttsec
Qsw: 7O,128,225 wscllhr
Flow RATA Traverse Data
Point lO Probe lO
Crtreded
Sta.kTemp YawAngl€ YewAngle Pl-P2
(Fl ldesl Olded (ln H,ol
Unadlust€d Rcplaement Polntuicd #WAF
Axial Velocfty Axlal Velocity lo. Points
V. lftl3ecl v. lltlsecl wAF? Uredc
001 2 116 0 1.8 o.11 0.838 40.272
002 11S 3 4-a o.54 o 4380 8_461
003 2 115 4.8 0.55 0.8380 49.352
004 2 115 2 3.8 0.59 0.8380 so.724
ms 174 4 5a 0.35 0_83m 39.472
006 I 115 2 3.8 0.57 0.8380 49.a57
007 2 115 2 3.8 o.s1 0.8380 49.457
ooa 2 115 4 5.E 0.59 0.8380 50.575 nla nla
009 2 113 2 3.8 0.38 0.8380 40.637 nla nla
010 2 114 I o.8 o.55 o.ct80 4S.O{
011 2 114 4.8 0.59 0.8380 50.513
o12 2 115 2 3.8 0.59 0.8380 s0.724
^la013211434.8 0.36 0.8380 39.s36
014 114 4 58 o57 o R?ao 69 657
015 z 115 3 4.a 0.59 0.8380 50.657
2 115 2 3.8 0.61 0.8380 51.575 nla
lveraSes 114.5 2.4 4.2 0.52 0.8380 47.56t nla nla
GP043AS-036878-RT-1579 Page 125 of 290
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GP043AS-036878-RT- 1 579 Page 126 of 290
EPA Method 4 Datasheet
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GP043AS-036878-RT-1 579 Page L27 of 290
A{\M.,N I RUS t. EPA Method 2F Datasheet
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GP043AS-036878-RT- 1 s79 Radewed: FPtv}*c"Flb-
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GP043AS-036878-RT-1 579 Revlewed: FP Uf"S_f2eCo?U-
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'f- r t, Ll g.o.3 {-t lt{o a. t5
-5 ltf,r 6.SL-.f ,r 5 s o.ct
Stack Schamadc
Shd< Dlameter (D)=
Hnt, Oht. Fmm St!d( Wll
I
fi=
l=
2
3
4
5
6
t
N
Poil lD
A
B
c
D
G P043AS-036878-RT- 1 579 Revlewed: FPtv!ffi2ce$-
64\M ., N I RUS L EPA Method 2F Datasheet
ffiGodC eBLg78-Opcr&rld:L /AB l-
trhnc fa,'lIr'a^ro lrtom:ilrk hunrrc l'}ld:).3.s7 Nr.
burEa:U..-l:^-u-. U- J ttrllc Prrrsrn I'H0l:-5 ?ProbcCondlUon
ffi:({ - r, :,t 'l Pttba lD / AlLnrmnt t7 Btrl t'?. i
tun I C taelChrdtl'll0l:Blrl 6.a
itrilTlmG I 7 .tLl 5!oofin::I l(at-r H'oI$
I?ryrna Polnt lPort+olntl
SEdTcmj
frt
Yew'Antlc
ItDed
Vslodtf AP l'HrO
lPl-P2l
PhdraPfHpl
lFa.Pltl Eommcmr:
t l,'l -l o.3?I
-f uL s o.6 6
-3 ilL 3 o*l
-1 ltc ,l 6.60
2-tl5 Lr a,s t
..?n7 3 o.s7
-3 il7 3 6.Sy
-q ttc ,l o, to
3-,t{3 o.3 7
-J.tl (a 6.ftr
-3 t7 f o_ sj
-.f l)a,o.6o
It 3 .t o.3 q
.J Itz a,o.15
-3 l17 a o.s 7
-1 lt7 3 o. (t
Schcma0c
Dlameter(D)=
Polnt, Om. Fiomst dw.ll
1
{=
l=
2
3
4
5
6
t
N
Poil lO
A
B
c
D
GP043AS-036878-RT-1 579 Revlewed: FPMFa'E
r ,,Co?U-
ProlcctCodc b3c.*,+&Onnulrl:Av/as L-
CrhnE '^.i{it^.o lrrqnctlc Ptusne l' lld:23. t)L.
Llltlta:lJ,.-ll^l*,. D. -)$rdc Prcrurt: l'll'rol:-s.3 PruD!Godldon
DrE;r{-tt-r.q Pnobc lO lAlLnmant ,l-)Dq(rI fi.j
ilun I 7 LerkCh*tFll,Ol:Dl$(r.Q
il.rtrlm::lg t')lboT&na:t13"HrO(ral
EPA Method 2F Datasheet,6/i\ M1i...............N I Rg)l
Irenre Pdni (Portfoltttl
SleclTcmp
fn
Yew'Antle
fiDcd
VclodtVAP l"HrOl
lPl+21
Plrdr!P ('HrOl
lFa+sl Eommcnts
l- l t3 o(o.3t
-')tt .l -f o t7
-?,,et o3"
-tl ll9 2 o.sq
f-l tts a o.3c
-J llf,3 A-'.'
-3 r,{o o.5,
-q I lll Y o.5 7
t-il5 o 637
tq 3 t.\ 5.{
*3 iltr I o. s7
-.'|tlc 3 6.C tt-r ttf,3rA '4,*a.lt
4 IL ) 6.57
-3 ilc 3 o.sy
-q nL e a.Lo
Schcmetlc
Diameter(D)=
Polntl Dtst FromSLcIWe[
1
[=
l=
2
3
4
5
6
t
N
Port lO
A
B
c
D
GP043AS-036878-RT-1579 Reviewed: FPM CPMFEgEts4 oi 29-
PrchclGodc o3L2a8 Oocnbdsl:ALIAB f.m
dhlt ?tzi(i.- r o lrlomltrlc PlGrlun l'lltl:a3'. t )nr.
iourtp:il.r.$i..l-r- 0'f,$rdc Frrrnrn l'H'Ol:-r 3 ProbcCondlthn
h:L{ - rt: r9 fficlD/Alhnmcrt n-7 cGl$IZ,S
lunl v LakChr*l'Hrol:Btrl G.O
itrilrIru:l0lol loofincr Rat lt olxl
EPA lllethod 2F Dahsheet
64\ Mlll r,R9ft
Irerrcrrc Polnt lPoil-Polril
Sre*Tcm,
fFl
tbu'Ande
ItDcrl
vclodtyaP l'Hrol
lPr-P2l
PhdroP('ttol
lpa+sl Eommcnt$
ilLl o.31
-)Itl-o .s.t
-3 t a osc
-1 n1 ?o.5 y
a-tlL 3 o.3 -t
-)il7 a o.55
-_3 ltz )_o.s G
-.r lr1 .B o.5r
3-'rs I o.3 ?
-2 tr *(r 9'
-3 IL a o.d 7
-q t)3 o.r I
Ll-,ts 3 6.3 5-a itL JJ] 6g 6. rs
-3 t1 a o.5b
^4,il?&o _f1
Schama0c
Dlamater(D1=
Polntl Obt. FEttt S1lctwlll
1
[=
$=
2
3
4
5
6
Pon lO
A
B
c
D
G P043AS-036878-RT- 1 579 Revlewed: FPlv}ffi$8t,,--
holcstGodr bsLel*DporrErld:AK,/ln N.6
illcrt P^.:Iic- to lrrsnclrlc Prrcrurr l' Hd:)"..917 N..
loirre:U.,-l;^-L - -t)- )ItrdcPrarlrrcl'lG0l:- s.3 Prtob!Condnhr
DrD:Lt - tl:)q ProbalOrAlhnmsrt lt?B(LIXI t7. s
lunl n LcrkOrdl'ilOl:DI'.I L .c-t
ilrrtrlma:lqss ltooThne:t?5_1 Hro(rl
EPA i[ethod 2F Datasheet
64\ Sllry rRIqlh
Irrcrr: Polnt lPortPolntl
StectTrmp
loFl
YewA'ltlc
ItDetl
Vdod$lP('!lr0l
lPr.P2l
PhdrAP('Hpl
lFr+s1 EonrmantsE
IA o o.3 7
-),t _s 3 .)s{
-3 rrr 3 o.s e
-Ll u5 2 o.s j
, r.f (,6.3 C
-:.il.s a.o. s7
-3 ,rs a o. d7
-9 ils t't o.5 ?
3-lrl a-o.3 Y
-:lt .l a.ss
-3 ril 3 d. sq
-q ,rs a o.s1
tl-,lt.l 3 o.3L
-2 I l.l ."1 6..t 7
-3 ,,5 3 o. 11
-tl Ir.f -L o.6t
SchemaUc
Diameter(D)=
Pohtt Oht. From Stadr Wall
1
[=
S=
2
3
4
5
5
Porl lO
A
B
c
D
GP043AS-036878-RT- 1 579 Reviewed: FPM'@,=6C"?Y_
Appendix A.3.2.3
Instrumental Test Method Data
l
PROJ{35E7E
P.clfiCorp
Hundnlts Unlt 2
4/l,,l2r'24
Runf I
St ttTlm 7*42
Stopnm $r19
2
15:32
15r52
t
16:05
16:25
4
L6i37
1.6t57
5
17:10
17:30
5
L7i4
18:04
7
18:17
18:37
8
19:01
19..21
9
19:33
19:53
EPAM.thodl-'[D.ta I 2 3 { S 6 7 I 9
Exh.u5tGasFlowR.tG(w5cffl)69,595,44868,272,97658,921,35869,o59,@168,926,49{
EPA Mcftod 3A,5C, 7E .nd 10 D.tt
CO, (t{w)
50, (ppmw)
Nq(ppmw)
No, (ppmw)
CO (ppmw)
Ma3. Emlarlon Ctlcul.Uom (U3ln8 EPA M.thod 191
lL,2
17.3
96.7
0.2
r.01.9
1
11.2
14.9
99.5
0.3
61.3
2
11.2
16.0
100.7
0.1
83.2
3
7r.2
15.2
100.8
o.2
77.0
4
17.2
t4.7
100.7
0.2
65.1
5
17.2
15.8
99.8
0.2
84.0
6
11.2
15.8
100.2
0.2
732.3
,
10.9 10.8
16.3 16.3
100.5 99.4
0.2 0.2
21.2.6 255.5
F" rsf/mmBtu
SO, (lb/mmBtu)
NOr (lb/mmBtu)
co (lblmmBtu)
soz {lblhr}
Nq (lblhr)
co (lb/hr)
200.0 1.69.2
803.8 811.1
515.5 304.1
182.6 185.9 188.7
831.3 827,5 823.8
658.2 1065.1 1289.3
1840
0.047
0.189
0.121
17.4
t6.7
192.8
0.041
0.195
0.o73
11.3
15.6
r77.?
0.044
0.197
0.105
1&t.6
828.6
447.7
0.041
0.198
0.092
174.7
831.0
386.8
0.040
0.198
0.078
168.9
828.4
326.O
0.043
0.196
0.100
182,3
826.5
423.7
11.3
16.5
189.5
0.(x4
99.9
424
0.19
87.8
440.9
0.101
0.043
0.197
0.158
0.046
0.203
o.262
o,u7
0.203
0.318
PlantGMSD.te I Z 3 l| S O t 8 9
Unit Lo.d (MW) 437 4,:t5 /*16 435 435 436 /r:]4 434 435
CO2(%w)
50, (ppmw)
5Or (lb/hr)
SO, (lb/mmBtu)
NO, (ppmvw)
No, (lb/hr)
NO, (lblmmBtu)
Co (ppmw)
co (b/h4
CO (lblmmBtu)
0.041 0.041
L24.9 227.3 267.3
GP043AS-036878-RT- 1579 Page 138 of 290
0.044 0.041 0.044
97.4 99.5 100.6
808.7 916.1 A27.3
0.184 0,189 0.19
111.9 62.4 90.1
r7.4 11 10.9
15.4 L1.7 17.2
186.8 199.9 204.t
0.043 0.045 0.u7
100.2 100.5 99.3
820.4 846.9 848.6
0.189 0.196 0.196
7t.4
15.7
190.4
11.4
15,7
179.5
100.8
830
0.191
79.6
11.4
15.6
177.6
100.3
422.3
0.19
69.3
345.9
0.08
565.2 317.7 451.4 39A.7
0.128 0.072 0.104 0.092
620.1 7137.7 1390.9
0.!14 0.262 0322
UTAH DEPARTMENT OF
ENVIRONMENTAL QUALITY
JUN - 4 2024
i __D]yE,oI oF ArR auALrrY
PROJ{r36878
PacifiCorp
Huntangton Unit 2
4ltLl2O24
40 CFR Part 75, Appendix A
56,5,6 Pollutant Stratificatlon Iest
Port Point
Stack Diameter: 323.0 "
Stratification Test Point 1: 14,2"
Stratification Test Point 2: 47,2'
Stratification Test Point 3: 95.6 "
Time Cor NO,
1
I
1
1
t
1
2
2
2
2
2
2
3
3
3
3
3
3
4
4
4
4
4
4
1 4l7L/2O24t4:42
I L4:43
2 t4:44
2 L4:45
3 t4:46
3 14:47
t 4l1tl2o24L4:52
1 14:53
2 14:34
2 14:55
3 14:56
I 14:57
L 4lLLl2024 15:03
1 15:04
2 15:05
2 15:06
3 15:07
3 15:08
I 4htl2o2415tL4
1 15:15
2 15:16
2 L5:L7
3 15:18
3 15:19
11.6 94.5
11.6 93.5
11.6 92.6
LL.4 92.L
7r.4 93.5
LL.4 93.6
t1.4 94.6
11.4 95.8
Lt.4 95.8
11.3 95.0
Ll.4 95.5
11.3 96.6
rt.z 97.4
tl.z 96.4
11.3 97.6
Lt.z 98.1
t]..z 98.1
11.5 96.9
11.3 96.5
11.3 95.8
11.3 95.5
11.3 95.2
11.3 95.6
11.3 9s.9
Mean
Max Deviation From Mean
Max Deviation (%!
Short Line?
Single Point?
11.3 95.5
0.3 3.5
2.2% 3,6%
OK OKoK ox
G P043AS-036878-RT- 1 579 Page 139 of 290
PROJ{36878
Pacl0corp
Huntin$on Unh 2
4h!2024
Test Run fl
StartTime 74:42
Run Length 24
Stop Time 15:19
Uncorrected Analyrer Data
PROJ{r36t78
P.cmcorp
Huntlndil Unlt 2
4lru2024
Trst Run *2
Stan Time 15132
Run LenSth 27
StopTime 15:52
Uncorected Analyzer Data
Mlnute
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
15
18
19
20
21
22
23
24
co. sor No. co Nor
Tim? w ppmw ppmw ppmw ppmw
74142 11.5 32.7 94.5 112.6 .0.4
14:4! 11.6 32.2 93.5 114.2 -0.2
74:44 11.5 31.4 92.6 134.0 -0.4
14:45 7r.4 30.0 92.1 1L7.5 0.1
L4146 11.3 30.0 93.5 237.2 0.2
!4t47 11.4 23.4 93.5 120.5 0.2
L4t52 ll.4 13,9 94.6 L07.4 0.1
14:53 11.4 73,7 95.8 161.3 0.3
14:54 11.3 13,5 95.8 190.0 0.2
14:55 LL.4 13,5 95.0 99.3 0.4
14:56 11.3 13.8 95.5 66.1 0.3
!4157 11.2 13.8 96.6 66.5 0.4
15:03 77.2 17.4 97.4 39.0 O.2
15:04 11.3 72.2 96.4 65.1 O.2
15:05 !7.2 12.5 97.6 58.1 O.4
15:06 rl.2 L2.6 98.1 L17.3 0.2
15:07 11.3 Lz.S 98.1 94.5 0.4
15:08 11.5 11.8 95.9 128.4 O.2
15.74 11.3 72.4 95.5 40.1 0.3
15:15 11.3 11.8 95.8 67.4 0.3
15:16 LL.1 10.5 95.5 55.1 0.2
15:17 11.3 72.5 95.2 90.5 0.1
15:18 17.2 13.5 95.6 77.5 0.2
15:19 11.3 13.5 95.9 48.8 0.3
@r so. No, co Nor
Tlme %w ppmw ppmw ppru pllmw
15:32 11.2 f5.7 99.9 64.2 o.2
15:33 L1.2 14.9 99.3 60.0 0.1
15:34 11.3 15.0 98.9 57.4 0.1
15135 71.2 75.2 98.5 43.5 0.5
15:36 11.2 15.3 97.5 35.3 O.2
75t37 71.2 15,2 97.3 39.8 0.3
15:38 11.3 15.1 96.1 56.3 0.2
15:39 11.3 15.0 95.9 69.1 0.4
15:40 11.3 14.8 96.0 73.2 0.2
15141 L7.2 74.a 96.5 54.2 0.3
LSt42 11.4 74.A 96.5 49.7 0.1
15143 11.4 14.9 96.8 69.1 0.1
L5:44 rL.4 14.9 97.3 69.5 O.2
15:45 11.3 14,5 97,4 45.4 0.4
15:46 1L.4 14.S 97.2 59.7 0.5
15i47 11.5 r3.7 98.4 54.6 o.4
15:/E 11.5 13.7 98.2 61.2 0.4
15:49 11.4 13.8 99.1 50.6 0.1
15:50 Lt.4 13.5 99.3 47.2 0.3
15:51 11.4 14.1 98.4 67.5 0.4
Mlnut.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
t7
18
19
20
c.
q
c..
Coreclcd AwEtc:
AreEte
c.m
q
C.,.
c.
c..
Corlct€d Awr.tel
11.3 t1.t 95.5 101.6 0.2
0.0 -0.2 -0.3 -0.5
0.0 {.1 -0.3 -1.5
0.0 4.2 .0.3 -1.1
9.0 26.7 151.0 153.1
9.0 26.5 150.1 150.7
9,0 26.6 150.6 1s1.9
8.9 26.9 152.3 151.8ffi
21 75152 1L.4 L4.L 97.6 130.4 0.2
4rc88. 11.3 14.6 97.7 60.2 0.3
0.0 -0.1 -0.3 -1,6
0.0 0.0 -0.3 -1.3
0.0 -0.1 {.3 -1.5
9.0 26.5 150.1 750.7
9.0 26.4 1.49.4 151.7
9.0 26.5 149.E 151.2
8.9 26.9 Ls2.3 1s1.8ffi
GP043AS-036878-RT- 1 5 79 Page 140 of 290
PROJ{'36t7E
P.clflCorp
Huntington Unit 2
4h7lN24
Test Run f3
StartTlme 16:05
Run Length 2!
StopTime 16:25
Uncorrected Analyzer Data
PROJ-{B6a7t
PacmColp
Huntlngton Unlt 2
4lttl2o24
Tcst Run rr4
StafrTime 76137
Run Length 21
StopTime L6,57
Minute
1
2
3
4
6
7
8
9
10
11
72
13
14
15
L6
L7
18
L9
20
2r
cor so2 No, co Nor
Tim Xw ppmw ppfrw ppmw ppmw
16:05 t!.2 15.9 98.8 67.7 0.1
16:06 11.3 15.6 98.1 59.3 o.2
76107 11.3 15.4 98.3 45.9 0.0
16:08 11.3 15.3 100.1 47.L O.2
15:09 11.3 15.4 100.3 50.8 0.2
16:10 11.3 15.9 100.6 70.9 0.1
15:11 11.3 15.9 100.9 106.0 0.0
16:12 11.3 76.2 99.0 74.o 0.1
15:13 11.3 16.3 98.9 98.3 0.1
16114 11.3 15.8 99.5 65.8 0.0
16:15 11.4 16.2 97.7 88.9 o.2
16116 11.3 15.0 9?.0 58.1 O.2
16:17 11.3 15.4 97.2 E8.9 0.1
16:18 11.4 15.6 97.3 155.7 0.2
16119 11.3 15.7 97.3 72.7 0.2
15:20 11.3 15.5 97.5 61.7 0.2
76:27 17.4 15.4 97.9 52.8 0.2
L5,22 11.3 L5.7 9a.4 69.4 O.2
L6123 11.3 15.3 98.8 156.9 0.3
L6:24 11.3 15.4 98.8 238.0 0.1
16:25 71.4 15.3 97.5 76.L 0.1
coz sor No, co Nor
Imc Xw ppmw ppmw pplru ppmw
16:37 11.3 15.9 102.0 73.2 0.2
16:38 LL,4 74.7 100.4 62.8 0.3
16:39 11.3 13.5 100.5 55.5 O.2
16:,+0 lr.4 13.9 99.2 60.1 0.0
16:41 11.4 14.6 98.8 69.9 0.1
16:42 17.4 14.8 98.1 74.0 0.1
16143 77.4 14.5 9A.4 $5.4 0.2
16144 11.4 14.5 98.4 64.4 0.4
16:45 L7.4 13.8 97.7 48.0 0.4
16:46 11.4 L2.6 97.0 50.1 0.3
16t47 11.3 14.4 97.0 65.9 0.3
16:48 11.3 15.3 98.3 50.3 0.4
16:49 1L.4 1S.7 96.9 1L5.4 0.2
1.6i50 11.3 15.5 98.4 87.9 0.1
16:51 11.3 15.1 99.0 48.9 0.3
76t52 11.3 15.4 97.6 58.2 0,3
15:53 11.3 75.7 97,6 105.E 0.5
16:54 71.2 15.2 98.5 59.6 0.3
15:55 11.3 15.5 96.2 108.8 0-1
16:56 11.3 15.6 99.5 85.7 0.0
16:57 1i..4 16.0 98.7 73.1 0.2
6
1
8
9
10
11
72
13
14
15
17
18
19
20
27
Arcrat!
Qr.
q
Cn p,"
c,
c..
Cor€ct€d Arcnt€i
11.3 rs.7 98.5 85.9 0.1
0.0 0.0 -0.3 -1.3
0.0 0.1 -0.3 -2.4
0.0 0.1 "{!.3 -1.9
9.0 26.4 149.4 15L.7
9.0 26.L 149.1 150.4
9.0 25.3 !t9.3 1Sr,.1
8.9 26.9 152.3 1s1.8@
Avcnt!
Co p,.
c.
c.
c..
Corectcd AGEte:
0.0 0.1 -0.3 -2.1
0.0 -0.1 -0.3 -1.9
0.0 0.0 {r.3 -2.2
9.0 26.7 149.7 150.4
9.1 26.5 148.9 151.2
9.1 26.3 149.0 !50.8
8.9 25.9 152.3 151.8ffi
GP043AS-036878-RT- 1 579 Page 141 of 290
PROJ{36t7t
Pa.lfiCorp
Huntlngton unh 2
4ill/2024
Test Run f5
StartTlme 77tLO
Run Length 2l
StopTime 7730
Uncorrected Analyzer Data
PROI{36478
Paciflcorp
Huntlngton Unit 2
4huzoa
TGst Run #6
StartTime l7/A
Run LenSth 2L
Stop Time 18:04
Uncorrected Analyzer Data
co2 sor Nq co No.
Mlnute Tlme Xw ppm pptlw ppmw ppmw
cor 50. No, co Noz
Tlme tw ppmw ppmw ppmw ppmw
L7:44 11.3 15.5 97.0 92.5 0.3
17.45 11.4 15.0 98.5 114.2 0.1
17:45 rL.4 16.3 98.3 L20.4 0.2
17147 11.3 15.9 100.6 74.8 0.4
17148 11.3 15.E 101.6 51.3 0.0
L7t49 11.3 16.4 707.7 77.7 0.1
17:50 11.2 16.1 101.3 49.3 0.2
L7t51 11,3 77,7 99.0 1M3 0.3
L7t52 11.3 L6.2 97.2 72.5 0.4
17t53 11.3 16.1 96.4 63.1 0.2
L7t54 L!.2 15.2 95.1 44.6 0.1
17t55 11.3 15.4 95.0 63.1 0.3
17:56 11.4 15.0 94.7 L26.4 0.1
L7157 11.3 15.2 95.0 157.5 0.5
17:58 11.5 15.6 94.3 89.3 0.0
17159 11.4 15.9 95.3 94.0 0.0
18100 11.3 14.8 95.8 51.8 0.4
18:01 11.3 L4.7 95.2 53.9 0.1
18:02 !7.2 13.6 97.2 32.8 0.3
18:03 11.3 13.8 96.1 83.2 0.3
18:04 11.4 14.3 95.8 80.6 0.1
1
2
3
4
5
6
7
9
10
11
72
13
t4
15
16
L7
18
19
z0
17;10 LL.2 15.8 100.4 52.0 0.3
17t77 11.3 15.4 98.7 50.0 0.1
77..L2 tt.2 15.4 98.6 49.8 0.2
17:73 Lr.2 15.0 98.5 40.t 0.2
77:74 L7.2 15.1 98.4 44.6 O.2
17:15 Lr.2 14.9 99.0 45.9 0.1
17t76 77.2 14.9 98.5 73.5 0.2
t7t77 L7.4 L4.7 98.5 74.A 0.2
17:18 11.4 14.1 99.5 59.8 O.2
17:19 t7.4 14.1 9t.4 92.8 0.2
17:20 11.4 14.7 97.7 81.2 0.1
L7t21 11.4 14.8 98.2 67.5 0.2
L7122 11.5 15.5 96.8 80.3 0.1
L7t2! 11.3 13.6 99.5 a7.7 0.2
L7t24 71..4 13.1 97.5 55.3 0.1
17t25 11.5 13.5 97.O 76.0 0.3
77..26 11.3 74.2 97.3 65.7 0.3
77127 11.3 14.1 97.4 49.7 o.3
77:28 11.4 74.3 98.1 iA.8 -O.2
77129 17.4 14.0 97.3 63.5 0.1
Minute
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
16
17
18
19
20
2721 17130 11.3 13.2 97.a 72.7 0.3
0.0 -0.1 -0.3 -1.9
0.0 -0.1 -0.1 -2.5
0.0 -0.1 -0.2 -2.2
9.1 26.5 148.9 75L.2
9.0 26.4 1/18.6 L49.4
9.1 26.5 r/l8.8 $03
8.9 26.9 152.3 151.8ffi
11.3 15.s 97.2 82.7 0.2
0.0 {.1 -0.1 -2.5
0.0 -0.1 -o.3 -1.5
0.0 .0.1 4.2 -2,O
9.0 26.4 148.6 149.4
9.0 26.3 148.3 152.5
9.0 26.4 1'1E.5 l!i1.0
8.9 76.9 752.3 151.8ffi
Co r.
AEntc
Qr.
q
c,
c..
Coredad Awatei
q
C,.
q
c."
Co.rected Av€rate:
GP043AS-036878-RT- 1 579 Page 142 of 290
PROJ.036818
P.ciflCorp
HontlrSton Unlt 2
4lt!2024
Test Run rT
sta.t Time
Run Lentth
Stop Time
L8..77
27
78:37
Data
PROJ.O36878
P.cificorp
Huntlntton Unit 2
4lt7l2024
Tcd Run f8
StartTime
Run Length
StopTime
LJncorreded Analyrer Dab
19r01
2l
19:21
Uncorected
10
L2
t4
cor sor No, co tor
Tim€ Xw ppmw ppmw ppmw ppmw
18:17 11.4 14.8 9E.1 82.8 O.2
18:18 11.4 15.2 97.2 119.6 0.2
18:19 11.3 15.1 97.3 106.2 0.1
18:20 11.3 74.9 97.3 68.3 0.1
78:2L 11.3 15.1 97.2 85.7 0.2
78122 11.3 15.4 97.0 94.1 0.1
1E:23 11.3 15.3 98.9 55.6 0.3
18:24 11.4 15.1 98.3 60.8 0.1
18:25 L7.4 15.8 97.4 65.3 O.2
18:26 11.3 16.5 98.5 53.6 O.2
18t27 L7.4 L6.2 98.1 68.9 0.0
18:28 11.3 16.0 99.8 63.4 -0.1
18129 11.3 15.5 100.0 5S.2 O.2
18:30 11.3 15.3 98.2 60.8 0.1
18:31 11.3 L5.2 96.4 81.4 0.3
18:32 11.3 14.5 95.5 732.2 0.0
18:33 LL.4 L5.2 95.8 170.4 0.3
18:34 11.5 15.6 95.5 263.8 0.3
18:35 tl.4 1S.8 98.3 277.2 O.4
18:36 11.6 15.8 96.9 336.1 0.1
0.0 -0.1 -0.4 -2.7
0,0 -{r.1 {r.4 -1.t
9.0 26.3 148.3 152.5
9.1 26.4 148.6 149.4
9.1 264 148.5 t5!-0
8.9 26.9 152.3 1s1.8@
€oz sor tllq co [oz
Tim. taw ppmw pFfiw ppmw ppmw
19:01 11.1 Lz.a 98.9 245.5 0.2
1902 11.0 L4.6 99.0 204.3 0.1
19:03 11.0 15.5 99.2 206.1 0.2
19:04 11.1 15.9 9a.2 269.3 0.2
19:05 11.0 16.1 100.2 2L2.9 0.3
19:05 11.0 16.5 100.3 168.9 0.3
19:07 11.0 16.1 99.9 155.1 0.4
19108 11.0 16.1 100.6 L29.3 0.1
19:09 10.9 16.3 101.3 125.8 0.2
19:10 11.0 16.0 98.4 119.5 -0.1
19:11 11.0 15.9 97.7 121.4 0.3
19:12 11.0 15,9 97.4 190.0 0.1
19:13 10.9 16.1 97.6 189.6 0.4
19114 11.0 L6.2 96.5 22a.9 0.2
19:15 11.0 16.2 97.0 194.4 0.4
19116 11.1 16.4 95.6 326.2 O.2
L9tl7 11.1 16.5 96.2 346.0 0.2
19:18 11.1 L6.7 96.9 203.2 O.2
19:19 11.0 16.0 96.4 L79.3 0.1
19:20 11.1 16.7 95.6 312.0 0.3
L9t27 11.1 16.8 96.0 274.6 0.3
Mirutc
1
2
3
4
5
5
7
8
I
10
11
L2
13
14
15
L6
L7
18
19
20
2L
t6
18
19
20
27 78137 11.6 16.4 96.6 M6.O 0.1
Are88. 11.4 15.5 C, .5 131.3 O,2
q,^ 0.0 -0.1 -0.3 -1.5
11.0 16.0 98.0 209.6 0.2
0.0 {.1 -0,4 -2.1
0.0 4.2 -0.3 -1.1
0.0 4.2 -{r.4 -1.6
9.1 26.4 14a.6 L49.4
9.0 26.4 148.8 L49.L
9.1 26,4 148.7 149.3
8.9 26.9 1s2.3 1s1.8@
c"
C, p.
c,
c^.
Corccted Avcnge:
AvaEgt
Co 0,"
q
C. p.
c.
c..
Corected AveEtc:
GP043AS-036878-RT- 1579 Page 143 of 290
I
PROI{:t6t7t
P.dfiCorp
Hundrl3totr Unft 2qfilmzr
T6t Run 19
StartTlmc 19133
Run Lcngth 27
Stoplime 19:53
Uncof €cted Amlytel Datr
cq soi ilq oo ilo,Mlnuta Tlira 96w ppmw ppmw ppm pgltw
1933 11.0 17.0 97.3 2s2.0 0.2
19:34 10.9 16.4 97,4 259.3 o.2
ilt:35 10.9 16.6 97.5 161.3 0.1
1$35 10.9 16.s *.2 236.6 0.0
19:37 10.9 '5,5 97.3 325.3 0.3
19:38 10.9 15.5 %.7 262.6 0.3
1939 10.9 L1.O 97.2 287.5 0.5
19:i{, 10.8 16.5 97,0 117.4 0.4
19:41. 10.8 7A,2 97.1 251.8 0.6
19t42 10.9 16.2 96.8 234.\ { 1
ls.Al 1G8 15.9 96.5 taLT 0.1
19:44 10.9 15.1 96.5 245.6 O.2
19145 10.9 16.1 95.9 254.8 0.2
19:45 10-9 15.2 96.5 289.3 0.2
L9A7 10.9 1s.8 97.2 268.E 0.1
19:48 10.9 14.6 96.8 304.1 0.1
19:49 10.9 11:1 97.4 2L7.6 0.2
l9:go I1.0 15.'l 97.o 213.4 0.1
19151 11.0 15.5 97.7 207.3 0.2
19:52 11.0 ls.t 95.8 2225 0.221 19:53 11.0 15.3 97.6 229.7 0.0
Arer.gr l0.g tco nn 2541 0.2
0,0 4.2 {3 -r.1
0.0 4.2 4.2 -0.5
0.0 4.2 {3 {,8
9.0 2s.4 1'8.8 149.1
9.1 26.5 148.9 152.3
9.1 25.5 ItltJ t5/,.'
8.9 25.9 152.3 151.8
CorertcdAsrq!: @
1
2
3
4
5
7
8
9
10
11
12
13
lil
15
l6
l7
18
19
20
Qr.
Qs
q
C, p-
c,
q..
GP043AS-036878-RT- 1 579 Page 144 of 290
Appendix A.4
Example Calculations
PROJ-036878
Huntindon 2
4lLt12024
Run f1 Sample Calculations
EPA Method 4: Determinatlon of Moisture Concentration ln Stack Gases
(40 CFR Part 60, App€ndix A-31
P-= Pu,+(AH/13.5)
= 23.87 + (L.8/13.61
= 24.00 ln. HB
T,=460+t-
= 460 + 73.2
=533 R
V,qd,= KrxVk
= 0.04706 x 126.5
= 5.95 scf (Eq.4-1)
VmGdt= KaxYxvmxPm
T.
= 17.64 x 0.997 x 50.358 x 24.00
39.87 dscf Gq. a-3)
V*"gn61 r V.6to1
= 5.95
5.95 + 39.87
= 0.130 (%/1001 (Eq.44)
B*lrtMl=lO(A-(8/lr+cr)
533
B*-
p(.b,
= to (3.10765 ru5o.rsl(s.r.8s.o[)
596.33
76.77
variable Value feftnttlon Unit of Measurement
23.87 ,arometric Pressure in. Hg
AH 1.8 )ressure Differential across Orifice in. H20
P-24.00 \bsolute Pressure at Gas Meter in.Hg
73.2 femperature at Gas Meter "F
T.533 \bsolute Temperature at Gas Meter
K1 0.o4706 :onveEion Factor ft3/mL
t26.5 /olume of Water Condensed c
s.95 /olume of Water condensed scl
K4 L7.64 lonstant 'R/in.Hg
0.9970 Vleter Calibration Fador Unitless
s0.358 /olume of Stack Gas Collected dcf
39.87 ;ample Gas Volume dscf
B"'0.130 ;tack Gas Moisture Content %/7OO
t5 115 ;tack Temperature
46.3 itack Temperature "c
P -5.30 itack Static Pressure in. HrO
23.48 \bsolute Stack Pressure in. Hg
Prt"lrt 596.33 \bsolute Stack Pressure mm Hg
A 8.10765 :onstant mm Hg
B 1750.286 :onstant mm H!
c 235 :onstant 'c
Bws (sat,ratea,o.t29 iaturated Stack Gas Moisture Content %l7oo
GP043AS-036878-RT-1579
= 0.r2e (%/1001
596.33
Page 146 of 290
Client
Source
Date
Run f
PROJ.036878
Huntington 2
4htl2024
1 @ High load
Variable Value )efinltion Unit of Measurement
%co2 12.5 :oncentration of Carbon Diox,de Drv Volume Percent (%vd)
%o,6 :oncentration of OxySen Dry Volume Percent (%vd)
Md 30.24 )rv Molecular Weisht ofthe Stack Gas lbllb-mole
B"'o.729 ;tack Gas Moisture Content %H2O / 7OO
28.66 \ctual Molecular Weitht ofthe Stack Gas lb/lb-mole
Pw 23.87 larometric Pressure in. Hg
P -5.30 ;tack Static Pressure in. H20
P 23.48 \bsolute Stack Pressure in. Hs
t.i 115 itack Temperature at Traverse Point i "t
T'i 575 \bsolute Stack Temperature at Traveree Point i "R
Kp 85.49 :onversion Factor (ft/sec) x v(((lbllb-moleXin.Hs))/(('Rl(in.H,o)))
Apr 0.41 )ifferential Pressure of Stack Gas at Traverse Point i in. H2O
co 0.838 titot Tube Calibration Coefficient Dimensionless
gv(l -3 vleasured Yaw Angle of Flow Velocity at Traverse Point i degrees
R..o -1.8 lotational Scribe Line Offset of Probe degrees
9vlll -L.2 :orrected Yaw Angle at Traverse Point i degrees
V"ro 42.390 ;tack Gas Axial Velocity at Traverse Point i ft/sec
47 _736 Werase Stack Gas Axial Velocitv Across All Traverse Points ft/sec
567.970 :ross-Sectional Ar€a of th€ Stack ft
Tro s28 itandard Absolute Temperature "R
Tsta,et 115.3 Werate Stack Temperature Across All Traverse Points 't
575.3 \verage Absolute Stack Temperature Across All Traverse Points .R
P*a 29.92 itandard Absolute Pressure in. Hg
WAF 0.99 /Vall Effects Factor from EPA Method 2H (1.0 if not used)Dimensionless
q*69,595,448 \verace Wet-Basis Volumefiic Stack Flow Rate Corrected to Standard Conditions wscf/hr
q*60,636,18s Verage Dry-Basis Volumetric Stack Flow Rate Corrected to Standard Conditions dscf/hr
G P043AS-036878-RT- 1 579 Page 147 of 29O
PnOJ.O35878: Hunfl ntlon 2
EPA Uethod 2G Surple CalcuLtlon3
nult It o Hlrft tm4 s.mpL pothr I (04/u/20241
Irrto r (0.it4 x 96cor) + (0.32 x %oJ + 0.28(10G%co2-%o2)
= (0.44 x 12.5) + (0.32 x 6l + 0.28(100-125{}
= 30.241b/b-moh
M.= Max(l-BJ+ (18.0x B*.)
= 30.24x (1 - 0.129) + (18.0 x 0.129)
= 2t.66lb/b-molc (Eq.2G-2)
P.= Pr",+(P/13.6)
= 23.87 + Gs.3/13.61
= Zl.il8 in, Ht
fr= 450+tj
= 460 +115
=575R
[Eq.2G-3)
(Eq.2c-5)
v.o =lgxCrx
= 85.49 x 0.84 x
= 42.iilXl ft/cec
x (cos8xn)
x (cos -1.21
(T.u x PJ
(Ts1*g; x P;6) xWAF
(528 x B./Al
(575 x 29.92) x0.99
(Eq.2G4)
(Eq.2G-9)
'qe=3600 x (V{4l) x {A) x
= 3600 x (47.736) x (s57.971 x
= 69,s9t+l8wscf/hr
q"= q.*r(r-Bsl
= 69,595,4118 x (1 - 0.1287)
= 60,636,185 &d/ht
(Ap)r x T"m
(P,x M")
G P04 3AS-036878-RT- 15 79 Page 148 of 290
Paclfrcorp
Huntlngon Unlt 2
4lLtl2o24
nun #1 Sampl€ Calcul.tioils
EPA M3thod 3A: Detcmln.don of OqlCn.hd Cr6on Dlolldc Conc€ntr.tlons ln Emllslons from St.tlonery Sourffi
(lnstrumental Analyue? Ptocedur€l
(to cFR Part 60, App.nduA-2l
CF= (C.vr - Co) x C..
(c. - c!)
= (11.3 - 0) x 8.92s
(e-0)
= 11.2!tutr (Eq.7E-sb)
V.d.bl.Valua ,etrnltion Unlt of Measurmrnt
cil 11.3 Verage Unadjusted Gas Concentration %w
c.0.0 WeraEe Prc/Post Zero Gas Response %vw
c,"8.9 :oncentration of Upscale calibmtion Gas %
c.9.0 werage PrdPost Upscale Gas Reponse Xw
q-11,.2 Nerage Gas Oncentrdtion Adiusted for Bias o/"w
GP043AS-036878-RT- 1 579 Page 149 of 290
Paciticorp
Huntintton Unit 2
4htlzoa
Run *1 Sample Calculations
EPA Method 6C: Determlnatlon of Sulfur Dloxide Emisslons from Statlonary Sources
(lnstrumental Analyzer Procedurel
(/t0 CFR Part 60, Appendix 44)
(c",s-q)xCma
(c. - co)
= 17.3 ppmw (Eq.7E-sb)
= 2.87E-05 lblscf
Enl..ao= (c*) (Fcl (100)
= 0.047|b/mmBtu
E;575.= (C,) (Q*,"r)
= (2.87E-05) (69,595,448)
= 2ilt.0lb/hr
(Eq. 19-7)
Varlabl€Valu€)ellnitlon Unlt of M€asurement
q,"t7.l Werage Unadjusted Gas Concentration ppmvw
co -o.2 \verage Pre/Post Zero Gas Response ppmvw
c-"26.9 :oncentration of Upscale Calibration Gas ppm
c-26.6 Werage Pre/Post Upscale Gas Reponse
C6as 17.3 Verage Gas Concentration Adiusted for Eias ppmvw
64.06 ilolecular Weight lb/lb-mole
385.3 385.3 /olume of One Pound of ldeal Gas at Standard Conditions scf/lb-mole
F 1840 Factor from EPA Method 19 scf/mmBtu
c*2.87E-06 )ollutant Concentration, Wet Basis pound/wet standard cubic foot
cor%w jL.2 :O, Concentration wet volume percent
Elb/mmBru o.o47 :-mission Rate Dounds Der million British thermal units
Q*ar 69,59s,448 Exhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
200.0 Emission Rate Pounds per hour
GP043AS-036878-RT-1 579 Page 150 of 290
PacifiCorp
HuntinSton Unit 2
4htl2o24
Run #1 Sample Calculations
EPA Method 7E: Determination of J{itrogen Oxides Emissions from Stationary Soures
(lnstrumental Analyzer Procedure)
(40 CFR Part 60, Appendix A.4l
%,=(Ca,!-ColxC."
(c. - co)
{95.50458 - C0.3)} x 152.3
(1s0.ss - (-0.3))
= 96.7 ppmw (Eq.7E-sb)
(cs",) (MW)
(101 (38s.3)
1.16E-{,5 lb/scf
E57..au=(c*) (F") (1oo)
(COr%w)
= 0.189|b/mmBtu
E66,= (c*) (Q6)
= (1.16E-05) (69,s95,448)
= 803.8 lblhr
(Eq. 19-7)
Variable Value Definitlon ljnit of Measurement
c",.95.5 qverase Unadiusted Gas Concentration
co -0.3 Average Pre/Post Zero Gas Response ppmvw
c."152.3 :oncentration of Upscale Calibration Gas ppm
c.150_6 ryerage Pre/Post Upscale Gas Reponse ppmw
cr",96.7 {verage Gas Concentration Adjusted for Bias ppmvw
MW 46.01 Molecular Weicht lb/lb-mole
385.3 385.3 y'olume of One Pound of ldeal Gas at Standard Conditions scf/lb-mole
F 1840 F Factor from EPA Method 19 scf/mmBtu
c*1.16E-05 Pollutant Concentration, Wet Basis pounds per standard cubic foot
CO2%w Lt.2 C02 Concentration wet volume percent
F,,,0.189 Emission Rate pounds per million British thermal units
Qqson 69,595,M8 Exhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
E u/n,803.8 Emisslon Rate pounds per hour
GP043AS-036878-RT- 1 579 Page 151 of 290
PaclfiCorp
Huntintton Unit 2
41tu2024
Run fl Sample Calculations
EPA Method 10: Oeterminatlon ofCarbon Monoxlde Emissions from Stationery Sources
(lnstrumental Analyzer Procedure)
(40 CFR Part 60, Appendix A{}
Cr.,= (C.", - Cd x C,,
(c- - c")
(101.603 - (-1.0511 x 151.8
(1s1.e - (-1.05))
= 101.9 ppmw (Eq. 7E-sb)
7.41E{5 lb/scf
Er/mmm=(cw) (Fc) (100)
(cO2%wl
(7.41E-06) (1840) (100)
lLt.2\
= 0.121|b/mmBtu
Erm,= (c*) (a**n)
= (7.418-06) (69,s9s,448)
= 51s.s lb/hr
(Eq. 19-7)
Variable Value ,eflnitlon Unit of Measurement
c",r 101.6 \verage Unadjusted Gas Concentration ppmw
co t.1 Verage Pre/Post Zero Gas Response ppmw
C."151.8 :oncentration of Upscale Calibration Gas ppm
c-151.9 Verase Pre/Post Upscale Gas Reponse ppmw
Cga.101.9 Verage Gas Concentration Adiusted for Eias ppmvw
MW 24.07 vlolecular Weight lbllb-mole
385.3 385.3 /olume of One Pound of ldeal Gas at Standard Conditions scf/lb-mole
Fc 1840 Factor from EPA Method 19 scf/mmBtu
c"7.41E-O6 )ollutant Concentration, Wet Basis pounds per standard cubic foot
COz%w L1,2 :O2 Concentration wet volume percent
Etb/hmst!o.t21 :mission Rate pounds per million British thermal units
Qry*rt 69,595,448 :xhaust Flow Rate (trom EPA Method 2F)wet standard cubic feet per hour
515.5 Emission Rate pounds per hour
GP043AS-036878-RT- 1 579 Page 152 of 290
P.clf,Corp
HuntlrEton Unit 2
4hLl2o,,-
Rel.tiye Accurecy Test Audit S.mple C.lculatlons
ilor (lb/mmBtul
Runf RM CEM
0.005 0.00003
0.006 0.00004
0.007 0.00005
0.007 0.00005 56=
0.008 0.00006
0.005 0.00004
0.008 0.00006
0.007 0.00005
0.007 0.00005
1
2
3
4
5
6
7
8
9
10
IL
72
0.189 0.184
0.195 0.189
o.r97 0.190
0.198 0.191
0.198 0.190
0.196 0.190
0.197 0.189
0.203 0.196
0.203 0.196
Average 0.197 0.191
sum nla nla
!um2 nle ala
0.@, o.(xxlos0.061 0.00042
0.q137 nla
= 00O1
CC=(h.mro) 56
Vn
= (2.306) (0.001)
3
= 0.001
m=JlE!99!-
1166y
RM
= o*ii;?'''
''oo,
= 3.aX
v.riab|!r
rdi 0.00042 ;um of the Squared Differences
t:dJ'0.0037 iquare ofthe Summed Differences
n 9 {umber ofTest Runs
sd 0.(x)1 itandard Deviation of Differences
to.ezs 2.305 f{alue from P52, Table 2-1
cc 0,001 1.5% Confi dence Coefficient
dt 0.007 \bsolute Averare Difference
lcct o_oo1 \bsolute Confi d€nc€ coefficient
RM o-197 \verale RM Value
RA 3.8%lelative Accurafl
GP043AS-036878-RT- 1 579 Page 153 of 290
I 10
Appendix B
Facility Process Data
Page 154 of 290G P043AS-036878-RT- 1 579
I r0
Appendix 8.1
Unit 1
. a,
| / ,r I t-ta r I .a - t
GP043AS-036878-RT- 1579 Page 155 of 290
Appendix 8.1.1
Low-Load Flow RATA
GP043AS-036878-RT- 1 579 Page 156 of 290
Average Data - Low Flow Run 1
P|ant: HUNTINGTON PI.ANT
lnterval: 1 Minute
Type: Block
Report Period: 0411012024 06:25 Through Ml10l2O24 06:43
Time Online Criteria: 1 minute(s)
Source
Paarder
(Unit)
04110124 06:25 23.796 9.9 ,455,316.
UNlT1
E AKTKE5U
(rNHG)
coz
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KScFM)
STKTEMP
(DEGF)
UNI I L(JAL'
(MW)
37 188
109.219.8 37,586,394.0 860.3
Ullolu 06:27 23.794 9.8 37,705,254.8 863.5 109.52 189
Ul1U21 06:28 23.798 9.7 37,569,189.3 860.7 109.71 189
04110124 06:29 23.757 1899.6 36,980,311.3 u7.1
041'10124 06:30 23.797 36,639,862.2 838.9 109.35 189
04110124 06:31 23.797 9.6 30,.1:|4,570.0 834.0 109.27
04110121 06:32 23.757 30,375,596.9 832.5 109.17 189
Ullol:z4 06:33 23.798 9.6 36.739./159.1 840.5 r08.97
Ul10n4 06:34 23.757 36,718,0tt.4 108.80 t89
04110124 06:35 23.797 9.7 36,524,380.4 835.2 108.68
Oll1ol24 06:36 23.797 38,640,197.0 837.8 108.64 191
Ul1U24 06:37 23.797 9.8 36,663,615.0 838.3 108.63
Ul1U24 06:38 23.797 36,585,352.4 108.60 191
Ul1Ol21 06:39 23.75O 9.8 36,il7.O17.7 835.5 108.rt8
Ul1Ol24 06:40 23.796 1919.8 36,375,967.3 831.4 t08.38
Ul10l24 06:41 23.796 9.8 36,249,035.6 825.7 'l90
Ul10l24 0A:42 23.796 9.8 36,444,530.1 833.1 108.45 190
A nU21 06:43 25.797 9.8 36,475,169.9 190
Average
Minimum
Maximum
Summation
lnduded Data
P^i^1.
Total number of
n.l. hi^la
23.797
23.754
23.798
452.'.136
36,774,172.3
36,249,035.6
37,705,2*.8
698,709,273.5
841.3
8?8.7
863.5
15.984.4
108.91
108.35
109.71
2.069.30
9.7
9.6
9.9
184.9
190
188
19'l
3.604
19
19
19
ts
19
10
19
ts
19
't9
19
19
F = Unit Offline
E = Exceedance
I = lnvalld
M = Maintenance
Report Generate d: O4l tO / 24 07 :t6
GP043AS-035878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 157 of 290
Average Data - Low Flow Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ml 1 0 I 2024 06: 45 Throug h 041 1 0l 2024 6:59
Time Online Criteria: 1 minute(s)
Source
Peramet€r
r (Unit)
I
04110121 06:45
UNtTl
BAR,FRESS
(tNHG)
wz
(Pcr)
FL(JWS(jFTI
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNI I L9AU
(tlVV)
n.795 7 836.108.46 89
04t1U24 06:46 23.79 36,684,428.9 838.8 108.56 189
t. o4t1on4 06:47 23.793 oo 36,680,513.9 838.7 189
Oll1ol21 06:48 23.7U 36,889,l|,tl7.7 108.71 189
Ul10l24 06:49 23.7U 37,335,520.5
Ul1Ol24 06:50 23.7U 36,900,051.0 190
Ul10l24 06:51 23.755 36,633,746.5
Ul1Ol24 06:52 23.755 36,9/16,396.7 1W.74
Ullon1 06:53 23.754 36.973.901.9 108.57
O4l'l0l24 06:54 23.794 36,78'l,389.0 8,1.2
Ul10l24 06:55 36,703,603.8
Ul1Ol21 06:56 23.791 36,S4{t,617.1 108.69 189
Ul1U24 06:57 36,995,968.1 846.0 108.61 189
Ul10l24 06:58 23.795 37,210,031.3 108..t0 189
Ul1On4 06:59 37jy,779.8
AYErage
Minimum
Marmum
Summation
lncluded Data
P^lhta
Total number of
n.r. D^l^r.
23.794
23.753
23.755
356.914
36,895,00e.4
36,588,75.1.7
37,335,520.5
553,425,140.9
843.8
836.3
854.3
12,656.6
't08.67
108.46
109.04
r,630.10
9.8
9.7
9.9
146.4
189
189
'190
2,537
15
'15
15
t5
15
't5
15
15
15
15
15
'15
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 041 L0 / 24 07 :77
G P043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Contro!
Page 158 of 290
Average Data - Low Flow Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0411012024 07:01 Through Ml1Ol2024 07:13
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
04l1on4 07:0'l
UNITl
BARPRESS
(INHG)
co2
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STI(TEMP
OEGF)
UNITLOAO
(MW)
23.795 9.7
Oq1On4 O7:O2 9.7 36,938,604.8 190
Ul1On4 07:03 23.796 9.7 37,0,+5,437.0 108.46 189
O41On1 07:(X 36,762,207.O 189
Ul10l24 07:05 ?3.797 34,788,512.2
O41On1 07:06 37,185,394.4 189
04l1on4 o7:o7 23..794 37,352,288.1
Ul10l24 07:08 37,117,O*.2 189
Ul1Ol24 07:09 23.800 37,281,422.4
Ullonl 07:10 37,472,891.O 190
01110121 07:11 23.N2 37.447.614.7 &55.9 l90
O4l1Ol21 07:12 37,574,982.1 190
04110124 07:13 37.553.177.4 191
A\r€rage
Minimum
Maximum
Summation
lnduded Data
P^inla
Total number of
nd. P^int.
23.799
23.795
23.N2
309.382
37,159.997.3
36,560,378.2
37,574,582.1
48s,079,965.5
849.3
835.9
858.5
11 ,041.3
13
13
108.45
108.29
108.56
I,/109.79
13
13
9.8
9.7
9.8
't27.1
190
189
191
2,464
13
13
13
13
13
13
13
't3
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/ L0 124 07 :L7
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 159 of 290
Source
I
Average Data - Low Flow Run 4
Plant HUNTINGTON PUNT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1 0l 2024 07: 22 Throug h Mt 1 Ot 2024 07 :31
Time Online Criteria: 1 minute(s)
Paraneter
(Unit)
04t'tot21 07..22
UNITl
BAR,PRESS
(INHG)
(;(Jz
(Pcr)
FLOWSCFH
(scFH)
lirK|-L(JW
(KSCFM)
STKTEMP
(DEGF)
UNIILOAIJ
(tfW)
s.7 37,285,746-5
Ul10l21 07:23 37,&34,807.5 854.0 108.98 189
ut10t21 37,055,91 1.4
ut10n4
Ul1Ol21 07:26 36,566,7trt.8 835.6 108.17 .l9o
36,910,130.9UnOn4 07:27
0411U24 O7:2a 37.192.366.6
Un0l24 07:29 23.803 9.8 37,145,955.3 104.71
Ul1Ol24 07:30 36,990,532.2 108.90
O4l1Ol24 07:31 37,059,095.6
A\rerage
Minimum
Maximum
Summation
lnduded Data
P^inta
Totd number of
n.ta hi6ta
23.803
23.802
23.8(x
2*.O27
9.8
9.7
9.8
97.6
37,016,375.5
36,566,763.8
37,334,8e7.5
370,103,755.2
8/16.4
835.8
854.0
8,1183.9
108.76
108.37
109.09
'l,087.63
189
189
190
'l,894
10
10
10
10
10
t0
10
10
10
10
10
10
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 041 LO 124 08:14
GP043AS-036878-RT- 1579
C = Calibration
S = Substituted
T = Out Of Control
Page 160 of 290
Average Data - Low Flow Run 5
PIant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ml1Ol2O24 07:33 Through Ml1Ol2O24 07:42
Time Online Criteria: 1 minute(s)
Sorce
Paramder
(Unit)
Ul1Ol24 07:33 23.8Gi 19t9.8 37,194,435.8 850.7 108.91
UNlT1
EA'(P]IESI'
(NHG)
co2
(PCr)
FLOWSCFH
(scFH)
st Kt-Low
(KSCFM)
STKTEMP
(DEGF)
UNI I LOAIJ
(tfw)
04l10t24 07:34 23.803 1919.7 37.381t.872.9 855.2 100.06
ut10t21 9.7 37,68/+,208.3 190
Ul1on1 07:36 23.804 9.7 37.810.969.4 865.1 109.,l6 190
ul10nl 37,740.948.8 109.12
ut10n4 07:38 23.N2 9.7 37.609.581.2 860.7 1@.27 190
ul10n1 37,398,093.3 't00.r9
o4l10l24 O7i4O 23.805 851.49.7 37,203.330.6 109.29 189
o1t10124 07..11 37,169,987.6
04t10124 07:42 23.804 9.7 37,1'.t2,622.0 856.5 109.50 1S0
Awrage
Minimum
Maximum
Summatlon
lncluded Data
P^inle
Total number of
n{. hlnta
23.8(N
23.802
23.805
238.036
9.7
9.7
9.8
st.1
37,460,805.6
37,169,987.6
37,810,909.4
37[,608,055.9
857.2
850.7
865.1
8,571.9
1V9.22
108.91
109.50
1,@2.'t8
190
189
191
't,901
10
't0
10
10
10
10
10
10
10
10
10
10
F = Unit Offline
E = Exceedance
I = lnvalld
M = Maintenance
Report Generated:. O4/LO I 24 O8:t5
GP043AS-036878-RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 161 of 290
Average Data - Low Flow Run 6
Plant: HUNTINGTON PljNT
lnterval: 1 Minute
Type: Block
Report Period: 0411012024 07:44 Through04l1Ol2O24 O7:52
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul1U21 O7:4
UNITl
EARPRESS
(|NHG)
v(J:z
(PCT)
FLOWSUI.H
(scFH)
STKFLOW
(KSCFM)
UI KI EMP
(DEGF)
UNITLOAD
(Mw)
23.805 9.7 852.8 109.52 't9t
0d,l10l24 07145 37,385,472.6 855.7 109.39 190
O1l1Ol24 07:16 23.804 37,392,739.5 855.9 109./O
04110124 07:47 30,940,017.0 109.47
04110124 07:,tt}36,751,830.4 8/1.4 109.53 1S1
Ul1Ol24 O7i49 9.8 37,020,884.9 u7.5 109.50
Ul10l24 07:50 23.805 37,237,141.2 852.5 109.52
Ul'lol24 07:51 9.7 37,324,123.2
Ul1U24 07:52 37,66S,985.0 86.2.7 109.70 191
AveraOe
Minimum
Maximum
Summation
lncluded Data
P^inte
Total number of
nrrr 9^inra
23.805
23.804
23.806
214.242
s.7
s.7
9.8
47.7
37,219,W2.A
36,751,8[x).4
37,669,985.0
334,979,123.8
852.1
u1.4
862.7
7.668.8
109.51
109.39
'109.70
985.59
191
190
191
1,714
I
I
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d: 04/ tO I 24 08:75
GP043AS-036878-RT- 1 579
C = Calibration
S = Substltuted
T = Out Of Contrcl
Page 162 of 290
Average Data - Low Flow Run 7
Plant HUNTINGTON PISNT
Interval: 1 Minute
Type: Block
Report Period : Ul 1 Ol 2024 07: 54 Throu gh M I 1 0 I 2024 08:03
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
A4l1OlZ4 OTiU
UNITl
&qRPRESS
(INHG)
c02
(PCT)
FLQWSSFFI
(scFH)
STKFLOW
(KSCFM)
STKTEMP
OEGF)
UNITLOAO
(lvtw)
Ml1Ol21 07:55 37,432,495.2 857.8 110.O2
Ul1On4 07:56 9.7 37,415,782.6 857.3
Ul1Ol21 O7:57 37,224,750.O r09.s3
Ul10t24 07:58 9.7 37,198,916.5 852.2 109.93
Mn$nl 07:59 37,28/.,917.4 854.1
Ul1U21 08:00 9.7 37,137,1163.6 '109.73
Ul10l24 08:01 9.7 37,054,2rt0.6
Ul10t24 0a:02 9.7 37,01 1 ,606.6 u7.4 189
O1l1Ol21 08:03 9_7 37,187,317.5 851.8
A\rarage
Minimum
Marimum
Summation
lncluded Data
Pdnt.
Total number of
nalt P^inlc
23.805
23.803
23.807
238.052
37,233,1V3.7
37,0t 1,60€.6
37,132,1%.2
372,331,037.0
109.85
109.63
110.02
1,098.53
s.7
9.7
s.7
97.0
852.9
u7.1
857.8
8.528.8
190
'lE9
190
1,895
10
t0
10
10
10
t0
't0
l0
10
'10
10
t0
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d: 04 hO I 24 O8:L5
GP043AS-036878-RT- 1579
C = Calibration
S = Substituted
T = Out Of Control
Page 163 of 290
Average Data - Low Flow Run 8
Plant HUNTINGTON PljNT
lnterval:1 Minute
Type: Block
Report Period: Ul 1U2024 08: 05 Throu gh M I 1 0 I 2024 O8:1 1
Time Online Criteria: 1 minute(s)
Sourca
Parameter
(Unit)
Ul1U21 08:05
Ut1U21 08:06
UNTTl
BARPRESS
(INHG)
vtJz
(PCr)(scFH)
STKFLOW
(KSCFM)
U I KI EM'J
(DEGF)
UNITLOAD
(MW)
23.808 9.8 37,905,1a{t.2 109_92
ul1u24
ut1u21
37.673.697.1
,719,222.1
86/1.0 110.62 189
865.6 110.98 189
04110121 08:09 37,752,727,1 r 10.99 18S
Ullonl 08:10 37,589,601.0 I I 0.93
Ul1U24 08:11 37,A09,O24.7 110.93
Awrage
Mlnimum
Maximum
Summetion
lncluded Data
9^inta
Totd numbor of
n.h D^inra
23.808
23.AO7
23.809
166.654
9.7
9.7
s.8
68.1
1 10.64
109.92
110.S9
771.48
189
188
189
1,321
7
7
37,735,580.0
37,589,661.0
37,905,1r13.2
264,149,060.1
8{t5.5
862.6
868.4
6,058.5
F = Unit Offline
E = Erceedance
I = lnvalid
M = Maintenance
Report Generate d: 04/ L0 /24 O9:Ls
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 164 of 290
Average Data - Low Flow Run 9
Plant HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1 Al2O24 08: 1 3 Through Ml 1 0 I 2024 08:20
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul1U24 08:13 9.7 37,639,291.1 r I 0.79
UN]T1
BA,RPRESS
(INHG)
co2
(PCr)
FLOWSCFH
(scFH)
t' I KI.LOW
(KSCFM)
ti I KI EMP
(DEGF)
UNII LUAU
([rw)
Ut1Ol21 08:14 37,595,236.3 110.74
Ut1U24 08:15 37.348.015.6 857.0 110.89
Ul1U21 08:16 3t.823.512.8 110.96
Ul1024 08:17 36,638,009.r l1o.a2
o1,l10l21 08:18 36,994,003.0 w.7 110.76
Ul1U21 08:19 37,U3,692.7 110.70
Ul1Ol21 08:20 37,333,S47.4 1 10.83
Avorage
Minimum
Maximum
Summation
lncluded Data
P^inre
Total number of
nrt. 9^inlr
23.808
23.807
23.810
190.468
37,214,538.5
36,638,009.1
37,639,291.1
297,716,308.0
9.8
s.7
9.9
78.5
853.8
840.5
863.5
6.830.1
1 10.81
110.70
1 1 0.96
886.51
190
187
193
1,523
C = Calibration
S = Substituted
T = Out Of Contrcl
F = Unit Offline
E = Exceedance
! = lnvalld
M = Maintenance
Report Generated : o4l 7O I 24 O8:.21
GP043AS-035878-RT-1579 Page 165 of 290
I
Appendix B.1,2
High-Load Flow RATA
GP043AS-036878-RT- 1579 Page 166 of 290
Average Data - High Flow Run 1
P|ant: HUNTINGTON P!,ANT
lnterval: 1 Minute
Type: Block
Report Peri od : 04 I 30 I 2024 1 4: 46 Throu gh O4l 301 2024 1 5:22
Time Online Criteria: 1 minute(s)
Source
Ptramder
(Unit)
Ul3U24 14:45
UNITl
ttAt{PxE:'s
(INHG)
co2
(PCT)
FL(JWiJUFH
(scFH)
lj t K|-LUW
(KSCFM)
5t Kt EMt
(DEGF)
UNII L(JAU
(MW
111
01130121 11:17 ,to.7 80,554,832.3 1,871.6 't12.12 491
Ulfil24 14i48 23.564 10.7 80,969,406.5 1,8E2.4 't12.14
Ul3Ol24 14:49 23.563 10.7 80,744,599.7 1,877.5 112.50 495
Ulfil24 14:50 23.563 10.7 w,172,O31.7 1,868.8 't12.37
UlW24 14:51 2X.*2 10.7 80,298,832.9 1,806.3 1'12.20 495
04130124 14i52 23.560 10.7 80,067,337.9 't,860.9 fi2.14
Ul30l24 '14:53 23.561 10.7 79,532,485.8 1,848.5 112.15 493
04t?0t24 14:il 23.582 10.7 79,4t6,797.0 1,851.3 112.27
o4130t24 1/t:55 23.82 10.7 79,361,911.4 1.,x5.2 112.42 $7
04130124 14:56 10.0 79,073,637.7 1,8i!9.2 112.60 485
uB0n4 1*57 23.560 10.6 80.240.540.6 1.865.9 fi2.44 483
O4EO|24 1/t:58 81,504,355.0 1,895.7 1 12.53 82
041?0124 14:59 23.558 10.5 8r.210.499.4 1.890.1 112.91 42
Ul3Ol21 15:00 80,224,855.8 1,866.8 't12.81 &
Ul30lr24 15:01 23.558 10.5 80,376,354.8 1,869.9 I 12.68 485
Ul3Ol24 15:Oz 23.557 't0.6 80,792,370.2 1,875.2 112.51
O4/3O|21 15:03 23.556 490t0_6 81,16S,984.4 1,888.2 112.fi
UlNl24 15:04 23.556 10.6 81.446.481 .9 1,894.9 1 12.65
04lSOl24 15:05 23.558 10.6 81,166,020.6 1,888.0 112.57 492
Ul3ol24 15:06 23.557 10.6 80.843.441.1 1,880.'t 112.42
0{,l30,l2l 15:07 't0.6 80,331,800.2 1,8fj7.7 112.27 492
o{,l30l24 15:08 23.555 10.6 80,273,952.0 112-29
o4.l30l24 ,5:09 23.554 10.6 80,830,175.1 1,880.6 I 1 2.59 491
UlW24 15:10 23.554 10.8 81,280,422.5 1,592.4 1 I 2.9e
ut3u21 15..11 23.555 10.6 81.496.8&1.7 1,897.7 I 13.10 .l88
0d,ftOl24 15:12 23.554 81,404,381.3 1,8S6.2 113.28 488
04.130124 15:13 23.555 10.5 8't.258.337.1 1,892.9
Ul3U24 15:14 23.555 10.5 80,6€l!!,,107.1 1,879.1 113.24 487
Ul3Ol24 15:15 23.5U 10.5 79.915.867.6 1,861.6 t 13.31 485
G{,l3U24 15:16 23.555 10.5 79,992,301.8 1,863.4 1 1 3.33 4U
04l3ol24 15:17 10.5 80,884,919.7 1,82.2 112.74 €5
04.l?0124 15:18 23.552 10.5 80,484,525.3 1,473.2 f2.74 487
Ul30l24 15:19 23.551 10.5 80,9'16,rt8.1 1.883.1 1r 2.69
04l30t21 15:20 23.551 10.5 80,983,860.0 1,885.4 112.90 rl89
04,130124 15:21 81,028,920.1 1.886.2 112.8210.5
1,883.2 112.31
Page 167 of 290
ur*t21 F?unit offlifff3 80,979,98s.9 494
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: o4llo / 24 L5:24
GP043AS-036878-RT-1579
C = Calibration
S = Substituted
T = Out Of Control
L
Average Data - High FIow Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ul3Ol2024 1 4:46 Through 0413012024 15:22
Time Online Criteria: 1 minute(s)
A\rsrag6
Minimum
Marmum
Summetion
lnduded Data
P^lnfe
Total number of
nda P^ihle
23.557
23.551
23.567
871.627
80,610,844.5
79,073,ffi7.7
81,504,355.6
2,W2,W1,246.0
1,875.3
1,839.2
'1,897.7
09,385.8
37
37
112.63
111.99
't 13.36
4,167.36
10.6
10.5
10.7
391.9
it89
4A2
495
18,094
37
37
37
37
37
37
37
37
37
37
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d: OaBl / 24 15:24
G P043AS-035878- RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 168 of 290
Source
Ptrdil€ter
(Unit)
Ul30l24 15:38
Average Data - High Flow Run 2
Plant HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: C/'1301202415:38 Through o4,13012024 15:58
Time Online Criteria: 1 minutds)
80,023,009.3 ,8t 1.0
UNITl
EAITIJI(EST'
(NHG)
vQz
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKIEMP
(DEGF)
UNTTLOAD
(MW
't0.5 1',t2.13 452
Ul30l24 15i39 23.548 10.5 80.&o.929.9 1,875.3 112.20 't91
04l3U21 l5:4O 23.ilB so,252,412.1 1,866.2 112.11 490
c{,f3o,n4 15i41 23.543 10.6 80,861,711.9 1,882.0 112.54 ,188
04BOl2l 15:12 80,898,599.4 1,882.9 1'12.62 €8
04130124 15:43 23.W 10.6 80.840.400.8 1,880.9 1'.t2.49 486
ut30t24 15:44 80,452,471.2 1,871.8 112.47 M
04B0l24 15:rt5 23.U7 10.5 80,503,884.8 1,873.7 112.65 488
Ul3U24 15:48 23.546 10.5 80,619,520.0 1,875.6 11234
UBO|Z4 15:47 23.545 10.5 80,508.524.0 1,872.0 '112.05 /l83
Ul30l24 15:48 23.il3 80,658,045.9 1,875.9 112.12 /183
0{,B0n4 15:49 23.*3 10.4 81,026,448.2 1,885.2 112.36 483
04/3,0121 15:50 23.5/'l 80,565,751.9 1,874.9 112.43 la6
01130124 15:51 23.*2 10.4 80,597,967.3 1,875.1 f2.24 ,189
04/3,0f21 15:52 23.54{t 10.5 8r.968.086.7 1,900.7 'l'12.2s
O43Ol21 15:53 13..il1 10.5 42,$2,188.7 1,918.9 112.39 493
04130124 15:54 23.il3 10.5 81,890,759.3 '|,904.8
UlW24 15:55 23.il8 10.6 81.9:n.436.4 1,905.5 112.26 495
o4,lfilz1 15:56 23-5r1O 10.6 42327,715.5 1,915.7
ABol24 15:57 23.539 10.5 82.590.359.7 1,921.1 112.21 4U
or,/3,0l21 15:58 23.536 81,865,263.5 1,906.2 112.62
Average
Minimum
Modmum
Summation
lncluded Data
p^lnta
Total numbor ot
netr P^i^t.
23.!i4
23.s36
23.550
1U.125
81,1 18,340.3
80,023,009.3
82,590,359.7
1.703.485.1/16.9
1,887.3
1,801.6
1,921.4
39,632.3
112.35
1 12.05
112.85
2,359.39
10.5
10.4
10.0
220.7
€9
42
/t95
10,263
21
21
21
21
21
21
21
21
21
2'l
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Malntenance
Report Generatedj. O4l3Ol24 t6:Ot
G P043AS-0368 78- RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 169 of 290
Average Data - High Flow Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 04,1301202416:14 Through 04t30t2024 16:il
Time Online Criteria: 1 minute(s)
Sorlrce
Parameter
(Unit)
Ul30l24 '16:14
UNtTl
BARPRESS
(NHG)
coz
(PCr)
FL(JWI'GFH
(scFH)
STKFLOW
(KSCFM)
UI KI EMF
(DEGF)
UN]TLOAD
(MW
10.1 81,661,377.1 1 15.21
o4t30t24 l6:15 23.*3 10.4 81.797.708.0 1,905.6 1 13.10
04t30t24 16:16 23.540 10.4 81.836.049..1 1,906.3 112.97 489
ut30t21 23.538 10.5 82,270,79'1.2 1,916.6 t2.94 490
ut30t24 16:18 10.5 82.69't.802.3 1,926.6 113.01 492
0/,t30t24 45210.5'16:19 23.540 82,41 1,569.5 1.9't9.9 '113_O2
04,t30t24 23.U3 10.5 82,192,504.6 1,914.6 I 13.04
uBon4 lA:21 23.il1 10.5 81.939.859.1 1 13.19 492
uBon4 23.539 10.6 8't,8r!!3,902.2 1,907.8 113.39
ut30t24 l6:23 2?.537 10.5 81,073,384.4 1.905.1
492
191
o4t30121 23.ilO r0.5 8r,506,888.4 1,901.3 .t 13.75 489
04/3,0124 18:25 23.538 10.5 81,400,52/1.6 1,897.9 113.12 488
04nol24.
o4t3u24 1A:27
23.537 10.5
10.5
81,292,43.0
8r,289,457
1,893.5
1,893.'l 112.76
112.85 487
ANNP4 16:28 81,553,801.6 1,900.7 113.17 447
04130124 10.5 81,381,439.8 1,898.1 113.60 488
04130t24 16:30 23.536 80,960.257.9 1,887.6 1 13.36 488
utw24 16:31 23.537 10.5 81,019,848.5 1,888.7 113.30 lag
utnt24 16:32 23.537 81,317 ,225.7 1,896.4 113.52 490
04,130l?{16:33 10.5 81,649,023.2 1,904.3 113.55 191
0/,t3u?{16:34 23.536 81,667,268.2 1,904.6 113.53 493
Average
Minimum
Marimum
Summation
lncluded Data
P^inte
Total number of
ncle P^infa
23.538
23.535
23.ilg
494.308
10.5
10.4
10.6
220-3
490
486
/+93
10,281
81,683,196.7
80,960,257.9
82,691,802.3
1,715,U7,130.9
1,903.9
1,8117.0
1,926.6
39,981.3
113.26
112.74
113.75
2,378.37
21
21
21
21
21
21
2',1
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4130/24 76:37
G P04 3AS -036878-RT- 1 579
C = Calibration
S = Substltuted
T = Out Clf Control
Page 170 of 290
Average Data - High Flow Run 4
Plant HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: 041301202416:50 Through 0413012024 17:10
Time Online Criteria: 1 minute(s)
Source
Paramgter
(Unit)
04.13,0t24 16:50 23.530 10.5 80,772,105.2 1,884.5 1 13.03 452
UNITl
EAI.IPI{E!'5
(lNHG)
uoz
(PCT)
FLOvvS(.;FH
(scFH)
t'tKt-Low
(KScFM)
SIKIEMP
(DEGF)
UNI I LOAU
(lvfw)
ut30t24 16:51 23_529 10.6 80,974,836.0 1,888.2
utsu24 16:52 23.529 10.6 80,522,862.8 r,878.0 1 r3.38 483
0d,t30t24 16:53 23.525 80,784,619.4 1,883.3 1 13.15
0/,/3Ot24 23.524 10.8 80,000,927.3 1,865.9 1 13.36 $2
0/,E0t24 16:55 23.527 10.6 80.264.958.9 1.872.0
Mt30t24 23.528 10.6 80,510,298.5 1,877.1 '113.18 .ttl6
uBol24 16:57 23.52A 10.6 80,605,789.9 1,880.0 1 13.33
0/,t30l21 23.524 't0.6 81.083.966.5 1,892.0 1 13.60 'Ag
0/,i3Ot2{16:59 23.527 10.6 81,409,356.9 1,898.8 '113.36
04,t30t24 17:OO 23.s25 t0.6 80,&t5,643.0 1,884.6 1 13.00 495
0/,t30t24 17:O1 10_7 80,013,848.0 1,879.0 112.90 157
0/,t30t24 17:02 23.525 t0.7 80,w,712.1 r.878.3 1 1 3.06 499
o4t30t21 17..O3 80,272,84O.3 1,872.3 113.34 498
o4tsol24 17'.O4 23.524 10.8 79,612,654.e 1,857.0 113.32 157
o4130t24 17:05 23.523 10.8 75,218,e72.5 1,U7j 113.07
04t30t24 17:06 79,280,486.0 1,848.2 112.98 197
04t30t24 17:07 23.524 10.8 78.807.957.4 1,837.0 112.93
0/.l30t24 17:08 78,177,s91.6 1,822.1 112.8 494
w30124 17:09 23.521 t0.8 78.1 25.881.6 1.820.5 112.74 452
uBot24 17i10 23.523 78,263,900.3 1,823.8 112.75 489
Average
Minimum
Madmum
Summation
lncluded Data
O^lnla
Total number of
nrtr P^i6la
23.528
23.523
23.530
494.U2
21
21
80,03!t,995.7
78,125,881.6
81,lo9,356.9
1,680,713,909.5
1,806.2
1,820.5
1,898.8
39,'t89.7
113.17
112.75
113.63
2,376.57
10.7
10.5
10.8
224.2
491
82
499
10,315
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/ 3O / 24 L7 :L2
G P04 3AS-0368 78 - RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 171 of 290
Average Data - High Flow Run 5
Plant HUNT]NGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 04,1301202417:25 Through M13012024 17:45
Time Online Criteria: 1 minute(s)
Source
Paramst€r
(Unit)
04t30t21 17..25
UNITl
BARPRESS
(NHG)
co2
(Pcr)
FLUWI'UFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(oEGF)
UNI I L9AU
(MW)
23.51 I 't0.8 ,505.8 1,834.5 1 .l90
0/,t30t24 17:28 23.518 10.8 79,032,360.9 1,843.5 113.20 192
ul30t24 17i27 23.518 49310.9 79,067,272.8 1,843.9 1 1 3.06
04.l30t24 17:28 23.515 10.9 78,674,608.3 1,835.4 11?.20 490
uBon4 17:29 23.517 78,€0,970.6 1.829.7 .t89
ut30t21 23.516 10.9 79,447,10d..2 1,852.0 1 12.80 489
ut30t24 17:31 23.5't5 10.9 75,171,285.5 1.845.1 112.82 €9
04t30121 23.511 10.8 78,7s1,523.3 1,834.6 112.52 490
ul30t24 17:33 23.515 78,491,&7.8 1,828.6 112.38 492
o/,tsot24 10.923.514 78,726,081.8 1,8v.4 112.fi
o4t30n4 l7:35 23.513 49310.9 78,793,7A2.9 1,835.7 112.35
0/,t3/)n1 17:36 23.513 10.9 78,e63,342.0 1,432.1 112.20 493
u&ot24 17i?7 10.9 78,583,&i7.2 1,830.2 112.14 492
04BAt24 17i38 23.512 78,e75,323.4 |.832.4 11214 490
04not24 23.5r0 10.9 78,545,235.1 1,829.2 112.10 489
04130t24 17:40 23.509 10.9 79,908,617.2 1,863.4 112.81 490
o4t30t24 17..41 23.509 10.8 79,007,858.5 1,U2.5 112.U
0{.t30l24 17:42 10.8 78.952.570.5 1,840.8 112.74 493
utfit21 17:43 23.509 10.8 75,077,391.7 1,843.9 1',12.78 .193
ut30t24 17:44 10.8 78.850.468.4 1,&)9.9 1't 3.13 4U
ul30t24 17:45 23.509 78,794,898.5 1,839.3 '113.38 492
Average
Minimum
Maximum
Summation
lnduded Data
Painra
Total number of
natq P^inlc
23.513
23.509
23.519
493.716
78,868,068.9
78,430,970.0
79,908,617.2
1.854.225.45.4
1,838.6
1,828.6
1,863.4
38,611.1
112.75
112.10
113.57
2347.78
10.s
10.8
10.9
228.O
491
489
4U
t0,316
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04130/24 t7 :48
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page L72 of 290
Average Data - High Flow Run 6
Plant HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 0/,1301202417:58 Through Ml3Ol2O24 18:'18
Time Online Criteria: 1 minute(s)
Source
Paramder
(Unit)
04130124 17:58 23.513 10.8 76,791,839.8 '1,789.1 1',12.35
UNIT,I
tsAKlJKEl'U
(INHG)
vuz
(Pcr)
t'Luwsuin
(scFH)
STKFLOW
(KScFM)
STKTEMP
(DEGF)
UNITLOAD
(Mw)
0430n1 23.513 77,U2,659.7 1,795.0 1'.t2.41 481
04't30t21 t8:00 23.514 10.8 77,871,220.5 1,809.3 112.32 4n
0/,t30t24 23.511 78,176,556.0 1,820.7 112.19 474
ul30l21 18:02 23.513 10.8 78.880.586.8 1,836.3 I 11.95 .183
0/,t30t24 18:03 23.514 10.9 78,961,665.8 1,837.5 111.74
ut30t24 18:04 23.515 10.9 78,855,472.8 1.835.1 111.80 491
04t30t24 18:05 23.516 10.8 78,837,038.6 I,83/1.3 't11.70
0/,t30t24 18:06 23.516 10.9 75,419,?12.2 1,8/18.6 111.92 490
04/30124 23.516 10.9 79,443,638.0 1,849.3 111.96
ut30n4 18:08 23.517 49110.9 79,045,773.9 1,888.3 111.fi
0{,re,ot24 18:09 23.518 10.9 80,r33,056.3 1,862.0 496
0/,B0l24 18:10 23.517 10.9 81,438,4.t13.7 1,892.9 1 1 1.13 503
u$0124 18:11 23.517 10.8 82,049,639.9 1,908.9 fi1.47
o1tt0t21 18:'12 23.510 t0.8 81,639,598.4 I,901.4 fi2.24 506
o1t30t21 10.7 79,058,457.2 1,U2.3 112.6'.1 496
04tw24 18:14 23.516 10.6 2,136,148.9 1,798.8 112.98
0/,t30,t?1 18:15 23.516 10.5 76,791,309.2 1.791.1 1 13.10 474
0/,t3{],t24 18:10 23.516 10.4 74,225,8/,5.4 1,777.5 1 13.09
0/,l30t24 18:17 23.516 10.3 76,e02,337.4 1.786.8 1 13.14 466
o1130t21 l8:18 23.516 10.2 77,908,462.1 1,817.0 't 13.O3
Average
Minimum
Maximum
Summation
lncluded Oata
P.rinla
Total number of
nrta D^i^ta
23.515
23.513
23.518
493.825
78,671,7U.6
74,225,8/.9.4
82,049,639.9
1,652,107,056.6
1,832.0
1,777.9
1,908.9
38,172.6
112.18
110.99
I 13.14
2.355.86
10.7
10.2
10.9
225.5
486
463
508
10.212
21
2',1
21
21
21
2'l
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
! = lnvalid
M = Malntenance
R€port Generatedl. O4l3O 124 t8:2O
GP043AS-036878-RT-1579
C = Calibration
S = Substituted
T = Out Of Control
Page 173 of 290
Average Data - High Flow Run 7
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: 0413012024 1 8: 33 Through 04t30t2024 18:53
Time Online Criteria: 1 minute(s)
Source
Parffider
(Unit)
Ul3U24 18:33 46
UNITl
t,AKI'KES5
(rNHG)
coz
(PCT)
FLtJvvti(,;I.H
(scFH)
STKFLOW
(KSCFM)
5I KI EMP
(DEGF)
UNITLOAD
([fuv)
23.512 't0.0 1,82 16
c4,l30l24 18:34 23.512 10.0 80,400,750.2 1,874.4 112_72
ol,l30t24 18:35 23.512 10.0 80,490,647.4 1,875.9 112.55 4U
O1l30n4 18:36 23.511 10.1 81, I 95,705.2 1,892.2 112.50
Ul3Ol24 18:37 23.51 I 10.1 81,211,095.9 1,892.9 112.61 /163
10.1 80,149,442.5 1,8t8.0 112.72 480Ul3U24 18:38 23.51',|
0{,l3I)124 18:39 10.1 1,846.8 458
ut3u24 18:41 23.510 t0.0 79,026,208.4 1,863.4 112.70 456
0/,Eot21 23.510 80,032,561.4 'l,864.9 112.41
olmnl 18:,16 79,690.070.5
o4t3w24 10.1 79.598.920.6 1,855.5 112.@
a4i30t24 l8:.19 10.1 79,1 13,509.4 1,W.7 112.78 U
atfit21 18:50 23.510 10.1 79,(xX!,151.8 1,Uz.A 112.57
04,t3{),t24 18:51 23.509 10.1 79,6'14,6't r.6 1,85;t.7 I 1 3.16 483
utfit24 18:52 23.509 10.1 79.@2.482.5 't,858.4 113.45 82
ulw24 18:53 23.509 10.1 79,802,190.0 1.863.9 '11!.72 442
Av€rage
Minimum
Modmum
Summation
lnduded Data
P6inta
Total nuiflber of
nrt. P^inre
23.510
23.509
23.512
493.719
10.0
10.0
10.1
211.0
80,012,018.8
79,003,151.8
81,2r 1,095.9
'r,680,252,394.6
1,865.4
1,U2.8
1,892.9
39,173.9
112.72
112.10
113.72
2.%7.O7
462
456
465
9,697
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generated : 04/30 /24 L8:55
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page L74 of 290
Average Data - High Flow Run 8
Plant HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: Ul3Ol2O24 1 9: 09 Through 0413012024 19:29
Time Online Criteria: 1 minute(s)
Scurcr
Pardnder
(Unit)
0!,,l3rJ,1i24 19:09
UNITl
t'AKI'KEUU
flNHG)
vgz
(PCT)
FLQWSSFFI
(scFH)
STKFLOW
(KSCFM)
IiI KI EMP
(DEGF)
UNI I LgAU
(lvfw)
23.s09 't0.1 ,1 112.U 41
Ul30l24 19:10 23.508 10.1 79,579,878.4 1,856.1 I 1 2.89 460
Ml3Ol21 l9:ll 10.1 79,86it,6!1.3 't,863.9 1 13.26
04t30t21 19'.12 23.509 10.1 80,4r5,229.9 1,877.1 113.46 461
Uru124 19:13 10.1 80,013,398.6 |,881.9 113.12
c4'l3o124 19:14 23.509 10.1 80.375.874.3 't,876.8 1 13.56 464
MlNl21 19:15 23.509 10.0 80,690,709.3 1,8U.2 113.55
o4,l30l21 19:16 23.510 &710.0 80,065,657.8 1,867.6 113.01
0,,f30l24 19:'17 23.511 10.0 79.368.363.7 1,851.7 113.11
o4,l3u24 19:18 23.511 48010.0 78,95r,317.8 1,U2.1 1 13.15
o4.l3ol21 19:'19 23.511 10.0 78,558,414.6 1,832.4 113.m
04,130124 19:20 23.51 1 't0.0 78,51 1,780.0 1 ,831.0 112.92 458
uBonl 19..21 23.511 10.0 79,2W,120.3 1,&18.3 112.71
04130124 19122 23.510 45610.0 79,631,11 1.8 't,856.4 1 12.66
Olt30l21 19:23 79,412,606.0 1.852.1 112.89 rts8
04130124 19:24 23.510 46110.0 79,409,081.7 1,851.r1 112.72
O1l3Ol24 19:25 23.512 1,&4.610.1 79,357,215.9 112.26 465
Ul30l24 19.24 23.512 10.1 75,1r''5,200.1 1,849.8 112.m 466
04l3ol?4 19:27 23.512 10.'l 75,fiz,704.7 't,852.0 112.28 463
Ul3U24 19:28 23.511 45910.1 79,401,654.4 1,850.9 112.00
23.512 't0.1 79,W122.O 1,&50.2 112.90
Av€rage
Minimum
Marimum
Summation
lndudod Dala
pninlc
Total numb€r of
n.l. Prlinlc
23.5't0
23.508
23.512
493.714
10.1
10.0
10.1
211.1
79,*2.258.4
78,511,700.6
80,696,709.3
1,671,227,127.0
1,856.0
1,831.0
1,O8r'.z
38,976.9
112.91
112.OO
1 1 3.56
2,371.O5
1A1
458
468
9,684
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated:. Oal30 l2a L9:32
GP043AS-036878-RT- 1579
G = Galibration
S = Substituted
T = Out Of Control
Page 175 of 290
Average Data - High Flow Run 9
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ml3Ol2O24 1 9:44 Through 0413012024 20:04
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
UEU24 19:44
UNITl
tsA'(P]<ESS
(NHG)
co2
(PCr)
FLOWSCFH
(scFH)
S I KFLUW
(KSCFM)
STKTEMP
(DEGF)
UN]TLQAD
(tlVD
10.2 79,733,121.2 1,856.5 11
23.517 80,202,092.9 1,869.0 112.19 468
0,,n0l24 19:47 75,741,O23.2 1,857.4 112.19
Ul30l24 19:48 10.1 79.157.91 1.3 1.8.1!!.4
04l3t0l21 19:40 10.1 78,451,373.6 1,827.6 112.44
04,130124 19:50 23.517 10.1 78,068,570.5 1,832.6
0d.l30l24 19:51 23.517 't0.1 78,879,439.5 1,838.1 112.59 455
Mlfil21 19:52 23.517 10.1 79,770,589./+1,858.6 112.50
Ul3Ol21 '19:53 23.515 10.1 80,190,.115.1 1,ffi7.7 112.33 {s8
or'.E0l24 19:54 23.518 10.0 79,836,383.6 1,859.2 112.25
UEU24 19:55 23.514 10.0 79.607.940.2 1.8*.7 112.50
o4,f3on4 19:56 23.518 10.0 79,49,153.1 1,851.3 112.61
O4r3Oa4 19:57 10.0 79,323.623.8 1,847.9 112.45 4U
O4t3Ol24 19:58 23.518 10.0 79,178,221.5 112.38
0{,t30l24 19:59 10.1 75.141.41.4 '1,8113.'l 112.24
04t30124 20:00 23.517 10.1 79,384,197.3 1,849.0 112.v 458
UlNl2A 2O:O'l 23.517 10.1 78.582.049.5 112.19
04,l3o,124 20102 23.517 l0.t 78,564,3.19.8 1,829.0
O1l3Ol21 20:03 23.516 10.1 78.785.405.0 1,834.1 't12.O',1
O4l3Ol24 20:U 23.517 10.1 79,356,5S8.2 1,840.8 't11.U
Average
Minimum
Marimum
Summation
lndudod Data
P^l^1.
Total number of
ndr P^inte
23.517
23.516
23.518
rt93.860
79,350,714.6
78,451,373.6
80,281,062.5
I,860,365,005.9
1,848.'t
1,827.6
1,869.9
38,810.0
21
21
10.1
10.0
10.2
212.O
1',12.29
111.U
f2.41
2,358.19
/161
/155
470
9.686
21
21
21
21
21
21
21
21
21
?1
F = Unit Offline
E = Exceedance
| = lnvalid
M = Malntenance
Report Generate d: 04 I ?0 I 24 20:13
GP043AS-036878-RT-1579
G = Calibration
S = Substituted
T = Out Of Control
Page 176 of 290
Appendix 8.1.3
Gas RATAs
Average Data - Gases Run 1
PIat HUT.ITINGTON PLAi'ITlntflat 1 Minuto
TyF: Blek
Ropqi Period: 0,1./il0/202,1 1,1:,tg Thouqh 0,U30/2024 15:22
Tlmo Onlno Critorle: 1 mlnutc6)
Ud
s \@.e*"?i**--ffi;
W 14:$ &.0 qlA 1O.7 &-1 0G
& 1.D7-'
----;6--- ---a-?i;.i ...-
4nf .a
@ rt@
4,6,6----iEr
l:|ll!|iM it6 4.a o@
@ i5s st qfia toa 6t
ryI 15:e $1,7 O.lla loa 6I & 4m3
w 15111
aae4e
@ l5i5
0.6
0@a t5Ja
ory! 15:1!a,&0
w is:tluntrmttrl 0.e !0.5 6,7 1,16.2 @ ia, il - w----=---6i--4i--_ ffi
M r Mdmcnancc
T = Out Of Cont@l
' = surpct
U = St.nup
R.F^c.ndd: q/30/24
GP043AS-035878-RT-1579 Page 178 of 290
Average Data - Gases Run 1
Plant: HUNTINGTON PLANT
lntflal: 1 Minuts
TypE: Bl@k
Reporl Period: 04/30/2024 14:46 Thrcugh 04/3012024 15.22
]lme Onlino Cileria: I minut6(s)
Ary S,0
Mttu 15t5
ffi &aa
Stubn 13.62.5
lebdbtuE 37
T#IltlkdM
q0?r
qq
orE
t0.6
ros
10,7
st.t
31
@.3
27,4
141,6
t,&a
,f
it5
,tt,
16.5
1,14.5
s.3
i.1
t.119.9
37
& 4,14.1
42 4.6.6
s 4,413.2
1&& 175.9.'
G.O 0.65
3EO q@
4f ,9 0.69
la,g.g 3.r$
f.i{r o:€
1,Bta 0a1
1,2140 0.6f
4.37,4 a,977
3'37
37
a7 a7
37
3?
IT
F - Unit Omim
E = Exregdrnce
C= Crlibntion
S = Subitltuted
M = Malntenancc
T = Out Of Control
'=suspEt
U =Stanup
GP043AS-036878-RT- 1579 Page 179 of 290
8oa6
Pffi.
til
ffi€
Average Data - Gases Run 2
Plr* HUNIINGTON PI.ANT
lnt{ld: l lrhub
TyDC Eod(
R.gdt P.rlod: Ofiio,zo:rl ls:tt tlrmtri 0ar:l0l20iL l5:5t
TIrr Onha OIaL: t mhuta(r)
r.t.a
dt
,.taa H
rJti
rU
,.tG
r,!Gl
ww
ffimffogioaw&a4il..
w t6a a17 0 tqa
w tt{
,,w rs is m -i
@ lst a
o&r. rE
@6-.Utru
ruzi6
il7 offiw i*, a4 q(, liai------------ t- o@ a a.--*Tii"if*ffi rs xl7 oq m 4 ------iffi-e:@ffifrCwd{hMd@b/ffi
ha. gl
f,b lal
hGl
ffi !,St
tffhh 4
Iddcb a
qq
m
@
tg
ls
TM
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4
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21
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x
x
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a
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a
d
4
F.UilO|nil.
Erhrh00
CrCdbndn
s.gl! ltur.d
ll r if&taaso
T. On Ot Cortrelr.sul.Gt
U t$.ro,
iwrffio{lClza
GP043AS-036878-RT- 1579 Page 180 of 290
Average Data - Gases Run 3
PK HUl{NNGTol{ PIAiIT
lnt6rat 1 Minlila
TyDc Cod(
Roodt Pdtod: Ot,l0rzc2il lC:la nul0h O!r!Oiim24 la:3.tth. Orl!. cll.dl| mhui.6)
til
@ tt4
rq. mi
mrq
mg
ffi aato
6
g
ofi
la
rs
IU
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a7
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s
a,
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a,87
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21
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C. dbrdon
Sr$&dnttd
tltta.hs|m
r. Oot Ot Coitnl
' rlurpct
U r 3trtsp
iwrcn&OaDota
GP043AS-036878-RT-1s79 Page 181 of 290
Average Data - Gases Run 4
PIaI HUNTINGTON PI.ANT
lnirra: 1 ifnuta
Type Bck
R.po.t Pqld: Ol/:lly:aol4 lC:50 nmuln 04r90/:Xn4 1710Inr Onh. Cttr.b: 1 mhlt.6)
&u6
H
ffim
rr ru
c(n Er-E---------_iEi--
lr ---4ai-
* - A-rfm
MtS
rfuM
h r&
ffi !1.@
t#rb d
ldlrddE d
qfi7
GE
@*
to?
'G!@
w
g
s
il7
@
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a
t.45
g7
t.tG
x.s,
a\
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w
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40
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23ra
A
2l
s
frt
s
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d
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t.E
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21
u
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at
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C
1o.fl5
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(47,
4Bt
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4
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^
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A
n
a
d
I
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F . Un[ Oilh.
l.lDad.lta
C t Crlllrador
5. tubrtftit d
ilrradililm
TrorrtOlCo.rt d..glpGt
U r StrtuD
iFtcffi.ld: gAoha
GP043AS-036878-RT- 1579 Page 182 of 290
Average Data - Gases Run 5
Ph.HUNTMTON PIANT
lrlJrd: l ifnxJt
T}D. Bod(
R.ood Pdlod: 0/l/:10/2m4 1725 Thmush 0ilil0f2024 l7:$
Tlil.Onl| cltrb: I rtrutols)
t
i
loqa
ffi.
tH
ffitE
I
I
ha. lOEt
IfuA7
ffi lql
ffiUt
llffiilb a
Tdltrdh a
@
qt6
E
+fr
d
1
tu
tu
tr
N
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ru
t.a.r
x
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t,ru
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n
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lil.r
ta?
lrS
1S
a
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@
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&
16
a
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m
E
E
tt
at
flt
s
dal
a
a
g
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4e
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ma
a
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4
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a
I
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F.UnIqilm
Itha.lll..
Cr CaDrrdd
s.Sradhltd
l.rlrJnt.m
f r Or O, clinol
. r s0rDa.i
U r 3trtu,r.Frtlilat o{!ql2a
GP043AS-036878-RT- 1579 Pag€ 183 of 290
il
I
r
L
Average Data - Gases Run 6
PIrt HUMNNGTON PI.ANT
lnE\d: t ilinut
Typc Aod(
R.odt P.lod: Otlroz@it l7:$ Irol{h (x1302024 lllt
Tlna OnIr! C]f,dL: t mhutao)
Sorh
tn
w t75
6r qE -*
-6----------?
-re
I
ai, a- --- -----i;r
-.&Ere
rl
l
l
g-.g
-l, ---------48-
ks @!
IhS
5m Lli?
ffi l!,@
ffi&Hi A
rdlrtrb a
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6
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a.0
d
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6
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tG
t6
fls
2frA
a
A
o
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157,7
d
a
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ItEadro
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il . tirlrtarxca
t r orlt Ot Coitrel
'.turrt
U r 3trirpiFtffiorylo/il
GP043AS-035878-RT- 1579 Prgc 18a of 290
Average Data - Gases Run 7
Pbt HUMITNSTON PUNT
Irtjrrd: I Mind.
Typc Bock
n.pai Prbd: O,U3OZU2a ll:33 fhmuoh 0a60ra&l,l tl:53nn ollt[c,l.fi: I mhui.o)
h
FmLrW
@16
uLh
s
j
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uo
0.8
ut
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00
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al!
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ld
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tro
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914
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Eq
m
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x
u
ua
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a
t
5
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a.ilJ
n
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I
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a
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x
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I r Iraadro
Crmn[ei
3 rlsl*l&r.d
Ir]ham
TtqliOlOootrtt
t rsltG
UrSt rluotFtffioirryx
GP043AS-036878-RT- 1579 Page 185 of 290
I
l
li
l
h
rPffi
lrr{
rruz ru
Average Data - Gases Run 8
Pbt HUNNNGTON PIAiITlni$r* l Mind.
Typ.: Bock
R.poi P..lod: Orr$i:M4 le:og lho{h 04ll0r:m24 le:20
]'lmc Onlna Crtdlr: I mhut (r)
75 1.1S W
i,l&!un a-----_fi__--__-_--1_wa':'"@ aLiEr
M ttl!Lt
ooi i[ 0
-W
ar - ----ais -
UaTc6l
n
i,t4?.i
ff-ffi
lru aa
m re
.Fffi
s
llr
GI
fi1.7
q@
@
@l
dra
a
I
fi.4
ff
21
2t
1,123
LG
1,140
2tma
21
2l
6
H
E
B
lrat
Itil
lU
2/Ar
21
a
412
g
a.a
a.s
a
A
qc
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s
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6
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a,$l
4S
s.s!
x
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(t
00
tct
nt.t
2t
21
21
27
2l
21
2t
a
n
A
n
d
a
I
F'Unilmlm
I ':!aadsc.C. Ol0ndoo
S is{Ddftlbd
,{ttllail.m
T r Oct Ot cootrol
'rsuiri
U. StrtupiwrCnad q6q/24
GP043AS-036878-RT-1579 Page 185 of 290
i
l
I
Average Data - Gases Run 9
Pht HUNNMIToI,I PI.AT{T
lntJvrt 't Mlnd.
TF€i Bb(
Rcpqi P.tud: 0it/30r202it le:'tll rho{h 0{30/:m2,l 2O:O,l
TlnrortE gi.rlr: I mhld!6)
&
H
@ r'.4
I
)
l
a
w
na
*l
MO
m
ut
0rla
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IQ
az,0
7.4
aa
g
IU
t,l*a
LO4t
t.t4t
a,B.l
a
A
w
w
6
6
rts
lls
ta,
2,165
a
a
&
{tr
4
a.iit,
a
n
OC
Pq
qr@
1Gt
s
s.,s
G
5
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fi
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4
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1
21
a
a
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F.UntdlIm
E.Iroadro
C. OlD.rno.r
s.slailnlrd
mr',drt mor
r r Olt Ot Coat ol
t rtr?Gt
u rStiuo
iryrffis/!qlr4
GP043AS-036878-RT- 1579 Page 187 of 290
l
lrl
tl
0 ro
Appendix 8.2
Unit 2
, al
| / .^ r .-aa a a .a -
GP043AS-036878-RT- 1 579 Page 188 of 290
ro
Appendix 8.2.L
Low-Load Flow RATA
a; ,. .a "t,:
.lIr:, i,{T.,r. FtrffL l]: l!-i nil. .t.rrai rii
GP043AS-036878-RT- 1579 Page 189 of 290
Average Data - Low Flow Run 1
P|ant: HUNTINGTON PIANT
Interval: 1 Minute
Type: Block
Report Period: Ul11l2O24 1 1:50 Through 0411112024 11:59
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul11l24 11:50
UNIT2
BARPRESS
flNHG)
v(Jz
(PCT)
FLOWiiUFH
(scFH)
STKFLOW
(KscFM)
STKTEMP
OEGF)
UNI I LOAL)
ruw)
23.762 10.1 38,2U,217.0 5 08.61
04111124 11:51 23.761 10.1 38,242,693.2 108.23
Ul11l24 11:52 10.1 38,195,881.9 107.92 211
Ul11l24 11:53 10.1 37,929,902.6 867.2 107.68 210
Ul11l21 1l:il 10.1 37,/+57,087.3 204
Ul'11124 11:55 10.1 37,105,055.7 ,,4a.7 107.88
Ul11l21 '11:56 23.759 10.1 37,133,/163.5 849.0 107.66 203
Ul11l24 11:57 10.1 36,861,556.0 107.38
Ul11l24 11:58
ut't'|24 11:59
10.1 36,729,0€0.7
37
Average
Minimum
Ma)(imum
Summation
lnclud€d Data
Painta
Total numbor of
n4r hihrc
23.780
23.759
?3.7A2
237.597
10.1
10.1
10.1
t 0r.0
37,489,556.0
38,729,W.7
34,242,653.2
374,895,559.9
857.3
839.2
875.5
8,572.8
107.76
107.26
108.61
1,077.U
206
201
212
2,OU
10
10
10
t0
10
l0
10
10
10
t0
10
10
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated : 04/ ttl24 L2:78
G P043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 190 of 290
Source
Parameter
(Unit)
04t11124 't2'.O1
Average Data - Low Flow Run 2
Plant: HUNTINGTON PLANT
Interval: 1 Minute
Type: Block
Report Period: 041111202412:01 Through 0411112024 12:08
Time Online Criteria: 1 minute(s)
36,985,823.
UNIT2
BATTPIIEt'ti
(NHG)
co2
(PCr)
FLUWl'UI-FI
(scFH)
5I KFL(JW
(KSCFM)
STKTEMP
OEGF)
UNITLOAD
(MW)
10.844.8
04111124 12:02 10.1 36.973.799.1 107.37
o4t11t24 12'.03 10.1 36,978,485.1 8/,5.7 '107.76
Ul11l21 12:U 23.757 36.252.948.1 111.37 197
Ul11l24 12:05 10.o 35,690,351.1 1't 1.96 196
Vl11l24 12:06 23.755 35.605.632.9 820.4 111.97
ut11t21 12'.07 9_9 34,937,879.9 805.1 112.O'l
Ul11l24 12:Og 9.9 34.265.872.0 789.6 1 12.06
AvBrage
Minimum
Maximum
Summation
lncluded Data
P^i^la
Total number of
n.lr P^i^la
23.756
23.755
23.758
190.052
10.0
9.9
10.1
80.o
825.9
789.6
845.7
6,607.2
110.20
107.08
112.06
881.58
197
193
201
1,579
35,961,3/18.9
34,265,872.0
36,985,823.3
287,690,791.5
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4l LU24 12:19
GP043AS-036878-RT- 1 579
G = Galibration
S = Substituted
T = Out Of Control
Page 191 of 290
Source
Parameter
(Unit)
Ut11l24 12:10
Average Data - Low Flow Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peflod: 0/,1111202412:10 Through 04t1112024 12:18
Time Online Criteria: 1 minute(s)
10.0 34,703,610.7 798.9 111./16 .tgoUl11l24 12111 23.755
UNIT2
BARPRESS
(tNHG)
co2
(Pcr)
FLOWSSFH
(scFH)
STKFLOW
(KSCFM)
ST]CEMP
(DEGF)
UNI I L(JAU
(MW
23.755 10.0 1 788.0 1.49
Ul11l24 12:12 34,973.280.3 111.68
Ul11l24 12:13 23.755 10.1 34.582.,+68.4 111.86
Ul11l21 12:11 23.755 34,147,386.0 78ti.6 111.80 t8e
Ul1'1124 12:15 23.755 10.1 33.881..163.2 111.42 188
04111124 12:16 23.754 10.1 33,977.403.7
Ul'11124 12:17 23.753 t0.1 &t,957,325.0 781.5 111.2A 188
04111121 12:18 23.753 34,002.893.1 7A1.7 110.63 r89
A\rerage
Minimum
Maximum
Summalion
lnclud€d Data
D^i^|.
Total numb€r of
nalr 9aihlq
2?.7il
23.753
23.755
213.790
10.1
10.0
10.2
90.7
u,272,7fi.8
g!,881,4&i.2
34,073,280.3
308.454.649.5
789.0
780.2
805.4
7,101.1
111.4A
110.trt
't 1 1.86
1.003.16
189
187
190
1,700
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated : 0 4/ tL / 24 t2:79
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 192 of 290
Average Data - Low FIow Run 4
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od: Ul 1 1 I 2024 1 2: 28 Throu gh Ml 1 1 I 2024 12:36
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ut11l24 12:28
UNIT2
BARPRESS
flNHG)
c(Jz
(PCT)
FLUWSUFIl
(scFH)
ti I KFLUW
(KSCFM)
5I KI EM|J
OEGF)
UNITLOAO
0ifw)
10.4 34,507,753.0 7A7.O 106.03
Ul11l24 12:29 23.750 34,541,968.7 7e7.7
Ul11l24 12:30 23.749 34.379.385.4 783.5
Ut11l24 12:31 23.750 33,851,704.6
Ul11l24 12:32 23.750 33,545,130.5 105.24
Ul11n4 12:33 23.7fi 34,306,831.7 105.34
Ul11n4 12:U 23.745 34,861,131.5 798.1 108.15
Ul11l24 12:35 23.749 35,248,727.7 809.1 109.70
01l'11121 12:36 23.78 v,925,720.',|w2.'l 109.96
Average
Minimum
Maximum
Summatlon
lnduded Data
P^inta
Total number of
fldr P^lhte
23.715
23.718
23.7fi
zrs.tiqs
9
9
10.4
10.4
10.4
93.0
I
I
u,462,928.1
33,545,130.5
35,244,727.7
310,'168,353.2
757.1
7U.O
809.1
7,084.0
106.81
105.24
109.96
961.26
1S0
188
192
1,708
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d: O4l tL I 24 13 :L8
GP043AS-036878- RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 193 of 290
Average Data - Low Flow Run 5
Plant HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1 1 I 2024 1 2: 38 Through 041 1 1 I 2024 12: 45
Time Online Criteria: 1 minute(s)
Source
Pardneter
(Unit)
Ul11l24 12ifi
UNIT2
BARPRESS
(NHG)
co2
(PCr)
FL(JWSUI.,H
(scFH)
STKFLOW
(KSCFM)
l'I KI EMP
(DEGF)
UNITLOAD
(Mw)
23.747 10.4 y,629,871.0 110.35
Ul11124 12:39 10.3 34,846,381.3 110.62
Ul11l24 12:40 10.3 u,713,875.2 110.92 191
Ul11124 12:41 10.3 34,373,558.9 1',|1.O7 189
Un1n4 12:42 10.3 y,032,782.1 1',t1.11
Ul11l24 12:4 10.2 u,o21,u3.1 1't0.99
Ul11n4 12:44 23.75 u,426,112.6 1'to.88
Ul11l21 12:45 23.745 34,498,r93.4 110.91
A\r€rage
Minimum
Maximum
Summation
lncluded Data
P.inr.
Total number of
nrh 9^inla
2?.747
23.745
23.74
189.974
u,442,765.1
34,021,3.1,!i.1
34,846,381.3
275,5/.2,120.A
10.3
10.2
10.4
82.2
8
I
792.3
782.8
801.3
6,388.5
110.86
110.35
11',l.11
886.85
190
188
.t93
1,518
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 041 1,1/ 24 t3:L8
GP043AS-036878-RT- 1 579
G = Calibration
S = Substituted
T = Out Of Control
Page 194 of 290
Average Data - Low Flow Run 6
Plant: HUNTINGTON PIANT
Interval: 1 Minute
Type: Block
Report Period: Ul 1 1 12024 12:47 Through O4l 1 1 12024 12:55
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul11l24 12:47
UN]T2
EAKTKESU
(NHG)
vuz
(PCr)
FLUWtjUFH
(scFH)
U I KFLUW
(KSCFM)
l'I KI EMP
(DEGF)
UNI I L(JAU
(Mw)
23.744 3
Ul11l24 12148 23.74 34,889,466.9 802.7 1 10.89
Ul11l24 12:49 23.744 10.3 3/314,774.8 784.9
ut11l21 12'.fi 23.74 u,314,325.5
Ul11t24 12:51 23.743 34,576,986.0 789.2
0411'|121 12:52 23.714 u,592,714.2
Ul11l24 12:53 23.743 34,332,108.9
Ml11t21 '.tz..il 23.742 34,092,965.7 777.7 t91
Ul11l24 12:55 23.712 34,133,682.3
Awrege
Mlnimum
Ma)dmum
Summation
lncluded Oata
p^tnl.
Total number of
nrrr P^inta
23.743
23.712
23.744
213.690
10.3
10.2
10.3
92.6
34,450,925.4
34,092,965.7
34,889,466.9
310.058.329.0
787.8
777.7
802.7
7,0s0.3
107.38
105.88
1 1 1.03
966.38
192
190
193
1,724
F = Unit Offline
E = Exceedance
I = lnvalld
M = Malntenance
Report Generated I O4l Ll I 24 L3 tlg
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 195 of 290
Average Data - Low Flow Run 7
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 041111202412:57 Through Ml11l2O24 13:04
Time Online Criteria: 1 minute(s)
Source
Paraneter
(Unit)
ut11t24 12..57
UNIT2
BARPRESS
(INHG)
coz
(Pcr)
r-L(Jvv5Ur-H
(scFH)
ti I KFL9W
(KSCFM)
STrcTEMP
(DEGF)
UNITLOAD(rw
23.741 10.2 U.7'm.7 106.42
Ul11l24 12:58 23.742 10.1 34,309,259.2 106.32 189
Ul11l24 12:59 23.741 10.1 u,74,6it6.8
Ul1'1124 13:00 23.74',1 y,716,404..1 791.7
Ul11t21 13:01 23.740 34,780,58It.2 792.5 105.56 190
Ul'11124 13:02 34,949,979.3 796.9 105.68 ,t91
Ul'11124 13:03 23.739 34,806,444.1 t05.75
Ul11l24 13:(X 23.735 35.351.71 7.5
Av€rage
Minimum
Maximum
Surflnalion
lncluded Data
P^inre
Total numb$ of
nd. hi^ra
23.740
23.739
23.742
,89.923
10.2
10.1
10.2
81.3
I
I
753.1
780.7
811.3
6,341.6
106.36
105.s6
.109.32
850.89
190
189
191
1,518
34,739,194.9
34,194,493.0
35,351,717.5
277,913.559.5
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generated: 04/t7124 t3:L9
GP043AS-036878-RT-1579
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 196 of 290
Average Data - Low Flow Run I
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 041 1 1 I 2024 1 3: 06 Through O4l 1'l 12024 13: 1 1
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul11n1 13:06
UN]T2
EAII,I"KESti
(rNHG)
coz
(PCr)
FLOWSCFH
(scFH)
STKFLgW
(KSCFM)
STKTEMP
(DEGF)
UNI I LUAU
([fw)
10.1 35,1 18,723.0 807 10.32
Ul11l21 13:07 23.737 10.1 34,928,88t3.4 110.49
Un1n4 13:08 23.734 34,8.19,48:i.9 801.7 110.62
Ul11n1 13:m 23.735 11,810,565.6 80i.0
Ul11nl 13:10 23-73/35,00/t,647.9 1 10.83
Ul11nl 13:ll 23.7U 45,361,869.5 1't0.53
A\,6rage
Minimum
Madmum
Summation
lnclud€d Datia
Dninl.
Totd number ot
n.lr B^inl.
23.716
23.7U
23.78
142.1'.t4
10.0
10.0
10.1
@.2
35,012,%2.2
34,8r0.565.6
35,36't,869.5
210,W4,'t73.3
805.4
801.0
813.5
4,832.3
1 10.55
't10.32
1 1 0.69
60:!.28
6
6
190
189
190
1,138
F = Unlt Offline
E = Exceedance
I = lnvalld
M = Malntenance
Report Generated : O4l L1,/24 L3:19
GP043AS-036878-RT- 1 579
C = Calibration
S = Substltuted
T = Out Of Contml
Page 197 of 29O
Average Data - Low FIow Run 9
Plant: HUNTINGTON PIANT
Interval: 1 Minute
Type: Block
Report Period : Ml 1 1 12024 1 3: 1 3 Through Ml 1 1 I 2024 1 3: 1 I
Time Online Criteria: 1 minute(s)
Source
Paramet€r
(Unit)
Ul11l24 13:13
UNIT2
BARPRESS
(rNHG)
coz
(PCr)
FL{JWI'(;FH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNII LOAU
(trfw)
23.733 10.0 &2.4 1 10.68
Ut11l24 13:14 23.732 r0.0 34,8&t,737.0 802.3 110.68 190
Ul11l24 13:15 23.732 10.0 35,149.528,2 110.73 191
04n1n1 13:16 23.73t1 10.1 35,45.693.3 814.7
Un1n4 13:17 23.73t1 't0.1 35,485,192.3 818.1 110.7't 190
Ul'11121 13:'18 23-733 10.0 35.520.012.6 8',t7.7 110.93 189
A\r6rago 23,733
Minlmum 21.732
Madmum 23.733
Summation 1.t2.396
lncluded Dela
P^i^la
Total number of
ndc P^inle
F = Unit Offline
E = Exceedance
r I = lnvalid
M = Maintenance
Report Generated:. 041 Ll/24 L3:20
cP043AS-036878-RT-1 579
10.0 35,215,'.t72.1
10.0 34,883,737.6
10.1 35,520,012.6
60.2 211.291.032.5
810.4
802.3
817.7
4,862.5
110.73
1 10.64
110.93
664.37
190
189
'191
1,141
C = Calibration
S = Substltuted
T = Out Of Contrcl
Page 198 of 290
l
Appendix 8.2.2
High-Load Flow RATA
Average Data - High Flow Run 1
Plant HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0/.11112024 14:42Through Ml11t2O24 13:19
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul11l24 14:42 45
UNIT2
BARPRESS
flNHG)
c(Jz
{PCT)
FLAWSCFH
(scFH)
\i I KFLUW
(KSCFM)
STl(TEMP
(DEGF)
UNII LOAU
ruw)
23.694 1't.5 160.1 ,629.8 108.
01111124 14:43 23.695 11.6 70,470,76A.4 1,619.2 108.91
Ul11l24 14i44 23.695 1 1.6 69,912,893.4 1,606.4 108.91
11.6 69,663,230.8 1,601.9 109.38 440Ul11l24 14:16 23.695
04l'11121 11:47 11.5 68,032,563.0 1,583.7 108.04 438
Ml11l21 11:48 1 1.5 6S,660,571.2 1,600.6 108.92 ,l38
Ul1'1121 11:49
Ul11l21 't4:5O 23.694 11.4 69,695,060.0 1.602.0 109.32 438
ur11l24 14:51 23.694 11.4 6g,4sz,z8/.3 i,sgzF -- 1og.2o /rsE
Mt11n4 U:52 23.A94 11.1 09,409,568.2 1,597.3 109.30 437
Ul11121 14:54 23.694 11.4 70.282.055.2 1,616.8 109.58
Ul11l24 14:56 23.694 11.4 69,427,380.4 1,598.0 109.87
Ul11l21 11:57 23.693 11.4 69,'t.t8,308.4 1.592.'1
Ul11l24 14:58
Ul11124 14:59 23.852 1 1.3 69,609,7,+5.0 1,604.5 110.A7 437
Ul11l24 15:00 23.652 11.3 70,142,182.9 1,617.1 1,t0.75 437
Ul11l21 15:01 23.691 11-3 69,684,03i,.3 '1,606.5 110.74 rl35
Ul11l24 15:02 't1.3 70,il1,876.2 1,622.6 109.43 4U
Ul11l24 15:03 23.690 I 1.3 69,540,073.8 1.597.8 108.79
04111124 15:O4 11.2 69,033,739.1 1,584.5 108.19 ,l{}0
04111124 15:05 23.689 11_3 68.700.978.0 't,576.3 107.95
Ul11124 15:06 11.2 68,770,714.5 1,577.4 107_80 4fi
Ur11124 15:07 23.688 11.2 1,584.8 t07.06
11.3 69,432,117.3 1,591.8 107.6 433
69,109.204.6
Ul11l24 15:08 23.887
04111124 '15:09 11.3 1,594.8 t07.38
04111124 15:10 11.4 69.849.606.'t 1,600.9 'to7.2s 442
Ut1'1124 15:11 23.087 11.5 1,596.9 108.94
11.5 69,432,374.9 t,ses.7 106.74
-
445
-.
09,719.802.9
ut1'v24 15:12 23.687
Ul11l24 15:13 23.687 11-6 69.219.2't8.1 1,585.2 106.84
04111124 15i14 1 1.6
11.5
68,990,047.1 1,580.7 107.10 438
Ul11l24 15:15 68,989,950.9 1,581.2 107.44
Ul11l24 15:16 11 .5 08,876,718.2 1,580.3 107.8!t
ut11tz4 E1g&ceedance2s.684 11.3 o8,g7s,oo8.o r,ieo.I 110.60 .ll!3
I = lnvalid
M = Maintenance
Report Generate d: 041 t7 I 24 7S :23
GP043AS-036878-RT- 1 579
G = Calibration
S = Substituted
T = Out Of Control
Ul11l21 15:17
Page 200 of 290
Average Data - High Flow Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: C/,n112024 14:42lhrough 0411112024 15:19
Time Online Criteria: 1 minute(s)
rI
Averag6
Minimum
Malimum
Summalion
lnduded Data
P^ihle
Total number of
nat. 9^iht.
23.091
23.e83
23.0S5
9O0.2,ltl
69,490,670.9
68,295,019.8
70,949,160.'l
2,640,645,492.9
1,596.8
1,572.e
1,629.8
60,677.1
108.85
106.74
114.75
4,139.27
11.4
11.2
11.0
433.5
437
429
48
16,610
38
38
38
38
38
38
38
38
38
38
38
38
F = Unit Offline
E = Exceedance
I = lnvalld
M = Maintenance
Report Generate d: O4l LU 24 L5 :23
GP043AS-036878-RT- 1579
C = Calibration
S = Substituted
T = Out Of Control
Page 201 of 290
Average Data - High Flow Run 2
P|ant HUNTINGTON PI.ANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Period: 04.1111202415:32 Through Ml11l2O24 15:52
Time Online Criteria: 1 minute(s)
Source
P*dneter
(Unit)
Ul11l24 15:32 433
UNIT2
BARPRESS
(NHG)
coz
(PCr)
FLUWI'UI.H
(scFH)
STKFLQW
(KSCFM)
!iI KI EMP
(DEGF)
UNITLQAD
(tuw
23.683 't1.3 1,600.5 111_41
Ul11l24 15:33 23.683 fi.3 69,356,465.4 1,602.0 111.U 4,it3
Ul11l21 15:U 23.683 11.3 09,161,131.7 1,597.6 4U
04111124 15:35 23.683 11.3 68,885,950.3 1,591.5 111.77 rli,5
0411121 l5:36 23.683 11.2
1 1.3
68,919,937.0
ut11t24 '.15._17 1,592.6 112.03
04111124 15:38 23.683 11.3 69.083.445.7 1,596.6 1 11.96
04111124 15:39 11.3 68,940,8@.4 1,592.6 111.71 4U
04111121 15:/tO 23.ffi2 't 1.3 68,710,516.0 1,5A7.2 111.65 1y
Ul11l24 15:41 23,681 1't.3 48,87a&.7 1,591.0 I I 1.86 4U
Ul11l24 15:42 23.681 11.3 69,133,007.9 1,557.7 111.87
Ut11l24 15:/13 23.680 1 1.3 69,340,045.2 1,60r.4 111.47 435
Ul1'1124 15:44 23.678 11.4 69,085,581.2 1,595.2 1 11.31 437
4411n1 15:45 23.679 11.4 68,8{X,829.9 1,589.3 111.53 438
04trn1 15:46 23.679 11.1 68,751,348.1 t,5ae.2 111.5S 4s7
04l'11124 15:47 23.680 11.1 66,679,76/t.t r,536.5 110.18 438
04111124 15:48 23.680 11.4 67,40/.,452.8 1,550.8 108.82 438
Ul11l24 15:49 23.679 11.4 68,199,950.4 1.567.0 '108.50
Ul11l24 15:50 23.677 11.4 68,&17,901.0 1,570.2 108.48 438
Ul11l21 l5:51 23.676 11.4 68.263.786.6 't,568.4 108.43
Ul11l24 15:52 I 1.5 67,998,450.0 1,fi2.1 437
A\rerage
Minimum
Milimum
Summation
lnduded Data
P6inra
Total number of
ndr P$nla
23.681
23.676
23.683
497.252
68,676,632.3
66,679,764.1
69,356.405.4
1.442.2@.277.A
1,584.4
1,536.5
1,602.0
33,271.4
1 r0.86
108.34
112.03
2,328.11
I 1.3
11.2
1 1.5
23A.2
4il6
43r3
438
9,150
21
21
21
?1
21
21
?1
21
21
21
21
21
F = Unit Offline
E = Exceedance
! = Invalid
M = Maintenance
Report Generate d: 04 / tt I 24 t6:O2
G P043AS-036878-RT- I 579
C = Galibration
S = Substituted
T = Out Of Control
Page 202 of 290
Source
Parameter
(Unit)
ut11t24 10:05
Average Data - High Flow Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Peri od: Ml 1 1 I 2024 1 6: 05 Through O4l 1 1 I 2024 1 6:25
Time Online Criteria: 1 minute(s)
,323.2
UNIT2
BARPRESS
0NHG)
co2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNI I LOAU
(MW
23.681 11
ut11t24 16:06 23.681 11.3 68,260,1 19.2 1,576.2 1',t1.11 431
un1l24 16:07 23.683 11.3 68,321,411.4 1.577.5 'n1.39 431
ul11t24 16:08 23.683 11.3 68,676,389.2 r,585.9 '111.5't rl33
o4t11t24 16:09 1 1.3 69,139,869.6 1.597.1 1 11.66 435
Ul11l24 16:10 23.681 1 1.3 69,518,963.4 1,605.8 11 1.58
ut11t24 16:1'l 11.3 69,458,617.2 1.604.3 1't 1.54 4{t8
Un1n1 16:12 23.681 11.3 69,518,831.4 1,605.6 111 .53 438
04n1n1 16:13 11.1 69,703,592.4 1,611.1 111.55 439
Ml11l24 16:14 2?.682 11.4 69,483.938.0 1,605.2 1',t1.70 438
04111124 16:15 11.1 48,927,162.7 1,592.5 111.78 437
Ul11l24 16:16 23.681 11.4 68.629.5s6.7 1,585.2 111.59 436
ut11l24 1A:17 11.1 48,28/.,444.8 1 ,577.5 I 1t.69 4U
0411'1124 10:18 23.482 1',i.4 68,341,081.3 1,579.3 111.87 435
Ul11n4 16:19 23.081 11.4 68,779,098.2 111.79
0411'|124 1A:20 23.681 11.4 68,754,291.9 1,588.7 111.79
o4111t24 16'.21 23.681 11.1 68.2110.994.5 1.576.7 111.7s 436
o4111124 16:22 23.081 11.4 08,375,703.8 1,579.6 111.68
Ul1'1121 1A:23 23.681 4{}611.4 a8.772.800.7 1.588.9 11',1.72
ut1'v21 1'1.1 68,916,409.7 1,592.1 111.74
Ul11l24 16:25 23.681 4381'.t.4 68.9/10.411.3 1,593.5 | 1'1.95
A\Ierage
Minimum
Marmum
Summdion
lncluded Data
P^inra
Total number of
nd. P^inla
23.681
23.680
23.4U
457.311
68,U2,129.1
68,240,994.5
69,763,592.4
1./t45.691.010.6
1,590.3
1,574.2
1,611.1
33,396.2
1 I 1.85
1 1 1.39
111.95
2,U4.73
11.4
't 1.3
11.4
238.6
436
43'l
439
9,148
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4l Ll /24 16:27
GP043AS-035878- RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 203 of 290
Average Data - High Flow Run 4
Plant: HUNTINGTON PLANT
Interval: 1 Minute
Type: Block with BAF Applied
Report Period: 0/,1111202416:37 Through M11112024 16:57
Time Online Criteria: 1 minute(s)
Source
Paramet€r
(Unit)
Ul11l24 16:37 435
UNIT2
BARPRESS
(NHG)
coz
(PCr)
FL(,WtiSFTI
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNILOAD
(MW)
11.1 65,172,763.1 ,590.9
ul11t21 23.476 11.4 88.872.022.8 1,W.7 109.25
ut11t24 16:39 29.476 11.1 68.887.380.0 1.584.9 109.19 436
ul11121 23.676 11.4 68,766,751.0 1,581.6 109.02 4{r5
Ul11l24 16:4'l 23.676 11.3 68,619,724.9 1,577.6 108.80 4U
ut11l21 16:42 23.075 11.4 6,724,073.8 1,575.4 108.57 433
ul11t24 16:43 23.475 11.4 68.751.361.2 1,579.7 108.45 435
uA1n1 23.675 11.4 68,859,550.7 t,582.0 't0€.37
ul11t?4 l6:45 11.4 68,911,565.8 1,583.5 108.48 437
04111t24 l6:46 23.675 11.4 68,831,472.8 1,582.3 108.71 438
ut11l24 23.675 11.4 69,288,68:i.3 1,599.8 111.A 438
ut'|1124 16:,18 23.675 11.4 s},175,78:1.2 1,588.2 111.57 438
ut1'U21 23.675 11.4 68,929,128.7 1,592.6 111.62
oq11n4 10:50 11.4 @,127,U7.5 1,597.5 11.1.70 437
ut11nl 23.675 11.4 69,14{t,678.3 1,598.4 11'.I.92
04t11t24 16:52 23.675 l't.3 68.051.353.3 1,587.4 112.02 433
o4t11t21 23.675 11 .3 68,098,18:i.7 1,588.5 112.00 433
ut11t21 16:S 43211.3 68.941.753.3 '1,594.7 112.25
Mt11t21 16:55 23.674 11.3 68,851,313.2 1,592.4 112.16 4?2
04t11t24 16:56 I 1.3 49122.332.8 1,598.6 1 12.13 436
ul11t24 16:57 23.474 11.3 69,298,188.4 1,602.9 112.20 €8
A\rerage
Minimum
Maxmum
Summation
lnduded Data
P^inr.
Total number of
hrl. P^inl€
23.675
23.674
23.677
197.174
68,934,429.1
68,619,724.9
69,298,188.4
1,447,623,011.6
1,589.4
1,577.e
1,002.9
3|3,377.0
110.41
108.37
112.25
2,318.7',|
11.4
11.3
11.1
234.7
435
432
438
9,145
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d: 04/ 7t I 24 t6:59
GP043AS-036878-RT- 1579
C = Calibration
S = Substituted
T = Out Of Control
Page 204 of 290
Average Data - High Flow Run 5
Plant: HUNTINGTON PISNT
Interval: 1 Minute
Type: Block with BAF Applied
Report Period: Ul 1 1 12024 1 7: 1 0 Through O4l 1 1 12024 17 :30
Time Online Criteria: 1 minute(s)
Source
Paraneter
(Unit)
Ul11l24 17i10
UNIT2
EAXPIIEt't'
(NHG)
vgz
(PCr)
FL(,WS(;FII
(scFH)
s I Kt-LUW
(KSCFM)
5I KI EMF
(DEGF)
UNII LUAU
(MW)
11 1 11
Ul11l24 17:11 23.873 1 1.3 68,773,551.5 1,592.2 I 1 2.09
Ul11l24 17:12 23.673 11.3 68,912,761.4 1.595.7 112.79 4U
Ul11l24 17:'13 23.673 I 1.3 69.022,052.5 1,598.0 112.73 €3
Ul11l24 17:14 1 1.3 68,783,944.2 1,592.3 112.66
ut11t24 '17:15 23.674 11.3 68.520.472.2 |,586.1 112.U 432
Ul11l24 17:14 23.674 11.3 68,4r)7,568.1 'f,582t.8 '112.4
04111124 17:17 23.674 11.3 68.880.512.6 |,588.r I 1 0.36 4U
Ul11l24 17:19 1 1.3 68,562,371.8 1,579.2
Ul11l24 17:19 23.674 11.3 68.344.994.7 I,573.1 109.40 436
ul11nl 17._20 23.674 11.4 68,641,903.8 1,579.1 10s.10 437
O4n1n1 17:21 23.474 11.1 69.070.256.3 t,588.6 r08.97 437
Un1n1 17:22 11.5 08,930,348.3 1,585.0
04111124 17:23 23.A74 11.5 68.855.380.8 1,583.8 109.01 4it9
O411n1 17:24 23.673 11.5 68,836,952.7 I,584.1
04111121 17:25 11-4 08,798,302.5 1,*2.7
04111124 17:26 n.673 43911.4 @,724,965.7 1.579.8 108.63
Ul11l21 17:27 11.1 68,595,39S.2 1,576.8
Ml11t21 17..2A 23.473 11.4 68,277,330.9 1,569.5 108.65 /l3o
ut11l21 17..29 11.1 a7,743,872.4 1,557.8
04111124 17:30 23.673 43511.4 67,777,118.5 r,558.0 108.63
A\rerage
Minimum
Maximum
Summation
lncluded Data
P^int.
Total number of
nd. hi^ta
23.673
23.672
23.674
197.112
11.4
11.3
1't.5
23A.7
68,627,496.9
67,777,116.5
69,070,256.3
1,441,177.435.4
1,582.0
1,557.8
't,598.0
33,222.2
110.25
108.49
112.79
2,315.27
436
432
439
9,150
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/17124 t7:32
GP043AS-036878-RT-1579
C = Calibration
S = Substituted
T = Out Of Control
Page 205 of 290
Average Data - High FIow Run 6
Plant HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Peri od: Ul 1 1 I 2024 1 7: 44 Throu gh 04 I 1 1 I 2024 1 8:04
Time Online Criteria: 1 minute(s)
UNIT2
BARPRESS
(INHG)
(j{Jz
(PCr)
FLOWSCFH
(scFH)
UI KI-LUW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAO
(MW)
11.2 68,74{},897.3 I 1.96
ut11t24 17i45 23.672 11.2 69,216,129.1 i,599.8 111.71 -Ao--
ut11n4 17:16 11.2 89,93/1,327.0 1,610.5 111.76
Source
Parameter
(Unit)
Ul11l24 17:44
ul11t21 17:47 11.3 70,u7,1$.2 I,619.2 111.80
ut11l24 17:49 23.672 1'.t.1 70,072.592.1 1,420.7 112.13 440
ul11t24 l7:50 23.672 11.4 69,687,947.6 1,612.5 1',t2.51 41
ut11t24 69.527.95S.7
ut11t21 17:52 23.673 11.3 69,203,618.4 1,603.6 112.73 439
ut11l24 17:53 1 1.3 68,917.555.4 1,595.6 112.70
ul11t21 17:il 23.A?3 11.3 08,677,5€l:1.1 1,590.7 112.*
un1n4 23.672
uh1n4 17:50 23.672 68,801,075.2
04t11t24 23.672
04t11t24 17:58 23.67'l 68,995.818.6 1,597.5 't12.73 437
041'11t24 23.671 69,502,257.8 1,608.4 112.1'.1 439
04t11t24 18:00 23.671 11.4 69.494.939.4 1,608.5 112.51 439
ul11l21 l8:01 23.471 11.1 89,130,230.7 1,600.9 112.81 437
ut11t24 18:02 23.87'.i
o4t11t24 23.871 87,Ct2,735.1
Average
Minimum
Maximum
Summation
lncluded Data
P^iatc
Total numbor of
n.li P^inlc
23.672
23.671
23.673
497.108
69,080,907.4
a7,572,735.1
70,201,495.O
r.450.699.055.9
1,597.9
'l,558.3
1,623.1
33.556.8
11z.',t8
109.90
112.U
2,355.09
11 .3
11.2
11.4
237.8
436
428
u1
9,166
21
21
21
21
21
21
21
21
21
21
21
2',1
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4h7l24 t8:2O
G P043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Control
Page 206 of 290
Average Data - High Flow Run 7
Plant HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Period: Ul 1 1 12024 1 8: 1 7 Through Ml 1 1 12024 18:37
Time Online Criteria: 1 minute(s)
Source
Pardne{€r
(Unit)
Ul11t24 18:17 23.669 11.5 68.804.012.9 1,588.4 '110.97 438
UNTT2
BARPRESS
(NHG)
c02
(PCr)
FLOWSCFH
(scFH)
S I KFLOW
(KSCFM)
SI KI EMP
(DEGF)
UNII LOAU
(tlW)
Ml1'1124 18:18 23.669 1 1.5 68,464,736.5 1.5€,2.2 111.57 437
Ul11l24 18:19 23.669 11.4 68,295,933.9 1,578.8 11'.t.74
ut11t24 18:20 11.4 68,555,463.8 1,585.0 111.82 4g
Ul11l24 18:21 23.668 't1.4 08,861,377.6 1,591.9 111.74 4"i3
ut't1t21 11.1 68,686,318.9 1,588.0 t't 1.80
04111124 18:23 23.668 4i,3t 1.3 68,879,820.7 1,5S3.'l 112.03
o4t1'1124 18124 11.3 68,761,579.3 1,590.0
unln4 19i25 23.667 11.3 68,838,754.'l 1,592.3 112.05 433
ut11n1 11.1 69,205,557.8 1,401.2 435
Ul11l21 18i27 23.667 11.1 69.096.329.8 1,599.3 112.41 ,136
ul11t21 18:2a 11.4 69,O19,138.5 1,598.5 112.52
ut1'U24 18:29 23.667 11.1 69,(x2,O11.6 1,598.6 112.81 .[38
oq11n4 18:30 23.ffil 1 1.3 68,981,208.8 1,597.2 112.il 437
o4t11t24 23.668 't 1.3 68,753,174.6 1,592.2 112.71 4v
04111124 18:32 23.668 11.3 08,309,662.4 1.582.3 1 12.89 429
a4'11t21 23.668 1'l .3 68,192,351.8 1,579.3 't12.80 424
Ul11l24 18:34 23.668 11 .3 68,137,502.7 1.577.4 112.57 427
ut11t24 23.069 11.4 67,863,771.9 1,571.1 112.57 131
04111124 18:36 23.669 11.4 67,843,411.0 1,570.9 112.65 435
oqt11t24 18:37 23.669 11.5 87,767,816.6 1,568.6 112.51 437
Average
Minimum
Ma)(imum
Summalion
lncluded Data
P^iate
Total number of
nrl. P^inta
23.668
23.667
23.669
457.O27
88,589,998.3
67,767,816.6
69,205,557.8
1,,140,389,905.2
1,587.0
1,568.6
1,601.2
33,326.9
112.24
110.97
1 1 2.8S
2,356.96
11.4
1 1.3
t.t.5
238.9
4U
424
438
9,109
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generated: O4lLll24 18:39
G P043AS-036878- RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 207 of 290
Average Data - High Flow Run 8
Plant HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Period: 04,1111202419:01 Through 0411112024 19:21
Time Online Criteria: 1 minute(s)
Source
Parsnder
(Unit)
Ml11l21 19:01
UNIT2
nAr{Pt(Ess
(rNHG)
c02
(PCT)
FLOWSCFH
(scFH)
U I KFLUW
(KSCFM)
st Kt tsMP
(DEGF)
UNITLOAD
(MW
23.673 11 .3 1,594.4 110.32
ut11t24 19:02 23.672 11.2 69,922,806.1 1,618.0 112.41
ut11t21 23.673 11.2 70.227.W0.5 1,427.8 1 13.39 430
ut11t24 '19:04 11.123.674 70,459,647.0 1,633.9 113.66
o4t11t24 23.474 t 1.1 70,437,219.7 1,U2.8 113.72 433
ut11l24 19:06 11.O 70,773,081.6 1.646.9 't 15.68 435
01111124 19:07 23.675 11.0 70,383,990.8 1,U4.7 118.09 436
o4111t24 11.0 70.234.702.4 1.64 t.0 't 18.02 435
04t11n4 l9:09 23.675 11.0 70,188,708.7 1,640.1 1 18.08
ut11t24 11.0 70,290,200.9 1.642.9 11A.17 435
ut11t24 19:1 I 23.676 11.0 70,084,186.4 1,637.6 1'18.O7
ut11l24 I 1.0 69,703,071.8 1,628.4 117.57 4U
un1n4 19:13 23.676 I 1.0 70,132,474.7 1,631.2 115.&
Oq11n4 l9:1.t 23.676 43310.9 70,663,8S8.8 1,038.9 1 13.81
O4t11124 19:15 23.676 1'1.0 70,962.973.3 1,645.9 fi3.42 432
o4t11t24 l0:16 23.676 11.0 71,213,8,.3.0 1,651.6 113.78
ut't1t21 19117 11.0 71,5'.t5,741.4 1,658.1 fi3.42 435
o4t11t24 l9:18 23.677 11.0 71,411,374.1 1,060.1 1 1 3.56
ul11t24 l9:19 1 t.0 71,173,871.A 1,650.5 113.73 438
ut11t24 1g:20 23.076 11.0 71,165.035.4 1,650.3 'l't3.73
ul11t24 19:21 11.1 71,540,700.3 1,657.9 1 1 3.38 4q
Average
Minimum
Maimum
Summation
lnclud€d Data
P^inra
Total number of
net. P^ihta
23.675
23.672
23.677
197.179
70,583,103.1
69,155,109.8
71,611,374.1
'1.482.246.125.7
1,UO.2
1,594.4
1,660.1
3.+.t143.6
114.89
'110.32
118.17
2,412.A1
11.0
10.9
11.3
231.9
4v
429
110
9,1 19
21
21
21
21
21
21
21
2'.1
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate d : 04ht I 24 79 :23
GP043AS-036878-RT- 1 579
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 208 of 290
Average Data - High Flow Run 9
PIant: HUNTINGTON PI.ANT
lnterval: 1 Minute
Type: Block with BAF Applied
Report Peri od: Uh 1 I 2024 1 9: 33 Through O4l 1 1 I 2024 19:53
Time Online Criteria: 1 minute(s)
Source
Parander
(Unit)
Ul11l24 19:33 23.880 10.9 70,763,966.1 1,040.3 113.57
UNIT2
EAKTKEl'S
(NHG)
GUz
(Pcr)
FLUW5(;rn
(scFH)
u I KfLtJW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW}
ul11t21 19:34 23.681 10.9 71,026,825.5 1,645.8 113.40 €3
Mtl1t24 23.681 71.357.034.8 1,653.6 t t3.46
Mt11l24 19:36 23.@2 10.9 7't,779,537 .8 r.664.0 1't 3.60 .l{l3
ut|1l24 23.682 10.9 71,865,087.8 1,661.8 113.M
04t11t24 19:38 23.682 10.9 71.537.512.6 1,668.2 113.86 435
ul11n4 23.683 10.9 72,228,722.9 1,074.9 1 13.86
o4t11n4 19:40 23.683 43510.8 71.913.774.1 1,078.0 117.45
04111n1 19:41 23.684 10.8 71,924,907 .8 1,675.8 1 1 6.62
ul11l24 /ti}o10.81g:12 23.684 71,706,630.6 1 ,672.0 1 17.06
Ul11l24 19:43 23.685 10.8 71,807,301.4 1,677.4 1 18.15 436
ut11t24 23.885 71,782,144.4 1,676.7 118.14 437
ut11t24 l9:/15 2s.686 43510.8 71.634.900.8 1,663.5 114.77
04t11t21 23.687 70,945,331.5 1,651.7
04t11t24 1g:47 23.688 10.9 71,6'.t7,941.7 1,659.9 113.72 4y
ut't1t24 19:48 23.689 10.9 71,803,120.1 1,661.'t 112.67 435
o4t11t21 23.690 10.9 71,774,0€,0.4 1,657.0 11',i.19
ut11l24 19:50 23.691 10.9 71,797,570.5 1,655.3 110.74 4v
Mt11t24 23.652 71,423,942.7 1,e4€'2
ut11t24 19:52 23.691 't0.9 71,443,206.0 1.e[6.6 110.57 436
ul11t24 19:53 23.492 10.9 71,588,380.5 1,&19.5 110.43
A\i€rage
Minimum
Madmum
Summation
lncluded Data
hi^ta
Total number of
nda D^inra
23.686
23.680
23.652
497.398
71,615,374.5
70,763,966.'t
72,228,722.9
1,503,922,864.4
1,660.9
1,640.3
1,078.0
34,879.3
114.O1
r 10.43
1 18.15
2,394.30
10.9
10.8
10.9
224.2
.135
431
437
9,130
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated: O4ltll24 19:56
GP043AS-036878-RT- 1 5 79
C = Calibration
S = Substituted
T = Out Of Control
Page 209 of 290
Appendix 8.2.3
Gas RATAs
GP043AS-036878-RT- 1579 Page 210 of 290
Average Data - Gases Run 1
Plrd: HUNTNGTON Pt A|.lT
lnttMl: 'l Minutc
Ttpa: Rol
R6port P.dod: 04/l ffin4 1,1:/t2 ThrcUEh O4/1112@4 15:19
Tkn. orllm critdh: 1 mlnu.(8)
w1D1 114 421.4
Mlm
1nt &.0
tl,a
Nlha 1a:4 ?ra s 4 a,@_a
i15 21Aa 7&6 $,0 & .,.10.1
--?i/iiill:-"i6 ---rarr f61t
o@
Mrra r48 &2 o_13t rl.a 116! &5 orlr
a7 4Sr.O
a@_3 0.1t!g 43744
@11ir i6o3
s3_a 0.14
E6' ois rt -- $! --- *- -iai -- -di&- -6-- - -' t'4: - -- 6.62 -- - -iir '- "' --
ulda 16.01 &2t oie -_-- --
afi!
qtza i5:@ &0.7 0.1!7 11.3 ots {.9 1&.4
-rin;"- ."-oio;_"-----"-ir.s"- - @1-oqlDa iaii"--wi*
M1A1 L:13 &t 0.101 11_a
WlAa 15:11 2,4.a
&toa 1516 4ai
& 4,330.1
E. E otrtrml
C = OIbndo
3 . Subctuncd
ir!illhbmn.Je:
T= Od Of Conhl
t . Su.9cci
u,sbtupbnGffindg/1u4
GP043AS-035878-RT- 1579 Page 211 of 290
Average Data - Gases Run '1
P|ant: HUNTINGTON PLANT
lnteMl: I l\4inute
Type: Roll
Repofr Periodr Ml 1/2024 14:42lhtoulh Mh j nA24 15: j9
oos
Time Online CnterEt 1 minde(sl
1 06i.3 0.242 2,3A
4335 42515
lrcluded DdaPonrs
Tohl tum*r orDara
0 03r
0039 3!3 416
F = Unit Offline
E = Excaadance
C = &libEtion
S =Substituted
U = Stafrup
GP043AS-036878-RT- 1579 Page 2L2 of 290
Average Data - Gases Run 2
Ptdr t{,ritTltoToN Ptlt{Thhnrt t Lrub
q7N L4
I
I
I
i_
I
ir
ilr
I
rr3 aa ffa.t olo a! 1fl,, o.qt ru d 49,
It, 4 7.n! qts ,l rG? c@ lat s 4d7
tt, *2 w qir 1@1 rs m t! o 4ru
N tttu 1f .7tf 2 u lryi qal qr w ato aaLr
0Ju
0s
1-62
A4 lll.t
tu n{a
Em6,
ffi q$a
F.tlrtOrlh.
t.EE -scrGrlid..l
3.3i.dtrbd
ll.tbhnm
I . ori Ot Cailrcl..3rtrac
U.hDit.te-i*Oarrl/2a
GPO43AS-035878-RT-r579
l
I
1
1
i
r1
lli1
Pagc 213 of 290
I
Average Data - Gases Run 3
Phnt Ht NThIGTON Pl-r*,fi
lntard: I l,Inuta
TlD.: Roll
R.pon Pdiod: Oryl1/2@t t6:05 ThB{h O+tlr2@4 1e25
TXna OrllE Cdkh I miilrt (.)
I Mtza ras nil o,@ ti3 s &7 q12 t@,! tra.o c@ t5, a,c6,7
6! -:ilio*
s!
oi'
a4a-
cls
il.r M3 a.ts r@t tEa oq ta.7 4a 4Sa
!r.r &7 c1$ s,a 1D.9 Ok lat 4t 4na2
213 &O qt' 16I a.6 o.@ 17/ 49 a,4lea
1.&7 t7,t.a ts arttt afr.7 oga *t a,14 ,1,&O
r,|'4 11.a
tuA1
b i.tiao
o,&
oil
2.1fr
i i
A
A
b
21
x
F r Unli Oflllm
: E.Erard.M
C. Olbndd
S.S{bdhftd
M. lr.lnt n n6
T.06Ol6d
I t.sstPaat
U. St itp
hnc.ddq/11,laI Gpo43As-o36B7s-RT-r579 Page 214 of 290
I
i1
I
l
l
i
!
I
i
,1
Average Data - Gaas Run 4
Ptril: HUNTtilGTCrl.l PLA{Ihi.r{: I lfrrL
Tna: Rol
RltulFlrlod: 0{r11r}iaa lctlTtn^dr 0{6ffm1 lc'lftrmrOidr tnlilh(.|
llrl
l
1
I
ro 1al &dr rl_t d a.sr
a, t4! o.q tlt 4 {fj
r4t t& q6 1rt { .s2
211?2 trD' !& Ol ar{ 60{,
@ cln
ffdt olt
{., qrl
1lfit G
.14 il
rr, u
rl.a ia!
stt&
N0s
ru crB
d
A
21
al
,t
A
n
A
21
8
2l
x
d
u
d
I
l
l
I
F. lrolt O{lim
E.btE
c.Oltdoi
S.n$dni..l
ll.iih[E
T . orrt OlGoorol..3c?..t
U .3i.dup
TFffiq,lu"
GP&3AS-036878-RT- 1579 Plgc 215 of 290
Average Data - Gases Run 5
Plmt tlt NT}{GToN Pt-Al,lT
lrtond: 1 Mnub
Typc: RoI
R.Oort Psid: O{,1 12m4 17:10 Th
Tknc oriim Crib.h 1
0.8 ir.! 4! 6,9 O.@ i6J
-wiE-1,fl__--g_---=.iiru
0,67 rr.l tlJ s.7 ofi iol.! 4iin -sra. r71a $rr 0,62 r,! 4., _*- --ffi
o.@r 1i t s, aal
11.5
fi.4
iii
qN 11.. a1 uu ffi
Mi;r_1fu _,i1---_6--.!N-
ffi -
o.e tlr &j tu3 Ol$ r&.3 1n3 o&t ia., M asET
0.6 tl.a 4.7 &rJ qi6 *.7 t&tr q@ t0 €2 a&5
orra ,1,5 l@s 8Z6 019 1@.2 t!r.C dos 1,! & .,{U
l.m dJ 1.&' ttd,7 ,r& zlota ,.tN o.& a27.3 alao &,@za
21
A
x A
il
n
21
1 ar 21 21
21
21
21
21
x
*,
h 211,a
h
8ffi 7M!
ll&rhr
Td,lJddr a
Page 216 of 290
F r Unlt O{lllm
E - is.d.E
C. CdlbIilcn
3 i Stb.tltrtd
M. t .lnrmho
T.oln O{Ccffil.. Ssapad
U. StIup
i@n G.ldd:fl/tlna
GP043AS-036878-RT- 1579
ir
I
Averago Data - Gases Run 6
Plrnr lt {TxtToN PtllrafH.nrt t Hilb
TrD.: R l
Rr.rt P.dd O+l't &l t7:4,1Thdt 0lrllrl@l ttoa
Tln dmcdirh I mlra(.l
k
ll
I
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GPO43AS-036878-RT- 1579
t-
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PrgG 2u of 290
Average Data - Gases Run 7
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Page 218 of 290
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GP043AS-036878-RT- 1579
Averagc tlata - Gases Run 8
Pttrr HID|Tn.oTON Ptrtar
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GP043AS{36878-RT- 1579
,t
Li
t;
I
Average Data - Gases Run 9
Pl.ri: }ITNTbIOTON HJINT
hiana: I llnrft
&@
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s1ru 18 ts, o!il to ffi s in w artr 6 6tu
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PagG 220 of 290
F. thlt Orilo.
l. haad.no
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3.3ifirbd
tr.lfhi.E
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GPO43AS-036878-RT-1579
)
Appendix C
Quality Assu rance/Qual ity Control
Appendix C.1
Units and Abbreviations
GP043AS-036878-RT- 1 579 Page 222 of 290
MA*?N,T+S'S.H
UNITS AND ABBREVIATIONS
@Xo/o 02 corrected to X% oxygen (corrected for dilution air)
lCCl absolute value of the confidence coefficient
ldl absolute value of the mean differencesoC degrees CelsiusoF degrees FahrenheitoR degrees Rankine
" HzO inches of water column
13.6 specific gravity of mercury
AH pressure drop across orifice meter, inches H2O
AP velocity head of stack gas, inches HrO
e total sampling time, minutes
tJg microgram
P" density of acetone, mg/ml
Pw density of water, 0.9982 g/ml or 0.002201 lb/ml
acfm actual cubic feet of gas per minute at stack conditions
An cross-sectional area of nozzle, f(
As cross-sectional area of stack, square feet (ft')
Btu British thermal unit
B*" proportion by volume of water vapor in gas stream
C" particulate matter concentration in stack gas, gr/acf
Cn g average unadjusted gas concentration, ppmv
Coi|, measured concentration of calibration gas, ppmv
cf or ft3 cubic feetcfm cubic feet per minute
Cc". average gas concentration adjusted for bias, ppmv
CM average of initial and final system bias check responses from upscale calibration gas, ppmv
crn or m3 cubic meters
Cr',rn actual concentration of the upscale calibration gas, ppmv
Co average of initial and final system bias check responses from low]evel calibration gas, ppmv
Cp pitot tube coefficient
C. particulate matter concentration in stack gas, gr/dscf
CS calibration span, % or ppmv
Cs measured concentration of calibration gas, ppmv
Cv manufactured certified concentration of calibration gas, ppmv
D drift assessment, % of spandcf dry cubic feetdcm dry cubic meters
Dn diameter of nozzle, inches
Ds diameter of stack, inches
dscf dry standard cubic feetdscfin dry standard cubic feet per minutedscm dry standard cubic meters
Fd F-factor, dscf/MMBtu of heat input
fpm feet per minutefps feet per secondft feet
tt square feet
gram
gallonsgr grains (7000 grains per pound)gr/dscf grains per dry standard cubic feet
o
gal
GP043AS-035878-RT- 1 579 Page 223 of 29O
6.i\ l+?NI+gp.E-
I
in
k
K
K3
K"
kg
UNITS AND ABBREVIATIONS
percent of isokinetic sampling
inch
kilo or thousand (metric units, multiply by 103)
kelvin (temperature)
conversion factor 0.0154 gr/mg
conversion factor 0.002668 ((in. HgXft)X(mt)f n))
kilogram
l$ pitot tube constant (85.49 fUsec)
kwscfh thousand wet standard cubic feet per hourI literslbihr pounds per hourlb/MMBtu pounds per million Btulpm liters per minutem meter or milliM thousand (English units) or mega (million, metric units)
m3 cubic meters
ma mass of residue of acetone after evaporation, mg
Md molecular weight of stack gas; dry basis, lb/lb-mole
meq milliequivalentmg milligram
Mg megagram (106 grams)min minute
ml or mL millilitermm millimeterMM million (English units)MMBtu/hr million Btu per hour
mn total amount of particulate matter collected, mg
mol mole
mol. wt. or MW molecularweight
Ms molecular weight of stack gas; wet basis, lb/lb-mole
MW molecular weight or megawattn number of data pointsng nanogramnm nanometer
Pb", barometric pressure, inches Hgpg picogram
Ps stack static pressure, inches H2O
Pm barometric pressure of dry gas meter, inches Hgppb parts per billionppbv parts per billion, by volumeppbvd parts per billion by volume, dry basisppm parts per millionppmv parts per million, by volumeppmvd parts per million by volume, dry basisppmvw parts per million by volume, wet basisPs absolute stack gas pressure, inches Hgpsi pounds per square inchpsia pounds per square inch absolutepsig pounds per square inch gauge
P.to standard absolute pressure, 29.92 inches Hg
Q6 volumetric flow rate, actual conditions, acfin
Qs volumetric flow rate, standard conditions, scfrn
Q.to volumetric flow rate, dry standard conditions, dscfm
R ideat gas constant 21.85 ((in. Hg) (ft3)y((.R) (tbmote))
G P043AS-036878-RT- 1 579 Page 224 of 290
64\ ft?.N,T+P.LE
UNITS AND ABBREVIATIONS
SBrnal post-run system bias check, % ofspan
SBi pre-run system bias check, % ofspan
scf standard cubic feet
scfrr standard cubic feet per hour
scfin standard cubic feet per minute
scm standard cubic meters
scmh standard cubic meters per hour
sec second
sf, sq. ft., orf square feet
std standard
t metric ton (1000 kg)
T o.gzs t-value
Ta absolute average ambient temperature, oR (+459.67 for English)
Tm absolute average dry gas meter temperature, oR (+459.67 for English)
ton or t ton = 2000 pounds
tph or tons/hr tons per hour
tpy or tons/yr tons per year
T. absolute average stack gas meter temperature, oR (+459.67 for English)
T.to absolute temperature at standard conditions
V volt
Va volume of acetone blank, ml
V"* volume of acetone used in wash, ml
V6 total volume HrO collected in impingers and silica gel, grams
Vm volume of gas sampled through dry gas meter, ft"
Vm(std) volume of gas measured by the dry gas meter, corrected to standard conditions, dscf
Vr" stack gas volume sampled, acf
Vn volume collected at stack conditions through nozzle, acl
Vs average stack gas velocity, feet per second
Vwqsto; volume of water vapor condensed, corrected to standard conditions, scf
Vwi(srd) volume of water vapor in gas sampled from impingers, scf
Vwsslstd) volume of water vapor in gas sampled from silica gel, scf
W watt
Wa weight of residue in acetone wash, mg
Wi,rp total weight of impingers, grams
Wse total weight of silica gel, grams
Y dry gas meter calibration factor, dimensionless
G P043AS-036878-RT- 1 579 Page 225 of 290
60 lYl?.N,T+gp.H
ACRONYMS
AAS atomic absorption spectroscopyACDP air contaminant discharge permit
ACE analyzer calibration error, percent of span
AD absolute difference
ADL above detection limit
AETB Air Emissions Testing Body
AS applicable standard (emission limit)
ASTM American Society For Testing And Materials
BACT best achievable control technology
BDL below detection limit
BHP brake horsepower
BIF boiler and industrial furnaceBLS black liquor solids
CC confidence coefficient
CD calibration drift
CE calibration error
CEM continuous emissions monitor
CEMS continuous emissions monitoring systemCERMS continuous emissions rate monitoring systemCET calibration error testCFR Code of Federal Regulations
CGA cylinder gas auditCHNOS elemental analysis for determination of C, H, N, O, and S content in fuelsCNCG concentrated non-condensable gas
CO catalytic oxidizer
COC chain of custody
COMS continuous opacity monitoring systemCPM condensible particulate matterCPMS continuous parameter monitoring systemCT combustion turbineCTM conditional test method
CTO catalytic thermal oxidizerCVAAS cold vapor atomic absorption spectroscopy
De equivalent diameter
DE destruction efficiencyDioxins polychlorinated dibenzo-pdioxins (pcdd's)
DLL detection levellimitedDNCG dilute non-condensable gas
ECD electron capture detectorEIT Engineer ln Training
ELCD electoconductivig detector (hall detector)EMPC estimated maximum possible concentrationEPA US Environmental Protection AgencyEPRI Electric Power Research lnstituteES emission standard (applicable limit)ESP electrostatic precipitator
EU emission unitFCCU fluid catalytic cracking unitFGD flue gas desulfurizationFl flame ionizationFIA flame ionization analyzerFID flame ionization detectorFPD flame photometric detectorFPM filterable particulate matterFTIR Fourier-transform infrared spectroscopyFTPB field train proof blankFTRB field train recovery blankFurans polychlorinated dibenzofurans (pcdfs)
GC gas chromatography
GP043AS-036878-RT-1s79 Page 226 of 290
60 ltgNI+P"p.H
ACRONYMS
GC/MS gas chromatography/mass spectroscopyGFMS graphite furnace atomic absorption spectroscopy
GFC gas filter correlation
GHG greenhouse gas
HAP hazardous air pollutant
HC hydrocarbons
HHV higher heating value
HPLC high performance liquid chromatography
HRGC/HRMS high-resolution gas chromatography/high-resolution mass spectroscopy
HRSG heat recovery steam generator
lC ion chromatography
ICAP inductively-coupled argon plasmography
ICPCR ion chromatography with a post-column reactor
ICP-MS inductively coupled plasma-mass spectroscopy
lR infrared radiation
ISO lnternational Standards Organization
kW kilowatts
LFG landfill gas
LHV lower heating value
LPG liquified petroleum gas
MACT maximum achievable control technology
MDI methylene diphyenyldiisocyanate
MDL method detection limit
MNOC maximum normal operating conditions
MRL method reporting limit
MS mass spectrometryNA not applicable or not availableNCASI National Council ForAirAnd Steam lmprovement
NCG non-condensable gases
ND not detectedNDIR nondispersive infrared
NESHAP National Emissions Standards For Hazardous Air Pollutants
NG natural gas
NIOSH National lnstitute For Occupational Safety And Health
NIST National lnstitute Of Standards And Technology
NMC non-methane cutter
NMOC non-methane organic compounds
NMVOC non-methane volatile organic compoundsNPD nitrogen phosphorus detector
NSPS New Source Performance Standards
OSHA Occupational Safety And Health Administration
PAH polycyclic aromatic hydrocarbons
PCB polychlorinated biphenyl compoundsPCWP plywood and composite wood products
PE Professional Engineer
PFAS per- and polyfluoroalkyl substances (PFAS)
Pl photoionization
PID photoionization detector
PM particulate matter
PMro particulate matter less than 10 microns in aerodynamic diameter
PMz.s parliculate matter less than 2.5 microns in aerodynamic diameter
POM polycyclic organic matterPS performance specification
PSD particle size distribution
PSEL plant site emission limitsPST performance specification testPTE permanent total enclosurePTM performance test method
I
GP043AS-036878-RT-1579 Page227 of 29O
64\ l*?N,I+p.P.H
ACRONYMS
QA/QC quality assurance and quality controlQl Qualifled lndividual
QSTI Qualified Source Testing lndividualRA relative accuracyRAA relative accuracy auditRACT reasonably available control technologyRATA relative accuracy test auditRCTO rotary concentrator thermal oxidizerRICE stationary reciprocating internal combustion engineRM reference methodRTO regenerative thermal oxidizerSAM sulfuric acid mistSCD sulfur chemiluminescent detectorSCR selective catalytic reduction systemSD standard deviationSemi-VOST semivolatile organic compounds sample trainSRM standard reference materialTAP toxic air pollutant
TBD to be determinedTCA thermal conductivity analyzerTCD thermal conductivity detectorTGNENMOC total gaseous non+thane non-methane organic compoundsTGNMOC total gaseous non-methane organic compoundsTGOC total gaseous organic compoundsTHC total hydrocarbonsTIC tentatively identified compoundTO thermal oxidizerTO toxic organic (as in EPA Method TO-15)TPM total particulate matterTSP total suspended particulate matterTTE temporary total enclosureULSD ultra-low sulfur dieselUV ultraviolet radiation rangeVE visible emissionsVOC volatile organic compoundsVOST volatile organic sample trainWC water columnWWTP waste water treatment plant
GP043AS-036878-RT- 1 579 Page 228 of 290
Ag
As
Ba
Be
c
60 lYlgN,I+gLH
silver
arsenic
barium
beryllium
carbonCd cadmiumCdS cadmium sulfide
CH2O formaldehyde
CH3CHO acetaldehyde
CH3OH methanol
CHr methane
CHEMICAL NOMENCLATURE
Se selenium
SOz sulfur dioxide
SOg sulfur trioxide
SO, sulfur oxides
TCDD tetrachlorodibenzodioxinTCDF tetrachlorodibenzofuranTGOC total gaseous organic concentration
THC total hydrocarbons
Tl thallium
TRS total reduced sulfur compounds
Zn
Clz
cl02
co
Co
Coz
Cr
Cu
C2H4O ethylene oxide
CzHo ethane
CaH4O acrolein
CaH6O propionaldehyde
CsHe propane
C6H5OH phenol
chlorine
chlorine dioxide
carbon monoxide
cobalt
carbon dioxide
chromium
copperEtO ethylene oxideEIOH ethylalcohol(ethanol)
hydrogen
water
HzOz hydrogen peroxide
HzS hydrogen sulfide
H2SO4 sulfuric acid
HCI hydrogen chlorideHg mercuryIPA isopropyl alcoholMDI methylene diphyenyl diisocyanate
MeCl2 methylene chloride
MEK methyl ethyl ketone
MeOH methanolMn manganese
nitrogen
ammonia
nickel
nitric oxide
nitrogen dioxide
nitrogen oxides
orygen
P phosphorusPb lead
PCDD polychlorinated dibenzo-p{ioxinsPCDF polychlorinated dibenzofurans
antimony
H2
Hzo
N2
NHs
Ni
NO
Noz
Nq
o2
GP043AS-036878-RT-1579 Page 229 of 290
I,l
ri
Appendix C.2
Manual Test Method QA/QC Data
Qwlity Source Sanpling Slstems & Accessoies
Wind Tunnel Facility:
Probe Type:
Probe lD:
Standard Pitot lD:
Cp(std):
Barometric Press.(in Hg):
Slde:
CalDate: 12-ltar-21
Personnel: DH
Temp ("F):
R.ro ("):
67.0
- 1.8
Cp=Cpo,ilW YoDltt 4.2o/o
o/o Dilf =
'Devlation = l{Cp(s) - AVGCp(s)}l {must be < 0.01}
Standard.deviatioh of the deviations must be less than 0.02 for both sides.
9tLru_lrt- CP @vs-nisn) * 100' CP \ors -to*)
y"Oit"rn""
"t
8ll not exceed +/-3olo.
708 E. Club Blvd., Dwham, North Carolina 27704
G P043AS-036878-RT-is79
' dt',....n
I
| 1.116r- 1.116
0.837
0.835
0.839
0.000
0.002
0.002
!YE!49E_ 0.837
Std deviation 0.002
Pitot Calibration for Method 2G
Environmental Supply Go., lnc.
S-Tube
s2G0{17
001
0.99
29.66
0.838
919-956-9688 FAX: [phone]
Page 231 of 290
.t,
I t
90
90
1.810
1.806
AVERAGE I 0.839
Std deviatlon 0.001
www. environsupply.'com
Quality Source Sampling Systems &Accessories
708 E. Club Blvd-, Durham, ysrth Qarclina !//(N
GP043AS-036878-RT-1579
Environmental Supply Co., lnc.
S-Tube
s2G0117
001
0.99
29.66
CalDate:
Personnel:
Temp ("F):
R"ro ("):
12-Mat-24
DH
67.0
- 1.8
Pitot Calibration for Method 2G
Wind TunnelFacility:
Probe Type:
Probe !D:
Standard Pitot lD:
Cp(std):
Barometric Press.(in Hg):
B€IDE 0.822
Co--Cplsay %Ditf O.4o/o
.Deviation = l{Cp(s) - AyCCp(s)}l (must be < 0.01}
Standard deviation of the deviations must be less than 0.02 for both sides.
% Diff * CP (ns -to'+) - CP @vs -nisn) a ,A0
CP @ug -ton 1
%Difference shall not exceed +/-3%.
919-956-9688 FAX: [phone]
Page 232 of 290
www. environsupply. com
Quality Source Sampling S)tstems & Accessories
708 E. Club Blvd., Durham, North Carclina 277M
GP043AS-036878-RT- 1 579
Environmental Supply Co., lnc.
S-Tube
s2G0135
00't
0.99
29.56
CalDate:
Personnel:
Temp ("F):
R"b ('):
19-Mar-24
DH
69.7
- 0.1
Pitot Calibration for Method 2G
Wind Tunnel Facility:
Probe Type:
Probe lD:
Standard Pitot lD:
Cp(std):
Barometric Press.(in Hg):
Slde:A-SIDE 0.809
o/oDali 0.1o/"
'Deviation = ltCp(s) - AyGCp(g))l {must be < 0.0.1}
Standard deviation of the deviations must be less than 0.02 for both sides.
%Diff - CP @w-tow) - CP @w-r'En) * 100
CP @ug-ton1
%Difference shall not exceed +/-3%.
919-95G9688 FhX: 919-682-0333
Page 233 of 290
www.environsupply. com
Quality Source Samplhg $stems &Accessories
Wind TunnelFacility:
Probe Type:
Probe lD:
Standard Pltot ]D:
Cp(std):
Barometric Press.(in Hg):
B.SIDE
708 E. Club Blvd", Durham, North Caroliura 277C4
cPo43AS-036878-RT-1579 :
Pitot Calibration for Method 2G
Environmental Supply Co., lnc.
S-Tube
s2c0r35
001
0.99
29.56
CalDate:
Personnel:
Temp ("F):
R"ro ("):
19-Mar-24
DH
69.7
- 0.1
(, = C olsnt\o/oDllt 01%
*Deviatlon = ltCp(s) - AyGCp(s))l {must be < O.O1}
. Standard devlation of the deviations must be less than 0.02 for both sides.
%Ditr - CP (*s-ton) - CP @vs-t'isn) *r*
CP (avg -tow )
%Dtffercnce shall not exceed +/-3%.
919-956-9688 HA)k 919-682-0333
Page 234 of 290
60
60
0.002
-0.001
AYE!49E_ 0.807
Std deviation 0.002
www.environzupply.com
EPA Method 5
MeterBox Calibration by Calibratetl Critical Orifice,
Leak Check, and Thermocouple Calibration Check
English Meter Box Units. English K'Factor
Yd:0.9970
TH@:1.782
n.br Bor O?i[c. C.libr.$on
ffiTM Fil !& l.rt [dr. h &d vx{ffi lM h t to ? n rt p& lM lD IE@ C,d V&c6 th. &t
flmtN rDc@Erd*d ( nd b.ilr.lo g4M6r 6r11fi!i)!!(trrtr(MD
a@c&t6l6c t lb.l.dlhr!d4dtudn6drloE 4eBdd
*a6&@. dE@ Y& 6 tu a@ r'r00,
FrEaqEe Fddd{8 hodE.dr.rfurtLut, cE dffih.g3loD rt ch d,
doa dttr ffir d* .(@l*ad&dru a6Fm't! ['r{2
m.b7 8or Plr.rur. Leak Chach nat., Bor vrcuum La.k ch.ck
ll t r 8or Th.rmocouph R.e.lout G.librtuon Chscf
lhc4t-affiHtrh
\z
-t
GP043AS-036878-RT- 1579 Page 235 of 290
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice: Post-Test,
English Meter Box Units, English K' Factor
lurrent Gal. Yd:0.9970
,ost-test Yd:1.0057
,ost-test Result:PASS
Meter Box Orifice Calibration
IMPORTANT For valid test resufts. So Adu.l Vacuum should be 1 to 2 in. Hg greal€rhan the Theoretical Ciltcal Vacuum shM above
IMPORTANT The Crfrical Orffico Coofrcien( K', must b6 ent6r6d in English unib, (if3'(d6g Rf0.t((in.Hg).(min))
_ oRtFtcE _ _ DRY MS METER _
VOLUME VOLUME CALIBRATION FACTOR CALIBRATION FACTOR
For Calibation Fador Y, he rato ofhs reading of th6 calibatioo mde. to tho dry gas met€r,
acceptabletol6rance ol indtuiduel valu6 from h6 average is }rc.02.
For Odf,c€ Calibation FactordH@, S6 orfic€ dilerentiat pr$sure in inches ofH2O hat equetos to O 75 ch ofair
at68 F and 29 92 inch€s of Hg, accepbbletol€Ence of individuat vatue6 iom th€ av€rage is +/4.2.
QA Crlterla:
AveEoe Yd I 0057
AHlA 1 7613
Variation of Yd's PASS
Variation of AH/a PASS
Vecuum Crilaria
dH Net outst s6rietr Coeffcient lnitial
s1c o /o19
210 61 6A
6a
Meter Box Vacuum Leak Check
T..tvrdnrm /i^ H6l
0
adjusl vaM€ tully open, fin6 adjust tully closed, sampte intei ptugged
b6zero (reter dialshbl6 for l minde)
GP043AS-035878-RT- 1s79
M6br box posltsst calabBton fom (orifices) R3
Page 236 of 290
M()N ll{()\l
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice,
Leak Check, and Thermocouple Calibration Check
English Meter Box Units, English K' Factor
Yd:0.9867
AH@:1.867
1r.67 in. Hg
Meter Box Orifice Calibration
IMPORTANT forv.Etd 6.u[.,|h AdElVrdum.tuSb 1 b 2 h. H9g.rl.rh.n lh. tuoEtialC,lialV&uum.hom.bove
IMPoRTANT n. qilbd Odft. Co.fident, K, md b.d.d in Engls untr, (tfs'(eg R)t.t((in.H!)'(man)).
For dhlbn F.dor Y,lh r.iio orlh. ru.dlne otlh alibnlbn m.brlo th. dry S. nd.r,
.@ph*toEdn@ orhdtoEdvrh.. hm lb.v.r.g. L +4.02-
For Otu C.lihton F.dorde, th. odi6 dir.r.ilhl prsuE in ind.! ol H20h.l.qu.t..to 0.75ch ol.,
.168 F.nd A.9hch.. olH9, ropiatr bhEna olhdilEolvilu.. tum lh.v.ng. ts irc.2.
CIA Cdl.dr:
o 9s7
Aver.oc AH@ 't,8671
(cu n)
Met6r Box Prcs3ure Leak Check Meter Box Vacuum Leak Chack
Should b. t7 in. HrO
0
rdJ$l v.lv. tuly op.n, frn. rdjud lury do$d, Empb el dqg.d
Mud Ez.o (m.nom.l.rbv.ldaM br 1 mhd.)
Meter Box Thermocoupla Readout Celibr.tion Chock
Thllmdph rtuhd
'R..dln! vll$t md h wilhln 1.5r olr.l.r.nc. rh.mom.brvdus (hedon.tuld. t mFdtor. sh) bralbdbn to E aoq.*.
Hrgn
32
6a a 60
tt1
350
14
7m 17
GP043AS-036878-RT- 1579 M.br bx hon6 6rPdgebgg9itstr290
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice: Post-Test,
English Meter Box Units, English K' Factor
Meter Box Orifice Galibration
IMPORTANT Forvalid test resulb, th6 Adual Vacuum should be 1 to 2 in. Hg greal6rthan the Th6or6tical Criical Vacuum shM sbovo
IMPORTANT The Crdcal Oiic6 Co.ftcient, X', must be entered in English unfrs, (fi)^3'(deg Rf0.5((in.Hg).(min)).
For Calibration Fador Y, the 6tio olthe rcading otthe @librdion m6ter to the dry gas heter,
acc€ptable tohance ofindiladu.l valu.s from ths.v6Bge i. +/4.02-
For Orific€ Calibratjon FadorAH@, th€ orifce differential prossur6 in inches ofH20 hatquates to 0.75 ch ofai
at 68 F end 29.92 inches ofH9, acc6pt.bletol66nce ofindilidual values from th6 av.6g6 is +/4.2.
rm0s.
AH lnhial htet omd lnbt oiltat scnaF Co6ffci6d lnfial Final
Meter Box Vacuum Leak Check
Coarce adjustvalve tu|ly open, fin6 adju3t fully closod, samplo inlet plugged
Must be zero (mter di8lsbbh for 1 minde)
Poformed by: Nam6
Approved by: Namo
Date:..'.'....- 45022.00
Dete:
GPO436-036373-RT-l s79
UETHOD 5 CruNCAL ORIFEE CALIBRANON
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GP043AS-036878-RT.1579
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oafl, Gaet arattE{affi
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t(llt lltfKluM(mm llellmtn.ll - il.Hc.Llb|tunlt3
t(mrtfl(tuflt(nm Hql(mln)l . ltt ta Untb
COlnl.
Page 239 of 290
ol .t ia -ao/TI aa.a at ttt
ru il
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d!ntotltr,0.4 D..il.t
t! Ia ,at
aa.l tt.a ,0.t ,l-l ?1..1
I ra
Appendix C.3
Instrumental Test Method QAIQC Data
t:,. .n a
.:lr-.. .!r,t, !r:ti l- r' { t- ?r,,'.,i;'
GP043AS-036878-RT-1579 page 240 of 290
0 rt
Appendix C.3.1
Unit 1
tl
| / .^ r r-aa . a .t - .,
GP043AS-035878-RT-1579 Page 241 of 290
PROJ-036878
PacifiCorp
Huntington Unit 1
413012024
Gas
Coz
Level
Low
Mid
High
Low
Mid
High
Low
Mid
High
Low
Mid
High
Cylinder lD
ZERO
E80141006
E80156888
ZERO
cc273758
DTo008969
ZERO
DT0038012
cc323381
ZERO
cc4100s6
cc323381
Sor
NO,
<2%<SYo or
t 0.5 ppm
Calibration Error Tests lnitial System Bias Check
Gas
Value
Analyzer Calibration
Error
o.6%
1.0%
L.2%
0.4%
o.2%
L.8%
o.t%
o.t%
0.9Yo
O.2Yo
0.2%
0.L/o
Analyzer
Response
System
Bias
0.0%
0.OYo
Q.0Yo
o.o%
0.0%
o.oYo
0.0/o
0.0Yo
0
8.925
t7.82
0
26.88
49.9
0
L70
33L.4
0
I44.5
328.3
0.1
9.1
L7.6
-o.2
26.8
s0.8
-0.3
L70.3
334.3
o.7
t45.t
328
0.1
9.1
-0.2
26.8
-0.3
170.3
0.7
t4s.r
GP043AS-036878-RT- 1 579 Page 242 of 29O
PROJ-O36878
PacifiCorp
Huntington Unit 1
4l30l2024
Level
Low
Mid
High
Low
Mid
High
Low
Mid
High
Low
Mid
High
Gas
Coz
Soz
NO,
<2%<5% or
t 0.5 ppm
Callbration Error Tests lnitial System Bias Check
Gas
Value
Analyzer Calibratlon
Error
0.6%
t.OYo
l.2Yo
o.4Yo
0.2/o
t.8Yo
O.1/o
0.L%
os%
O.2Yo
0.2%
o.L%
Analyzer
Response
System
Bias
o.o%
o.0%
O.O/o
o.0%
O.OYo
0.o%
O.OYo
O.OYo
0
8.925
17.82
0
26.88
49.9
0
L70
331.4
0
L44.5
328.3
0.1
9.1
17.6
-o.2
26.8
50.8
-0.3
770.3
334.3
0.7
145.1
328
0.1
9.1
-0.2
26.8
-0.3
170.3
0.7
r45.1
GP043AS-036878-RT-1579 Page 243 of 290
htu.&n&Od.dOfrl,.tfc
th^rm !s
iun 6dh
SrU
hntc kd bot d
iu. r-o 21
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ffi &d hot ot
hnm lr*
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hM kd hol c.t
Page 244 ol 29OGP043AS-036878-RT- 1579
GP043AS-036878-RT- 1579 Page 245 ol 290
1l
I
I
PROJ-036878
PaclflGorp
Huntingon Unlt 1
4l?Ol2O24
EPA Method 7E 916.2.2
NO2 to NO Converter Efficiency Test
Time t{O, ppm
4/3O12420:L9;O3 43.3
4l30l2420:t9:r3 43.7
4l3Ol242O:L9:23 43.9
4/3012420:19:33 44.2
4l3Ol2420zl9:43 44.5
41301242O:19t53 44.6
413012420:2O:03 44.8
4/3O12420:20:73 44.9
4/3O12420:20:23 44.9
4/30/2420:20:33 45.4
4/30/2420:20:43 45.3
4/301242Ot2O:sl 45.7
4/30/2420:2L:A3 45.6
4/30/242O:2L:13 45.6
4130/2420:21:23 45.7
4l3O/2420:2L:33 45.6
4/301242O:2L:43 45.9
NO, nopo,tr.
No.t v"tr.
Converter Efflclency
Llmit
45.9
8.42
9s%
>9(m
G P043AS-036878-RT- 1 579
t
Page 246 of 290
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4/30124 l4:L8:L4
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4/30/24 t4:19:O4
4130124 14:t9:14
4l30l24 l4:L9t24
4130124 l4:L9:34
4l3il24 l4:Lgt44
4l30l24 14:19:54
4/30/2a L4:2O:O4
4130124 l4:2O:L4
4l3ql24 L4t2O:24
4l3Ol24 L4t2O234
4130124 L4:20:M
4130/24 L4t2O:54
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4/3Q124 14:21:14
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4l3O/24 L4:2L:34
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4l?o124 L4:2L:54
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4l30l2414:22124
4130124 L4:22:34
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4130124 L4:23:24
4/30124 14:23:34
4l3Ol24 L4:23:44
4130124 L4:73:54
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4130174 L4:24:L4
4130lZ4 L4:24t24
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4130/24 L4:24:44
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4130124 L4:25:14
4130124 14:25:24
4/3A124 L4:25:34
4130124 14:25:44
4130124 L4:25154
0.1
0.1
0.1
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0.1
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0.1
0.1
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2.4
5.8
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15.0
15.4
15.4
15.0
L7.8
L7.9
18.0
18.0
L7.9
18.3
18.1
L7.7
t7.6
L7.5
17,6
L7.6
L7.7
17.7
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17.6
t7.6
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t7.6
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17.6
t7.7
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o.2
2.9
10.9
2r.5
31.6
36.6
39.5
41.4
43.2
43.9
44.6
45.1
45.5
45.5
45.7
49.4
50.5
s0.6
50.9
s0,8
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-o.2 2.L
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4.4 0.4
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-0.3 -0.2
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-0.3 0.9
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37.7 1.9
228.2 34.3
381.0 102.5
GP043AS-036878-RT- 1 579 Page 247 of 290
4l30l24 14:25:04
4/30124 t4:26:r4
413012414:26:24
4l3o/24 14:26:34
4l3o/2474:26:M
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4l3o/2414:27:W
4/3012414:27:14
4/30/24 L4:27:24
4130/24 L4:27:34
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4130124 L4:27:54
4l3Ol24 !4:28:04
4130/24 t4:28:L4
4/30/24 14:28:24
4130124 t4:28:34
4/30/24 14:28r44
4/30124 14:28:54
4/30124 74:29:04
4130124 14:29:14
4/30124 14:29:24
4130/24 t4:29:34
4/30/2414:29:M
4130124 L4:29:54
4/30/24 t4:3o:04
4130124 L43o:r4
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4130124 L4:30:34
4/30124 74:3O:M
4/3012414:10:54
4/30124 L4:31:O4
4130124 l4:3L:L4
4130/2414:31:74
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4130/24 L4:3L:44
4130124 L4:3L:54
4/30/2414:32:04
4130/24 l4:32:L4
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4/30/2414:36:04
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4/3O/24 L4:36:34
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4/30/2414:36:54
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4/30/24 L4:37:L4
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4/30/24 L4:37:44
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22.4 385.0 200.1
L4.7 389.5 284.t
10.5 389.5 337.2
7.6 389.6 3s9.8
6.3 367.4 35s.8
4.7 334.1 367.4
3.8 333.9 359.0
3.4 334.0 332.7
2.9 334.0 327.9
2.7 334.1 327.2
2.4 334.0 326.9
2.2 334.s 325.7
2.3 3:14.5 321.8
2.4 3:t4.1 ?28.2
2.2 3:t4.3 329.3
2.L 334.2 t27.5
2.4 333.8
'27.72.O 333.4 326.7
1.8 333.7 327.3
2.0 333.9 327,2
1.9 333.7 326.5
2.5 300.4 317.9
6.1 L52.4 281.3
17.7 4.9 213,t
L7.7 3.2 L28.2
2t.3 L.7 61.1
23.t 1.1 2L.7
24.3 0.8 4.4
25.2 0.6 -0.4
25.8 0.6 -L.2
26.6 0.5 -0.9
26.2. 0.3 0.4
26.7 0.4 l.s
26.3 0.4 3.0
25.8 0.4 2.2
26.6 0.1 L.2
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26.9 0.3 0.7
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20.5 101.2 1.1
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100.9 -s.3
168.1 -4.6
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169.4 -1.1
159.5 -0.5
169.s .r.1
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159.3 -2.9
159.5 -3.0
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3.7 40.6
1.9 79,4
0.5 111.8
0.3 L32,7
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-0.3 142.7
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t4.L 168.4 -3.8
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t.6 169.5 -2.4
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6.7 0.0 -3.2
4.0 -0.5 -6.8
2.t 4.2 -6.4
1.0 -0.3 -7.4
0.6 .0.3 -s.0
0.3 -0.2 4.8
0.3 {.1 -5.0
0.2 -o.L -5.7
4.2 -0.3 -6.8
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0.1 94.7 -7.3
0.2 149.s -6.3
0.4 161.0 -6.6
0.4 t69.2 -3.5
0.5 169.3 -4.5
0.7 L69.7 -3.9
0.8 L70.r -3.9
0.7 169.7 -3.9
0.6 170.0 -3.5
0.6 t69.7 -4.3
o.7 169.6 -3.8
0.7 169.3 -t.7
0.6 169.5 4.2
o.7 169.9 -3.2
0.6 L70.0 -r.7
0.5 144.9 11.0
0.2 60.s 38.0
0.1 1.1 74.9
4.2 0.6 108.5
0.0 0.4 129.5
4.2 0.2 139.3
-0.2 0.2 1tt{r.6
0.0 0.0 140.7
-0.1 0.0 138.1
-0.3 -0.1 141.0
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0.1 4.2 L42.6
0.1 -o.4 140.8
0.0 {.3 140.9
-0.3 -0.2 L41.3
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-0.3 -0.4 141.0
0.3 -0.3 137.0
3.0 -0.3 L22.4
8.9 {.3 92.6
15.5 -0.3 55.2
20.3 -0.3 24.6
22.5 -0.4 6.3
24.1 -0.3 -1,4
25.4 -O.2 -4.0
25.7 -0.5 -4.4
26.1 -0.3 -2.6
26.4 -0.4 -1.5
25.5 -0.5 -O.7
27.5 -0.4 -2.O
27.2 -0.6 -3.7
27.O -O.2 -3.9
26.7 -0.4 -3.3
GP043AS-036878-RT- 1 5 79 Page 258 of 290
Appendix C,3.2
Unit 2
PROJ-036878
PacifiCorp
Huntington Unit 2
4lttl2o24
Gas
coz
Level
Low
Mid
High
Low
Mid
High
Low
Mid
High
Low
Mid
High
Cylinder lD
ZERO
E80141006
E80156888
ZERO
cc273758
xc0243938
ZERO
cc344703
cc323381
ZERO
cc344703
cc323381
Soz
co
Calibration Error Tests lnitial System Bias Check
Gas
Value
Analyzer Calibration
Error
O.0Yo
o.4%
t.2%
0.3Yo
o.3%
L.L%
O.|Yo
0.4%
o.s%
0.2%
0.4%
0.t%
Analyzer
Response
System
Bias
0.O/o
0.0/o
0.OYo
0.o%
O.OYo
0.OYo
0.Oo/o
O.Oo/o
0
8.925
L7.82
0
26.88
63.53
0
152.3
331.4
0
151.8
328.3
0
9
L7.6
-o.2
26.7
64.2
-0.3
151
332.9
-0.5
153.1
328.1
0
9
-0.2
26.7
-0.3
151
-0.5
153.1
<5% or
t 0.5 ppm
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Time
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Time
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GP043AS-036878-RT- 1 579 Page 266 of 290
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GP043AS-036878-RT-1579 Page 267 of 290
Time
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4hll24L7:OO:57
4/ttl24 L7:OL:O7
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GP043AS-036878-RT- 1 579 Page 268 of 290
Time
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41fi124 t73a:o7
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GP043AS-036878-RT-1579 Page 270 of 290
Time
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4l7ll24 L8:4LtO7
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G P043AS-036878-RT- 1 579 Page 27L of 290
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417U2419:2s:27
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4/tL/24 L9:3L:17
4/t7/24 L9:3L:27
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GP043AS-036878- RT- 1 579 Page 272 of 290
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Time
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4/tl./2420:05:47
co2 502 coNOx
GP043AS-036878-RT- 1 579 Page 273 of 290
l
PROJ-036878
PaciftCorp
Huntlntton Unit 2
4lL7l2A24
EPA Method 7E 516.2.2
NO2 to NO Converter Efflciency Test
Time NOr ppm
4/tL12420:09:27
4lrtl242O:O9:37
4ltt/2420t09147
4/tt/242O:09:57
4/LU2420:1O:o7
4/tU2420:L0:L7
4/tLl242Ot1Ot27
4/ltl2420:10:37
4/rt/242Ot10:47
41L1./242.O:lO:57
4/rt/242A:tL:07
4/tLl242O:Ll:t7
ilQn.p*
NOzcon**t*
Converter Efficlency
Llmit
44.t
44.4
M.6
44.6
M.9
44.7
44.7
M.5
44.9
44.7
44.7
4.9
u.9
44.4
9396
>90x
Page 274 of 290GP043AS-036878-RT- 1579
Appendix C,4
Calibration Gas Certificates
CERTIFICATE OF AI\IALYSIS
Grade of Product: EPA PROTOCOL STAI\DARI)
Part Number:E03N180E15A0015
CylinderNumber: EB0141006
124 - Tooele (SAP) - UT
872023
CO2,02,BALN
Airgas
an Air Uquide company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, Ul[ 84o74
Airgas.com
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
1 53-402892933-1
1s0.0 cF
2015 PS|G
590
Nov 14,2023
Expiration Date: Nov 14.2031
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EpA
600/R-121531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. tnis iylinOer has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
CARBON DIOXIDE
OXYGEN
NITROGEN
Lot lD
9.000 %
10.50 %
Balance
8.925 yo
10.47 o/o
7.489 O/O CARBON DIOXIDE/NITROGEN
,12,05 O/O OXYGEN/NITROGEN
ANALYTI CAL EQI.IIPM EI{T
Analytical Principle Last Multipoint Calibration
+l- 1.0o/o NIST Traceable
+l- 0.8o/o NIST Traceable
0.6%
0.70/o
Date
May 14,2025
Dec 14,2023
'11t14t2023
1111412023
CALIBRATION STANDARDS
Cylinder No Concentration
NTRM
NTRM
1306041 1
98051 01 0
cc413537
SG916,I286BAL
InstrumenUMake/Model
Triad Data Available Upon Request
Sionature on file
Approved for Release
G P043AS-036878-RT- 1 579
ANALYTICAL RESULTS
Actual ProtocolGoncentration Method
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
CO2 NDIR (Dixon)Ocl 17,2023
od 17,2023
Page 1 of 1
Page 276 of 290
Aitga$.
an Air Liquitb company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
EPA PROTOCOL
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Auq 08.2030
STAIYDARD
153-402506334-1
158.0 CF
2015 PSIG
590
4u908,2022
Expiration Date:
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certiflcation of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12/531, using the assay procedur$ listed. Analytical Methodology does not require conection for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 957o. Th6re are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
molet/mole basis unless otherwise noted. The resulE relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below 100 Dsio. i.e. 0.7
17.82 o/o
21.',t9 0/o
G1
G1
Type Lot lD Cylinder No
CALIBRATION STAIVDARDS
Concentration
24.04 o/o CARBON DIOXIDE/NITROGEN
22.53 O/O OXYGEN/NITROGEN
NTRM
NTRM
13060802
09061434
cc4't5397
cc282492
Date
Dec 11, 2025
May 13,2025
CERTIFICATE OF AI{ALYS$
Grade of Product:
E03Nt61E15A0287
EB01 56888
124 - Tooele (SAP) - UT
872022
C02,02,BALN
AIVALYTICAL RESULTS
Actual ProtocolConcentration Method
ANALYTICAL EQTIIPMENT
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
Ju!20,2022
Jul20,2022
Triad Data Available Upon Request
Sianafura on flla
Approved for Release
GP043AS-036878-RT- 1 579
Page 1 of1
Page 277 of 290
CERTIFICATE OF AI\ALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
Part Number:E02N199E15A1190
Cylinder Number: CC273758
Laboratory:124 - Tooele (SAP) - UT
PGVP Number: 872023
Gas Code:
Aitgas.
an Air LQuide corparry
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
Reference Number:
CylinderVolume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
1 53-40283361 3-1
144.0 CF
2015 PS|G
660
Sep 06, 2023SO2,BALN
Expiration Date: Sep 06, 2027
Certification performed in accordance with "EPA Traceability Probcol fror Assay and Certification of Gaseous Calibration Standards (May 2012)' document EpA
600/R-121531, using the assay proceduree listed. Analytical Methodology does not require correction for analWcal interference. This cylinder has a total analytical
uncertainty as stated below with a crnfidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
Triad Data Available Upon Request
Sionature on fila
Approved for Release
G P043AS-036878-RT- 1 5 79
Page 1 of1
Page 278 of 290
mole/mole basis unless otheMise noted. The results relate only b the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
NOt Uge lhrs bolo\,v 100 psig, i.e.
Component Requested
Concentration
ANALYTICAL RESULTS
Actual Protocol Total Relative
Concentration Method Uncertainty
Assay
Dates
SULFUR DIOXIDE 26.00 PPM 26.88 PPM G1 +l- O.8o/o NIST Traceable OBt3Ol2O23, OgtOOt2O23
NITROGEN Balance
CALIBRATION STAIVDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
GMIS 07212022A105 E80141121 49.88 PPM SULFUR D|OX|DE/N|TROGEN 0.70/0 Dec21,2026
lnstrumenUMake/Model
ANALYTICAL EQUIPMENT
Analytical Principle Last Multipoint Calibration
Nicolet iS50 AUP2010228 SO2 LSO2 Aius23,2023FTIR
:::,flPRAXNN
Molegarfuarrwe pfufrE
Docl{umbon /31&OG
Pruelr Dlrt{buton, lnc.
5100 8. Alameda Sfeet
Loo Angolec GA 9005E
Tcl: 323-585-2lEl
Fax: 7t4.612-66E9
. PGIrP lD: F22021
Ctfutts&.Ordcrl$ordon
PRAMIR PKG PROT/O UT }IS
1Al SNo$iln LPl$r/Y
PRC^/OUT8/lqEall,.
O.r&a6!tin E A0[ gll11l&1
MtOtErUneTfl$&
Plrr rvurroc Nl sD6ilaE{S
OrdurEr PO l'n,'tu 7gf4olgt
f,Dr&jgl&Uxnl
lnNw,Dr.l@11a12
Ol,rGrSoltAOerAS CGA660
cyffifPt84/..N Ydn t 2mp.E 110m
Concentdon
o7Arymzg
CYlrder Numbec DT0oo896g Epaltded Unceltainty
49.0 ppm sultur dloxlde t 0.3 PPm
B.hncs NlUogen
CenSkdon Infontdion:c,,fifrc€tbn Datc:O7l14n@1 forn.' 96 Months Explntlm Dab:07l14nwg
Il$€rtHlrwcaflf.d.ocodngbt!2012EP TrEdIUPrcbol.Darr!.tllEP &r&1431,uthg-Eloduncl.thatdiyer|bae.l...da..b.dtl..rPrl.hd
urEdEfrly a. hrd dconlldaco-drpprodntly e$,. xfi ! aourqrl$rk.2" Do Nd uro tt{. St d.rd f Pn rn b lEOfli 10O P€lG.
AnOlyttCOl Dda: (R'm'!,'osts"cftl, ziza'Dctt' crort Gm(hb,
f, CqPCItrt Sunlroodd. Rjtr!|c.Sllldrrf: Typcr6ffi(brfi GilISTOIqZCDE
nrtrOl rqqrO flCf candOothr ircrtcltl.rPliilc rn{itrFfo.imd, ur m!ts rE[rfrtyd]dFsrtt[onrrbh.rttsbuydfh.lqtdthclnlbrmr[m-torml Purpn-no
.atlr hfqltLlal cdhad lsth ocidft. Ec rdlbfh.dlUFotidt! adr ffimdoo.
Rr$.i dconanffit 60Fn
Crubdoo.Ertrldr 4g.gppllr
lnatumantt tad Amd( ghCE Eil A\ir{z1.ssat
Arafdcd tadroc Wsp.clrcm*y
l-dMult oanlcdD.dott (,,llStiE}l
C0.tcrflonrl,trc!.t hV So.ePpmro,g PPm
EgruonDna 6mm$
Tnc..Db to: SRil r/ S.mCc il, Oyln(kt SRl, l8&!., 6+{31 I FT2s,fo' 8R f @ErHon (slru,lh uit ), 6o.2t ppm , ii 028 ppm
snredrfrh-ffi oarzrwa
Z, 0 R 5(I7. Cr 49.9
It 60.8 Z 0 C! 50
Z o C: ag.g R: 60.7
z:. .0. .- ft gtz----.C:-.Je,9.--. Conc: ll9.0
R: qr.c zr o e 50 com 50
L. o G 4e.e R: CO7 cffi: 49.e
lroit rgr L.rT..aLry 50
GP043AS-036879-RT- 1 579 Page 279 of 29O
AitUas.
an Air Liquide conpany
Airgas Specialty Gases
Airgas USA LLC
5zS North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number: XC0243938
Laboratory:124 -fooele (SAP) - UT
PGVP Number: 872023
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402735091-1
144.0 CF
2015 PS|G
660
May 15,2023
CERTIFICATE OF AI{ALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
E02Nt99E15A1827
SO2,BALN
Expiration Date: Mav iS.2031
Certification performed in accordance with "EPA Traceability Probcol for Assay and Certification of Gaseous Calibration Standards (May 2012)' document gFA
600/R-1 2/531 , using the assay procedures listed. Analytical Methodology does not requir€ correction for analytical interference. This cylirider nas a total analytical
unoertainty as stated below with a confidence level of 957o. There are no signmcant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otheMise noted. The results relate only b the items tBted. The report shall not be reproduced except in full without approval of the laboratory. Do
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036878-RT- 1 579
NOt Use lnrs below 100 psig, i.e. 0.
Component Requested
Concentration
ANALYTICAL RESULTS
Actual Protocol Total Relative
Concentration Method Uncertainty
Assay
Dates
SULFUR DIOXIDE 63.00 PPM 63.53 PPM G1 +l- 1.4o/o NIST Traceable O5lOgt2O23, OStlSlzO2ZNITROGEN Balance
CALIBRATION STAIVDARDSfVpC Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM 16010215 KALOO3621 97.69 PPM SULFUR DIOXIDE/NITROGEN O.8O/O Nov 01, 2027
lnstrumenUMake/Model
AIVALYTI CAL EQTIIPMENT
Analytlcal Principle Last Multipoint Calibration
Nicolet iS50 AUP2010228 SO2 MSO2 FTIR Mav 02.2023
Page I of I
Page 280 of 290
Airuas.
an Ak Liquicle compay
Airgas SpecialtyGases
Airgas USALLC
5zS North Industrial loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402249456-1A
'144.3 CF
2015 PS|G
660
Nov 01,2021
Expiration Date: Nov 01.2029
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certitication of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require conection for analytical interference. This cyinder has a total analytical
unc€rtainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036878-RT- 1 579
Page 1 of 1534022'19456-lA
Page 281 of 290
CERTIFICATE OF AIYALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
E03N199E15A4118
E80107014
124 -Tooele (SAP) - UT
872021
CO,NO,NOX,BALN
mole/mole basis unless otherwise noted.
Concentration Concentration Method Uncertainty
NOX 62.00 PPM 62.93 PPM G1 +l- 1.1o/o NIST Traceable 1012512021 , 1110112021
CARBON MONOXIDE 62.00 PPM 62.56 PPM G1 +l-0.7o/o N|STTraceable 1012512021
NITRIC OXIDE 62.00 PPM 62.88 PPM Gl +l- 1 .1o/o NIST Traceable 1012512021 , 111012021
NITROGEN Balance
CALIBRATI ON STAI{DARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM 12011236
PRM 12386
NTRM 20061042
GM|S 401648675102
The SRM, PRM or RGM not6d above is
KALOO4576 49.24PPMCARBONMONOXIDE/NITROGEN
D685025 9.91 PPM NITROGEN DIOXIDE/AIR
cc733400 98.61 PPM NtTRtC OXTDE/N|TROGEN
CC5OO959 5.074 PPM NITROGEN DIOXIDSNITROGEN
in reference to the GMIS used in the assav and not oart of the
0.6o/o
2.0o/o
0.9%
21%
Au131,2024
Feb 20,2020
Oct 06, 2026
Feb 01, 2023
ANALYTICAL EQTIIPMENT
Analytical Principle
Nicolet iS50 4UP2O10228 CO LCO
Nicolet iS50 AUP2010228 NO LNO
FTIR
FTIR
FTIR NO2
ocr13,2021
oct20,2021
ocr20,2021
Aiuas.
an Ar Liqui& company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Grade of Product: EPA PROTOCOL STAIYDARI)
E02Nt99E15AC639
CERTIFICATE OF ANALYSIS
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402299373-1
144.3 CF
2015 PS|G
350
Dec 14,2021
CylinderNumber: CC410056
Laboratory:124 - Tooele (SAP) - UT
PGVP Number: 872021
Gas Code:CO,BALN
Expiration Date: Dec i4,2029
Certification performed in accordance with "EPA Traceability Protocol for A$ay and Certification of Gaseous Calibration Standards (May 2012)' document EpA
600/R-121531, using the assay procedures listed. Analytical Methodology does not require conection for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affec{ the use of this calibration mixture. All concsntrations are on a
mole/mole basis unless otherwise noted. The results relate only b the items tgstBd. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder belofl 100 psig, i.e. 0.7
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036878-RT- 1 579
Page I of 1
Page 282 of 290
AIVALYTICAL RESULTSActual ProtocolConcentration Method
CARBON MONOXIDE 145.0 PPM 144.5 PPM G1 +t- 0.6% N|ST Traceabte 12t14t2021
NITROGEN Balance
CALIBRATION STAIVDARDS
No Concentration
NTRM 09010252 KAL004920 98.48 PPM CARBON MONOXIDE/NITROGEN O.5o/o ocl16,2024
ANALYTICAL EQUIPMENT
Nicolet iS50 AUP2010228 CO LCO FTIR Dec 08, 2021
Aituas.
an Air Lquid€ cornpeny
Airgas Specialty Gases
Airgas USA LLC
SzS North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402645362-1
144.0 CF
2015 PS|G
660
Jan 30,2023
Expiration Date: Jan 30.2031
Certmcation performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a btal analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this celibration mixture. All concentrations are on a
mole/mole basis unle8s otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036878-RT- 1 579
Page 1 of I
Page 283 of 290
CERTIFICATE OF AIYALYSrc
Grade of Product: EPA PROTOCOL STAI{DARI)
E03Nt99E1540353
cc344703
124 -Tooele (SAP) - UT
872023
CO,NO,NOX,BALN
6NOt USe Inrs below 100
Component Requested
Concentration
AIYALYTICAL RESULTS
Actual Protocol Tota! Relative
Concentration Method Uncertainty
Assay
Dates
NOX 150.0 PPM 152.3 PPM G1 +l- 1.0o/o NIST Traceable 0112312023,0113012023
CARBON MONOXIDE 150.0 PPM 151.8 PPM Gl +l-0.60/o NIST Traceable 0112312023
NITRIC OXIDE 150.0 PPM 152.3 PPM G1 +l- 1.0o/o NIST Traceable 0112312023,0113012023
NITROGEN Balance
CALIBRATION STAIVDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
KALOO4835 98.48 PPM CARBON MONOXIDE/NITROGEN O,5O/O od 16,2024
Feb 17 ,2023
Oct 06, 2026
Jun 15,2025
NTRM 09010226
PRM 12409
NTRM 2006'1057
GMIS 1534012021103
15.01 PPM NITROGEN DIOXIDSAIR 1.5O/O
98.61 PPM NITRIC OXIDE/NITROGEN 0,9%
4.956 PPM NITROGEN DIOXIDE/NITROGEN 1.60/O
D913660
cc73u82
ND73012
The SRM, NTRM. PRM. or RGM noted above is onlv in reference to the GMIS used in the a$av and not Dart of the analvsis.
ANALYTICAL EQIIIPMENT
Analytical PrinciplelnstrumenUMake/Model Last Multipoint Calibration
Nicolet iS50 AUP2010228 CO LCO
Nicolet iS50 AUP2010228 NO LNO
Nicolet iS50 AUP20'10228 NO2 impurity
Jan 05, 2023
Jan 25,2023
Jan 25,2023
FTIR
FTIR
FTIR NO2 impurity
!.lc'ilnn our r lfld
:notu Pm':!l(i'vL
Docilumben 1ili113
Llndo Gar I Egulpmont lnc.
5700 E. Alrmcd. Sret
Lor Ang*r CA 9ooltt
TcL 323€l!t{154
Frr: 7l4.54il66tg
PGI/P !D: FiZl022
CERNFICATE OF ANALYSN /EPA PROTOCOL GAS
Ctdons& Oilalnlctdoa
LCEPIGPrcVO UTHS
r2'lt I rNDt STRI^L PI(WV
PRoro UT l.L0a-a138
R.q-bdCondrffir:
c.rtlcd CoEnhloi:
hdurrilthcd:
AnrUtEllrdrod:
lldrAt$olnlC.mn:
tt6mm
tru ppfir
Ctmilfihocdr
wt2oa2
PruSpec EZ Cat
E&ftI*ILHEE
For Rcfucttcc
Cettfudon lafornotbn:Ccrfr'ftpitim W:O$172A?2 lena; 06 Monthe Erpln&ltr Datc: 051 17 EA30
ThLcrh(brtcJtlrdrEdil{b|h.2012EP TnablBFrsb6l,D6urnrnttEP 40o,R.rz63l.urlltPmccdurGl.UnanlrlntyrbovrbGprad-.brdub.seud.d
mc.rLlnv.l r bvd of ao.illlhn6 otappEdnrbly 5l3 ulh r olrr.e! Loa.? k. Z Do Xol l.L qrnd.d f Pltl.ul! L llI h..r f ooPslc.
AnaMbalData: (R"8t,bD?c'sirta'd,zrzmot+crotto'r'lcbJ
f . OqPorrl' ,{ttdH. Rtr66o!ffid: Tygrlgylhrhrfi
ClrfrtIr-ED.b GAllMl
Lffiffit*4/r,,/|. ZDslalit
Fart lirna.r: ill NOttEi\S
c,tuilrcl{4,,0'r.gfloftr1a1
F,olEutut?gzz
Loafrrrs.? ilxttfizlla!
clzrhdrg0lttolrtrAs CGAO
CrcPr'',,rrJn Yunr] fimplC'lllotE
Grcardml06l
216 pFrll pPtr
G,Il/?I,lc
r0!5b ,4&.1-lt , CAL017t0a
zlt, peitrrl.l ppn
lEmr2m0
Oclcltnrlhr
^rnarbhtr:ElQfenod :
TrrE .lI5! SRUI, s.,n?hll gyhrtlf*
sRU Corsrtr[o.r / Unarrhv
SRUErpkrlbrh:
ol [r ux of th. lrlbnnruon ottrhd honln rxcd t]r f.r oOtllrnrd for proY|Ore ]rdr lffinrbn.
Dd.
Z. 0 R 255 C: 17O Gom: l7l,
R: 26 *, 0 C3 l6ei co.E 17L
Z 0 C lf.t 13 265 Com: lm
UOf,: ptl LmTrtAtrry: 17tl tm
d,^lL,
AnrltE d By
05n7rloto
DT003t0tz
170 ppm
Behnco
Nllrlc orldc
Nlbogcn
L, 0 E 265 O: 160.? GoG! l7ll
R3 255 Z 'O c: l09l CoE: l7O
Z't 0 G: lo,E R: 6 CoB: l7o
UOll: pm LrnTrt^.raf lm Fn
GP043AS-036878-RT- 1 579 Page 284 of 290
Airgas.
an Air Uquide cornpany
Airgas Specialty Gases
Airgas USA LLC
sz5 North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OF AI\IALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
E03Nt99E15404S6
cc323381
124 -Tooele (SAP) - UT
872022
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402396220-1
144.0 CF
2015 PSIG
660
Apr 04,2022
Expiration Date: Apr 04. 2030
Certification performed in accordance with 'EPA Tracoability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require conection for analytical interference. This cylinder has a btal analytical
uncertainty as stated below with a confidence level of 950/0. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
Triad Data Available Upon Request
Sionatura on fila
Approved for Release
GP043AS-036878-RT- 1579
Page I of I
Page 285 of 290
mole/mole basis unless otherwise noted.
USE ThiS below 100 Dsio. i.e. 0.
ANALYTICAL RESULTS
Actual Protocol Total RelativeComponentRequested
Concentration
Assay
DatesConcentrationMethod Uncertainty
NOX 330.0 PPM 331 .9 PPM G1 +l- 1.2oh NIST Traceable 0312812022, 0410412022
CARBON MONOXIDE 330.0 PPM 328.3 PPM Gl +l-0.5o/o N|STTraceable 0312812022
NITRIC OXIDE 330.0 PPM 331 .4 PPM G1 +l- 1.1o/o NIST Traceable 0312812022, 0410412022
MTROGEN Balance
CALIBRATION STANDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
Feb 13, 2026
Feb 02,2022
Oct 19, 2026
Apr 30,2024
NTRM 14060359
PRM 12395
NTRM 20060321
GMIS 1534002020104
CC434477 252.5 PPM CARBON MONOXIDE/NITROGEN
D887660 9.91 PPM NITROGEN DIOXIDE/AIR
EBO113037 250,3 PPM NITRIC OXIDE/NITROGEN
EBO13OO55 4.81 PPM NITROGEN DIOXIDE/NITROGEN
0.3o/o
2.0o/o
0.8%
2.0%
The SRM, PRM or RGM noted above is only in reference to the GMIS used in the assay and not part of the analysis.
!nstrumenUMake/Model
ANALYTICAL EQUIPMENT
Analytical Principle Last Multipoint Calibration
Nicolet iS50 AUP2010228 CO MCO
Nicolet iS50 AUP2010228 NO MNO
Nicolet iS50 AUP2010228 NO2 impurity
FTIR
FTIR
FTIR NO2 impurity
Mat 02,2022
Mat 09,2022
Mar 10,2022
Airua$.
an Air Llquida cornp|ny
Aiqgas Specialty Gases
Airgas USA LLC
525 North Industrial loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
153402707756-1
146.0 CF
201s PS|G
660
Apr 10,2023
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 20i2)" document EpA
600/R-1 2/531 , using the assay procedures listed. Analytical Methodology does not require correc,tion for analytical interference. This iylinder has a total analyticat
uncertainty as stated below with a confidence level ol 95o/o. There are no significant impurities which afiect the use of this calibration mixture. All concentrations ;re on a
mole/mole basis unless otheMise noted. The results relate only to the items tested. The report shall nol be reproduced except in full without approval of the laboratory. Do
Sionature on fila
Approved for Release
GP043AS-036878-RT-1579
Page 1 of 1
Page 286 of 290
CERTIFICATE OF AIVALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
E02A|99E15W0021
cc502363
124 -fooele (SAP) - UT
872023
NO2,BALA
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Aor 10. 2026
Not use This bolow 100 psiq, i.e. 0.7
Component Requested
Concentration
ANALYTICAL RESULTS
Actual Protocol Total RelativeConcentration Method Uncertainty
Assay
Dates
NITROGEN DIOXIDE 50.00 PPM 48.42PPM G1 +l-2.0o/o N|STTraceable O4tO3t2O23,O4t1Ot2O23
AIR Balance
CALIBRATION STAI\IDARDSType Lot lD Cylinder No Concentration Uncertainty Expiration Date
GMIS 12397 CC511358 59.32 ppM NTTROGEN D|OX|DE/N|TROGEN 1.40/0 Dec 17,2024
ANALYTICAL EQIIIPMENT
Analytical Principle Last Multipoint CalibrationI nstrumenUlllake/Model
Apr 06, 2023MKS FT|R NO2 018143349 FTIR
Triad Data Available Upon Request
Appendix C.5
Accreditation Informatio n I Certifications
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SIAE Americon Associofio n f or Loborotorv Accreditotion
Accredited Air Emission Testing Body
A2LA hos occrediled
MONTROSE AIR QUALITY SERVICES
ln recogniiion of the successful completion of the joint A2LA ond Stock Testing Accrediiotion Council (STAC)
evoluotion process, this loboroiory is occredited to perform testing ociiviiies in complionce with
ASTM D7036:2004 - Stondord Proctice for Competence of Air Emission Testing Bodies.
Vice President, Accreditolion Services
For the Accreditotion Council
Ceriificote Number 3925.01
Volid to Februory 28,2026
This otcred,itation progrann is not includ,ed, under the A2LA ILAC Mutuat Recognition Arrangement.
GP043AS-035878-RT- 1579 Page 288 of 290
PresenteQ this2Tm doy of Februory 2024.
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Page 289 of 290
CERTIFICATE OF COMPLETION
Craig Kormylo
This document certifies that this individual has passed a comprehensive examination and is now a
Qualified lndividual (Ql) as defined in Section 8.3 of ASTM D7036-04 for the following method(s):
Source Evaluation Society Group 1: EPA Manual Gas Volume and Flow Measurements and lsokinetic
P a ft icul ate S a m pli ng M ethod s
Gertificate N u m ber: 043-2020-3
-*rdt--lz DATE oF ISSUE: 12131120
Tate Strickler, VP - Quality Systems
DATE OFEXPIRATION: 12130125
M$gNTm[q
GP043AS-036878-RT-1579
CERTIFICATE OF COMPLETION
Craig Kormylo
This document certifies that this individual has passed a comprehensive examination and is now a
Qualified lndividual (Ql) as defined in Section 8.3 of ASTM D7036-04 for the fotlowing method(s):
Source Evaluation Society Group 5: Paft TS CEMS RATA Testing
Certifi cate Number: 043-2020-4
-*./t--cz DATE OF ISSUE: 12130120
Tate Strickler, VP - Quality Systems
DATE OFEXPIRATION: 12129125
M$PNTMIT
GP043AS-036878-RT-1579 Page 290 of 290
DIVISION OF AIR OUALITY
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name PacifiCorp Huntington
Company Contact:Richard Neilson
Contact Phone No.435-687-4334
Stack Designation:Unit No. 1
Test & Review Dates
Test Date:4/10/2024
Review Date: 8/5/2024
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.1200 0.2600 0.3400 0.088 0.236 0.075
lbs./hr. 595.0 1290.0 1686.0 351.37 943.510 304.873
ppm
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
323.28 570.013 0.9970 1.782 0.838 23.61 -4.4 23.286471
Contractor Information
Contact:Andrew Bruning
Contracting Company: Montrose Air Quality Services
Address: 990 W 43rd Avenue, Denver, CO 80211
Phone No.: 303-810-2168
Project No.:
1800

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
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
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Company PacifiCorp Huntington
Point Source Unit No. 1
Test Date 4/10/24
Start
Time
End
Time Run
CO
lb/hr
CO
lb/MMBtu
CO2
%
CO
PPM
NOx
lb/hr
NOx
lb/MMBtu
NOx
PPM
SO2
lb/hr
SO2
lb/MMBtu
SO2
PPM
Unit Load
MW
Heat Input
MMBtu/hr
Flow
SCFH
14:46 15:07 1 303 0.074 10.6 60.3 1150.5 0.243 116.5 405 0.085 30.3 487 4746.4 80610845
15:38 15:59 2 301.6 0.064 10.5 51.1 1136 0.24 117.4 328 0.069 24.4 489 4736.3 81118340
16:14 16:35 3 277 0.058 10.5 46.7 1127.6 0.237 115.8 343.8 0.072 25.4 490 4760.5 81683197
16:50 17:11 4 556.3 0.117 10.7 96.4 1041.5 0.219 109 395.6 0.083 29.8 491 4746.5 80033996
17:25 17:46 5 1080.1 0.227 10.9 188.4 1046.5 0.22 111.1 420.3 0.068 32.1 491 4757.1 78868069
17:58 18:19 6 620.1 0.131 10.7 108.3 1023.4 0.218 108.9 439.9 0.094 33.7 486 4694.3 78671765
18:33 18:54 7 45.5 0.01 10 7.8 1155.7 0.259 121 395.9 0.069 29.5 462 4466.2 80012019
13:09 13:30 8 35.8 0.008 10.1 6.2 1122.5 0.253 118.1 422.2 0.092 31.1 461 4444.4 79582258
19:44 20:05 9 45.5 0.04 10.1 7.9 1130.6 0.254 119.3 434.2 0.096 33 461 4450.4 79350715
10
11
12
13
14
15
16
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.12 595.00
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/10/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/10/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 14:46 15:07 Y 30.2 30.3 -0.09 Y 0.0868 0.085 0.002 361.69 405 1 14:46 15:07 Y 10.4 10.6 -0.19
2 15:38 15:59 Y 24.7 24.4 0.29 Y 0.0709 0.069 0.002 293.83 328 2 15:38 15:59 Y 10.4 10.5 -0.09
3 16:14 16:35 Y 24.9 25.4 -0.52 Y 0.0722 0.072 0.000 297.44 343.8 3 16:14 16:35 Y 10.3 10.5 -0.19
4 16:50 17:11 Y 29.8 29.8 0.01 Y 0.0856 0.083 0.003 351.28 395.6 4 16:50 17:11 Y 10.4 10.7 -0.29
5 17:25 17:46 Y 32.1 32.1 0.02 Y 0.0900 0.088 0.002 362.38 420.3 5 17:25 17:46 Y 10.7 10.9 -0.23
6 17:58 18:19 Y 34.3 33.7 0.64 Y 0.0981 0.094 0.004 387.06 439.9 6 17:58 18:19 Y 10.5 10.7 -0.23
7 18:33 18:54 Y 30.0 29.5 0.48 Y 0.0913 0.089 0.002 349.65 395.9 7 18:33 18:54 Y 9.8 10 -0.18
8 13:09 13:30 Y 31.8 31.1 0.72 Y 0.0970 0.092 0.005 371.83 422.2 8 13:09 13:30 Y 9.8 10.1 -0.28
9 19:44 20:05 Y 33.4 33 0.40 Y 0.1018 0.098 0.004 387.14 434.2 9 19:44 20:05 Y 9.8 10.1 -0.28
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 30.1 29.92 0.22 0.088 0.086 0.003 Average = 10.230 10.450 0.217
Sd Standard Deviation = 0.40 Sd Standard Deviation = 0.002 Sd Standard Deviation = Sd Standard Deviation = 0.06
Confidence Coefficient = 0.31 Confidence Coefficient = 0.001 Confidence Coefficient = Confidence Coefficient = 0.049
RA - Relative Accuracy =1.70%RA 4.50%RA RA - Relative Accuracy =2.60%
n = 9 9 0 n = 9 or RA of 1%0.22%
t0.975 = 2.306 2.306 t0.975 = 2.306
E.L. Relative Accuracy = 73%
a For steam generators;b Average of three samples;9
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
13.2 Relative accuracy Performance Specification. The RA of the CEMSS must be not greater than 20 percent when RM is used in the denominator of Eq. 2-6
(average emissions during test are greater than 50 percent of the emission standard)or 10 percent when the applicable emission standard is used in the
denominator of Eq. 2-6 (average emissions during test are less than 50 percent of the emission standard).
Up dated January 17, 2006
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
13.2 CEMS Relative Accuracy Perfromance Specification.
The RA of the CEMS must be no grater than 20 percent of the mean value of the reference method (RM) data. 1 percent O2 or CO2.
The results are also acceptable if the absolute value of the difference between the mean RM value and the mean CEMS value is less than or equal to 1.0 percent O2 (or CO2).
Up dated September 14, 2016
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
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Anarad AR-30C 4924
4926Anarad AR-50C
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PassedPassedPassed
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 1
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.26 1290.00
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/10/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 9/30/2014 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 14:46 15:07 Y 115.2 119.5 -4.3 Y 0.238 0.243 -0.005 991.47 1150.5 1 14:46 15:07 7.5
2 15:38 15:59 Y 114.3 117.4 -3.1 Y 0.236 0.24 -0.004 977.39 1136 2 15:38 15:59 7.5
3 16:14 16:35 Y 112.9 115.8 -2.9 Y 0.235 0.237 -0.002 969.93 1127.6 3 16:14 16:35 7.5
4 16:50 17:11 Y 106.9 109 -2.1 Y 0.221 0.219 0.002 905.66 1041.5 4 16:50 17:11 7.5
5 17:25 17:46 Y 107.5 111.1 -3.6 Y 0.217 0.22 -0.003 871.92 1046.5 5 17:25 17:46 7.5
6 17:58 18:19 Y 106.0 108.9 -2.9 Y 0.218 0.218 0.000 858.90 1023.4 6 17:58 18:19 7.5
7 18:33 18:54 Y 117.6 121 -3.4 Y 0.258 0.259 -0.001 985.72 1155.7 7 18:33 18:54 7.5
8 13:09 13:30 Y 114.8 118.1 -3.3 Y 0.251 0.253 -0.002 964.06 1122.5 8 13:09 13:30 7.5
9 19:44 20:05 Y 116.0 119.3 -3.3 Y 0.254 0.254 0.000 966.54 1130.6 9 19:44 20:05 7.5
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 112.4 115.6 3.213 0.24 0.238 0.002 Average =
Sd Standard Deviation = 0.60 Sd Standard Deviation = 0.002 Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = 0.458 Confidence Coefficient = 0.002 Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy =3.30%Relative Accuracy =1.70%Relative Accuracy = RA - Relative Accuracy =
n = 9 9 0 n = 0 or RA of 1%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 =
E.L. Relative Accuracy = EMRA 91% EMRA
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
4. Performance and Equipment Specifications
4.3 Relative accuracy. The RA of the CEMSS shall be no grater than 20 percent of the mean value of the RM test data in terms of the
units of the emission standard or 10 percent of the applicable standard, whichever is greater
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
For SO2 emission standards below 0.20 lbs./MMBtu use 20 Percent of the emission standard;
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
12. Calculate the arithmetic difference between the RM and the CEMSS output for each run. The average of the nine (of more) data sets constitute the RA.
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 1 percent O2 or CO2.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
4925Anarad AR-880
Anarad AR-23 4927
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PassedPassed
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 1
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.340 1686.00
Date CO Dry CO Dry CO
4/10/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 14:46 15:07 Y 62.86 60.3 -2.56 Y 0.079 0.074 -0.005 329.27 303
2 15:38 15:59 Y 52.15 51.1 -1.05 Y 0.066 0.064 -0.002 271.54 301.6
3 16:14 16:35 Y 43.37 46.7 3.33 Y 0.055 0.058 0.003 226.80 277
4 16:50 17:11 Y 67.93 96.4 28.47 Y 0.085 0.117 0.032 350.25 556.3
5 17:25 17:46 Y 191.60 188.4 -3.20 Y 0.235 0.227 -0.008 945.84 1080.1
6 17:58 18:19 Y 109.18 108.3 -0.88 Y 0.136 0.131 -0.005 538.44 620.1
7 18:33 18:54 Y 4.12 7.8 3.68 Y 0.005 0.01 0.005 21.05 45.5
8 13:09 13:30 Y 5.29 6.2 0.91 Y 0.007 0.008 0.001 27.04 35.8
9 19:44 20:05 Y 6.63 7.9 1.27 Y 0.009 0.04 0.031 33.63 45.5
10
11
12
13
14
15
16
Average = 60.35 63.68 3.33 0.075 0.081 0.006
Sd Standard Deviation = 9.72 0.015
Confidence Coefficient = 7.475 0.012
RA - Relative Accuracy =17.90%
n = 9 9 0
t0.975 = 2.306 2.306
E.L. Relative Accuracy = 22% 5.16%
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
7330258.58
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Passed Passed
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Thermo Scientific 48i
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:0.12 595.00
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/10/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/10/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 14:46 15:07 Y 30.2 30.3 -0.09 0.0868 0.085 361.69 1 14:46 15:07 Y 10.4 10.6 -0.19
2 15:38 15:59 Y 24.7 24.4 0.29 0.0709 0.069 293.83 2 15:38 15:59 Y 10.4 10.5 -0.09
3 16:14 16:35 Y 24.9 25.4 -0.52 0.0722 0.072 297.44 3 16:14 16:35 Y 10.3 10.5 -0.19
4 16:50 17:11 Y 29.8 29.8 0.01 0.0856 0.083 351.28 4 16:50 17:11 Y 10.4 10.7 -0.29
5 17:25 17:46 Y 32.1 32.1 0.02 0.0900 0.068 362.38 5 17:25 17:46 Y 10.7 10.9 -0.23
6 17:58 18:19 Y 34.3 33.7 0.64 0.0981 0.094 387.06 6 17:58 18:19 Y 10.5 10.7 -0.23
7 18:33 18:54 Y 30.0 29.5 0.48 0.0913 0.069 349.65 7 18:33 18:54 Y 9.8 10 -0.18
8 13:09 13:30 Y 31.8 31.1 0.72 0.0970 0.092 371.83 8 13:09 13:30 Y 9.8 10.1 -0.28
9 19:44 20:05 Y 33.4 33 0.40 0.1018 0.096 387.14 9 19:44 20:05 Y 9.8 10.1 -0.28
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 30.1 29.92 0.210 Average = 10.239 10.456 0.22
Sd Standard Deviation =0.40 Sd Standard Deviation =0.06
Confidence Coefficient =1.19 Confidence Coefficient =0.050
RA - Relative Accuracy =5.00%RA - Relative Accuracy =2.61%
n =9 n =0 n =0 n =9 or RA of 1%0.22%
t0.975 =2.306 t0.975 =t0.975 =t0.975 =2.306
BAF =Use BAF 1.0066
a For steam generators;b Average of three samples;Alterative RA
c Make sure that RM and M data are on a consistent basis either wet or dry.
RATA Semiannual Test Annual
SO2 RA < 10% RA < 7.5% OR < 12ppm
Pass 1.4 ppm
CO2 - The relative accuracy for CO2 monitors shall not exceed 10 percent. See Alternative Below
Pt. 75, App. A 3.3.3 The relative accuracy for CO2 monitors shall not exceed 10 percent. Alternative - If the mean difference of the CO2
monitor measurements and the corresponding reference method measurement, calculated using Equation A7
Up dated September 25, 2017
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which ever is greater.
Up dated January 17, 2006
Anarad AR-30C 4924
Anarad AR-50C 4926
Passed
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Passed
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 1
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:0.26 1290.00
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/10/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/10/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 14:46 15:07 115.2 116.5 Y 0.238 0.243 -0.00511 991.47 1 14:46 15:07 7.5
2 15:38 15:59 114.3 117.4 Y 0.236 0.24 -0.00406 977.39 2 15:38 15:59 7.5
3 16:14 16:35 112.9 115.8 Y 0.235 0.237 -0.00166 969.93 3 16:14 16:35 7.5
4 16:50 17:11 106.9 109 Y 0.221 0.219 0.00176 905.66 4 16:50 17:11 7.5
5 17:25 17:46 107.5 111.1 Y 0.217 0.22 -0.00335 871.92 5 17:25 17:46 7.5
6 17:58 18:19 106.0 108.9 Y 0.218 0.218 -0.00032 858.90 6 17:58 18:19 7.5
7 18:33 18:54 117.6 121 Y 0.258 0.259 -0.00150 985.72 7 18:33 18:54 7.5
8 13:09 13:30 114.8 118.1 Y 0.251 0.253 -0.00161 964.06 8 13:09 13:30 7.5
9 19:44 20:05 116.0 119.3 Y 0.254 0.254 0.00006 966.54 9 19:44 20:05 7.5
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 0.236 0.238 0.00175 Average =
Sd Standard Deviation =Sd Standard Deviation =0.002 Sd Standard Deviation =Sd Standard Deviation =
Confidence Coefficient =Confidence Coefficient =0.002 Confidence Coefficient =Confidence Coefficient =
RA - Relative Accuracy =RA =1.60%RA =RA - Relative Accuracy =
n =0 n =9 n =0 n =0 or RA of 1%
t0.975 =t0.975 =2.306 t0.975 =t0.975 =
No Bias
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
RATA Semiannually Annual NOx Multipliers
NOX RA < 10% RA < 7.5% Old Multiplier New Multiplier
Alternative RA
For units where the average of the monitoring system measurements of NOX emission rate during the RATA
is less than or equal to 0.20 lb./MMBtu, the mean value of the NOX continuous emission monitoring system
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
specification of 10.0 percent is not achieved.
di (Rmi - CEMSi)-0.002
Alterative RA Passed
Anarad AR-880 4925
Anarad AR-23 4927
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Dry Volumetric Flow
dscfh
Run Date Start Time End Time RM CEM Diff
1 4/10/24 14:46 15:07 72,043,178.93
2 4/10/24 15:38 15:59 71,608,920.79
3 4/10/24 16:14 16:35 71,932,564.50
4 4/10/24 16:50 17:11 70,914,215.85
5 4/10/24 17:25 17:46 67,893,828.01
6 4/10/24 17:58 18:19 67,826,940.71
7 4/10/24 18:33 18:54 70,181,085.30
8 4/10/24 13:09 13:30 70,309,511.98
9 4/10/24 19:44 20:05 69,747,801.63
10 4/10/24
11 4/10/24
12 4/10/24
13 4/10/24
14 4/10/24
15 4/10/24
16 4/10/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Dry Volumetric Flow
dscfm
Run Date Start Time End Time RM CEM Diff
1 4/10/24 14:46 15:07 1,200,719.65
2 4/10/24 15:38 15:59 1,193,482.01
3 4/10/24 16:14 16:35 1,198,876.07
4 4/10/24 16:50 17:11 1,181,903.60
5 4/10/24 17:25 17:46 1,131,563.80
6 4/10/24 17:58 18:19 1,130,449.01
7 4/10/24 18:33 18:54 1,169,684.75
8 4/10/24 13:09 13:30 1,171,825.20
9 4/10/24 19:44 20:05 1,162,463.36
10 4/10/24
11 4/10/24
12 4/10/24
13 4/10/24
14 4/10/24
15 4/10/24
16 4/10/24
Average =
Standard Deviation
PacifiCorp Huntington
Unit No. 1
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Actual Volumetric Flow
acfm
Run Date Start Time End Time RM CEM Diff
1 4/10/24 14:46 15:07 1,895,407.23
2 4/10/24 15:38 15:59 1,877,862.23
3 4/10/24 16:14 16:35 1,887,643.65
4 4/10/24 16:50 17:11 1,859,325.40
5 4/10/24 17:25 17:46 1,878,580.44
6 4/10/24 17:58 18:19 1,874,476.35
7 4/10/24 18:33 18:54 1,880,119.48
8 4/10/24 13:09 13:30 1,884,531.38
9 4/10/24 19:44 20:05 1,868,833.22
10 4/10/24
11 4/10/24
12 4/10/24
13 4/10/24
14 4/10/24
15 4/10/24
16 4/10/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
WET VOLUMETRIC FLOW
wscfh
Run Date Start Time End Time RM CEM Diff
1 4/10/24 14:46 15:07 Y 79,898,640.15 80610844.5 (712,204.35)
2 4/10/24 15:38 15:59 Y 79,417,031.27 81118340.3 (1,701,309.03)
3 4/10/24 16:14 16:35 Y 79,775,964.51 81683196.7 (1,907,232.19)
4 4/10/24 16:50 17:11 Y 78,646,576.93 80033995.7 (1,387,418.77)
5 4/10/24 17:25 17:46 Y 79,447,405.50 78868068.9 579,336.60
6 4/10/24 17:58 18:19 Y 79,369,135.91 78671764.6 697,371.31
7 4/10/24 18:33 18:54 Y 79,690,189.95 80012018.8 (321,828.85)
8 4/10/24 13:09 13:30 Y 79,836,017.66 79582258.4 253,759.26
9 4/10/24 19:44 20:05 Y 79,198,199.01 79350714.6 (152,515.59)
10 4/10/24
11 4/10/24
12 4/10/24
13 4/10/24
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
14 4/10/24
15 4/10/24
16 4/10/24
Average = 79,475,462.32 79,992,355.83 516,893.51
Standard Deviation 972,929
Confidence Coefficient = 747858
RA - Relative Accuracy =1 1.6%
n = 9
t0.975 =2.306
Wet Volumetric Flow
wscfm
Run Date Start Time End Time RM CEM Diff
1 4/10/24 14:46 15:07 1,331,644.00
2 4/10/24 15:38 15:59 1,323,617.19
3 4/10/24 16:14 16:35 1,329,599.41
4 4/10/24 16:50 17:11 1,310,776.28
5 4/10/24 17:25 17:46 1,324,123.42
6 4/10/24 17:58 18:19 1,322,818.93
7 4/10/24 18:33 18:54 1,328,169.83
8 4/10/24 13:09 13:30 1,330,600.29
9 4/10/24 19:44 20:05 1,319,969.98
10 4/10/24
11 4/10/24
12 4/10/24
13 4/10/24
14 4/10/24
15 4/10/24
16 4/10/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
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Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 1
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024
Start Time 14:46 15:38 16:14 16:50 17:25 17:58 18:33 13:09 19:44
Stop Time 15:07 15:59 16:35 17:11 17:46 18:19 18:54 13:30 20:05
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28
As ft^2 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01
Cp (Pitot Tube Coefficient)0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84
Yd Meter Y Factor (unit less)0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970
Pbar Barometric Pressure ("Hg)23.61 23.61 23.61 23.61 23.61 23.61 23.61 23.61 23.61 23.61 23.61 23.61
Pq (Static Pressure)-4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40 -4.40
Ps (Pressure of the Stack)23.29 23.29 23.29 23.29 23.29 23.29 23.29 23.29 23.29 23.29 23.29 23.29
Ts Stack Temp Avg. oF 124.90 123.00 123.40 122.90 123.00 122.30 121.70 122.00 121.80
Tm Meter Temperature oF 78.00 78.00 84.00 84.00 86.00 86.00 87.00 87.00 87.00
CO2 (carbon dioxide)10.41 10.41 10.31 10.41 10.67 10.47 9.82 9.82 9.82
O2 (oxygen)7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Md Molecular Weight Dry 29.97 29.97 29.95 29.97 30.01 29.98 29.87 29.87 29.87 #VALUE!#VALUE!
Ms Molecular Weight Wet 28.79 28.79 28.78 28.79 28.26 28.24 28.45 28.45 28.45 #VALUE!#VALUE!
N2 (nitrogen)82.09 82.09 82.19 82.09 81.83 82.03 82.68 82.68 82.68 #VALUE!#VALUE!
Vm Sample Volume (cf)49.47 49.47 49.58 49.58 48.83 48.83 77.29 77.29 77.29 0.00 0.00 0.00
Vm std Standard Volume (dscf)38.18 38.18 37.84 37.84 37.14 37.14 58.67 58.67 58.67
Vlc Moisture (g)87.50 87.50 87.50 87.50 134.50 134.50 169.50 169.50 169.50
Vwstd Moisture Volume (scf)4.12 4.12 4.12 4.12 6.33 6.33 7.98 7.98 7.98
Bws Moisture Content (%100)9.83%9.83%9.83%9.83%14.54%14.54%11.93%11.93%11.93%
S Bws (saturation moisture)16.97%16.12%16.29%16.07%16.12%15.81%15.55%15.68%15.59%
AvgSqrtDlp √∆P 0.839 0.832 0.837 0.824 0.824 0.822 0.829 0.830 0.825
Vs. Gas Velocity (ft./sec)55.42 55.42 55.42 55.42 55.42 55.42 55.42 55.42 55.42 55.42 55.42 55.42
Qa (stack actual flow rate) acfm 1,895,407 1,877,862 1,887,644 1,859,325 1,878,580 1,874,476 1,880,119 1,884,531 1,868,833
Qs (stack std. flow rate) dscfm 1,200,720 1,193,482 1,198,876 1,181,904 1,131,564 1,130,449 1,169,685 1,171,825 1,162,463 #VALUE!#VALUE!#VALUE!
Qsd (stack std. flow rate) dscfh 72,043,179 71,608,921 71,932,564 70,914,216 67,893,828 67,826,941 70,181,085 70,309,512 69,747,802
Qw (stack flow rate) wscfm 79,898,640 79,417,031 79,775,965 78,646,577 79,447,405 79,369,136 79,690,190 79,836,018 79,198,199
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 1
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024 4/10/2024
Heat Input - BTU/hr.
F factor - scf/MMBtu 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0
Fuel Analysis - ft3/min 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0
Fuel Flow - ft3/min 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
Heat Input - BTU/hr.0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
SO2 Concentrations
Uncorrected 30.20 24.70 24.80 29.74 32.00 34.10 29.80 31.40 33.20
Dry Corrected 30.21 24.69 24.88 29.81 32.12 34.34 29.98 31.82 33.40
Wet Corrected
NOx Concentrations
Uncorrected 115.30 114.30 112.90 106.90 107.20 105.50 117.10 114.40 115.80
Dry Corrected 115.21 114.27 112.88 106.92 107.51 106.01 117.58 114.79 116.01
Wet Corrected
CO Concentrations
Uncorrected 62.90 51.50 42.60 66.80 188.00 106.00 0.20 1.40 3.20
Dry Corrected 62.86 52.15 43.36 67.93 191.60 109.18 4.12 5.29 6.63
Wet Corrected
CO2 Concentrations
Uncorrected 10.60 10.60 10.50 10.60 10.80 10.60 10.00 10.00 10.00
Dry Corrected 10.41 10.41 10.31 10.41 10.67 10.47 9.82 9.82 9.82
Wet Corrected
O2 Concentrations
Uncorrected 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Dry Corrected 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Wet Corrected
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.088 0.236 0.075 Average % concentration
lbs./hr.351.37 943.51 304.87 CO2 O2
ppm or % 30.14 112.35 60.35 10.24 7.50
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)8.68E-02 2.38E-01 7.90E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.020E-06 1.376E-05 4.571E-06
lbs./hr.361.69 991.47 329.27 10.41 7.50
ppm or %30.21 115.21 62.86 10.60 7.50
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)7.09E-02 2.36E-01 6.55E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.103E-06 1.365E-05 3.792E-06
lbs./hr.293.83 977.39 271.54 10.41 7.50
ppm or %24.69 114.27 52.15 10.60 7.50 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)7.22E-02 2.35E-01 5.50E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.135E-06 1.348E-05 3.153E-06
lbs./hr.297.44 969.93 226.80 10.31 7.50
ppm or %24.88 112.88 43.37 10.50 7.50 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)8.56E-02 2.21E-01 8.54E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.954E-06 1.277E-05 4.939E-06
lbs./hr.351.28 905.66 350.25 10.41 7.50
ppm or %29.81 106.92 67.93 10.60 7.50 Raw Value
Run 5
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)9.00E-02 2.17E-01 2.35E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.337E-06 1.284E-05 1.393E-05
lbs./hr.362.37 871.9179 945.84 10.67 7.50
ppm or %32.12 107.51 191.60 10.80 7.50 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
O2
CO2
Clear
lbs./MMBTU
Run 6
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)9.81E-02 2.18E-01 1.36E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.707E-06 1.266E-05 7.938E-06
lbs./hr.387.06 858.8980 538.44 10.47 7.50
ppm or %34.34 106.01 109.18 10.60 7.50 Raw Value
Run 7
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)9.13E-02 2.58E-01 5.50E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.982E-06 1.405E-05 2.999E-07
lbs./hr.349.65 985.72 21.05 9.82 7.50
ppm or %29.98 117.58 4.12 10.00 7.50 Raw Value
Run 8
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)9.70E-02 2.51E-01 7.05E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.289E-06 1.371E-05 3.846E-07
lbs./hr.371.83 964.06 27.04 9.82 7.50
ppm or %31.82 114.79 5.29 10.00 7.50 Raw Value
Run 9
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)1.02E-01 2.54E-01 8.84E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.551E-06 1.386E-05 4.822E-07
lbs./hr.387.14 966.54 33.63 9.82 7.50
ppm or %33.40 116.01 6.63 10.00 7.50 Raw Value
Run 10
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
Run 11
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
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Huntington Unit 1 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-10-2024)-2G
Calibration Error Test
Test Date April 10, 2024 O2
CS - Cal. Span 20.00
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 10.00 10.00 0.00 0.00% Passed Cal.
High-level 20.00 20.00 0.00 0.00% 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 50.00%
100% of Cal. Span High-level 100.00%
Test Date April 10, 2024 CO2
CS - Cal. Span 17.82
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 0.10 0.10 0.561% Passed Cal.
Mid-level 8.93 9.10 0.17 0.982% Passed Cal.
High-level 17.82 17.60 0.22 1.235% 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 50.08%
100% of Cal. Span High-level 100.00%
Test Date April 10, 2024 SO2
CS - Cal. Span 49.90
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 0.401% Passed Cal.
Mid-level 26.88 26.80 0.08 0.160% Passed Cal.
High-level 49.90 50.80 0.90 1.804% 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 53.87%
100% of Cal. Span High-level 100.00%
Test Date April 10, 2024 NOx
CS - Cal. Span 331.40
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 -0.30 0.30 0.091% Passed Cal.
Mid-level 170.00 170.30 0.30 0.091% Passed Cal.
High-level 331.40 334.30 2.90 0.875% 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 51.30%
100% of Cal. Span High-level 100.00%
Test Date April 10, 2024 CO
1686 CS - Cal. Span 328.30
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 0.70 0.70 0.213% Passed Cal.
Mid-level 144.50 145.10 0.60 0.183% Passed Cal.
High-level 328.30 328.00 0.30 0.091% 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 44.01%
100% of Cal. Span High-level 100.00%
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name PacifiCorp Huntington
Company Contact:Richard Neilson
Contact Phone No.435-687-4334
Stack Designation:Unit No. 2
Test & Review Dates
Test Date:4/11/2024
Review Date: 9/23/2024
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.1200 0.2600 0.043 0.195
lbs./hr.
ppm
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
322.68 567.899 0.9970 1.782 0.838 23.87 -5.3 23.480294
Contractor Information
Contact:Andrew Bruning
Contracting Company: Montrose Air Quality Services
Address: 990 W 43rd Avenue, Denver, CO 80211
Phone No.: 303-810-2168
Project No.:
1800

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
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
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Company PacifiCorp Huntington
Point Source Unit No. 2
Test Date 4/11/24
Start
Time
End
Time Run
CO
lb/hr
CO
lb/MMBtu
CO2
%
CO
PPM
NOx
lb/hr
NOx
lb/MMBtu
NOx
PPM
SO2
lb/hr
SO2
lb/MMBtu
SO2
PPM
Unit Load
MW
Heat Input
MMBtu/hr
Flow
SCFH
14:42 15:03 1 244.6 0.057 11.2 49.3 773.9 0.172 93 139.1 0.031 11.9 429 4279.1 69490670.9
15:32 15:53 2 311.7 0.072 11.3 62.4 816.1 0.189 99.5 177.3 0.041 15.6 436 4327.6 68676632.3
16:05 16:26 3 451.4 0.104 11.4 90.1 827.3 0.19 100.6 190.4 0.044 16.7 438 4345.4 68842429.1
16:37 16:58 4 398.7 0.092 11.4 79.6 830 0.191 100.6 179.5 0.041 15.7 435 4363.1 68934429.1
17:10 17:31 5 345.9 0.08 11.4 69.3 82.3 0.19 100.3 177.6 0.041 15.6 436 4333.7 68627496.9
17:44 18:05 6 440.9 0.101 11.3 87.6 824 0.19 99.9 189.5 0.044 16.5 436 4259.4 69080907.4
18:17 18:38 7 620.7 0.144 11.4 124.9 820.4 0.189 100.2 186.5 0.043 16.4 434 4334.9 68589998.3
19:01 19:22 8 1137.7 0.262 11 221.3 846.9 0.195 100.5 199.9 0.049 17.1 434 4336.1 70583163.1
19:33 19:54 9 1390.9 0.322 10.9 257.3 846.5 0.196 99.3 204.1 0.047 17.2 435 4323.4 71615374.5
10
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12
13
14
15
16
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.12
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/11/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/11/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 14:42 15:03 Y 17.4 16.7 0.67 Y 0.0464 0.044 0.002 174.74 139.1 1 14:42 15:03 Y 11.2 11.2 0.01
2 15:32 15:53 Y 14.9 15.6 -0.69 Y 0.0398 0.041 -0.001 147.19 177.3 2 15:32 15:53 Y 11.2 11.3 -0.09
3 16:05 16:26 Y 16.1 16.7 -0.64 Y 0.0429 0.044 -0.001 159.36 190.4 3 16:05 16:26 Y 11.2 11.4 -0.19
4 16:37 16:58 Y 15.1 15.7 -0.57 Y 0.0406 0.041 0.000 151.49 179.5 4 16:37 16:58 Y 11.1 11.4 -0.26
5 17:10 17:31 Y 14.8 15.6 -0.82 Y 0.0397 0.041 -0.001 147.72 177.6 5 17:10 17:31 Y 11.1 11.4 -0.26
6 17:44 18:05 Y 15.9 16.5 -0.65 Y 0.0423 0.044 -0.002 159.36 189.5 6 17:44 18:05 Y 11.2 11.3 -0.09
7 18:17 18:38 Y 15.9 16.4 -0.55 Y 0.0422 0.043 -0.001 159.25 186.5 7 18:17 18:38 Y 11.2 11.4 -0.16
8 19:01 19:22 Y 16.4 17.1 -0.75 Y 0.0451 0.049 -0.004 162.46 199.9 8 19:01 19:22 Y 10.8 11 -0.15
9 19:33 19:54 Y 16.3 17.2 -0.89 Y 0.0454 0.047 -0.002 164.14 204.1 9 19:33 19:54 Y 10.7 10.9 -0.15
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 15.8 16.39 0.54 0.043 0.044 0.001 Average = 11.100 11.250 0.149
Sd Standard Deviation = 0.47 Sd Standard Deviation = 0.002 Sd Standard Deviation = Sd Standard Deviation = 0.08
Confidence Coefficient = 0.36 Confidence Coefficient = 0.001 Confidence Coefficient = Confidence Coefficient = 0.063
RA - Relative Accuracy =5.70%RA RA RA - Relative Accuracy =1.90%
n = 9 9 0 n = 9 or RA of 1%0.15%
t0.975 = 2.306 2.306 t0.975 = 2.306
E.L. Relative Accuracy = 36% 1.67%
a For steam generators;b Average of three samples;9
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
13.2 Relative accuracy Performance Specification. The RA of the CEMSS must be not greater than 20 percent when RM is used in the denominator of Eq. 2-6
(average emissions during test are greater than 50 percent of the emission standard)or 10 percent when the applicable emission standard is used in the
denominator of Eq. 2-6 (average emissions during test are less than 50 percent of the emission standard).
Up dated January 17, 2006
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
13.2 CEMS Relative Accuracy Perfromance Specification.
The RA of the CEMS must be no grater than 20 percent of the mean value of the reference method (RM) data. 1 percent O2 or CO2.
The results are also acceptable if the absolute value of the difference between the mean RM value and the mean CEMS value is less than or equal to 1.0 percent O2 (or CO2).
Up dated September 14, 2016
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
PassedPassedPassed
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Thermo Electron 43I-ANSCB "0600514680
7330258.83Thermo Scientific
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Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 2
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.26
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/11/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 9/30/2014 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 14:42 15:03 Y 96.7 97.4 -0.7 Y 0.186 0.184 0.002 699.37 773.9 1 14:42 15:03 6.0
2 15:32 15:53 Y 100.8 99.5 1.3 Y 0.193 0.189 0.004 715.53 816.1 2 15:32 15:53 6.0
3 16:05 16:26 Y 102.1 100.6 1.5 Y 0.196 0.19 0.006 728.22 827.3 3 16:05 16:26 6.0
4 16:37 16:58 Y 101.7 100.8 0.9 Y 0.196 0.191 0.005 732.11 830 4 16:37 16:58 6.0
5 17:10 17:31 Y 101.5 100.3 1.2 Y 0.196 0.19 0.006 729.31 822.3 5 17:10 17:31 6.0
6 17:44 18:05 Y 100.8 99.9 0.9 Y 0.193 0.19 0.003 728.29 824 6 17:44 18:05 6.0
7 18:17 18:38 Y 101.2 100.2 1.0 Y 0.193 0.189 0.004 730.41 820.4 7 18:17 18:38 6.0
8 19:01 19:22 Y 100.5 100.5 0.0 Y 0.199 0.195 0.004 717.66 846.9 8 19:01 19:22 6.0
9 19:33 19:54 Y 99.3 99.3 0.0 Y 0.199 0.196 0.003 718.59 846.5 9 19:33 19:54 6.0
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 100.5 99.8 0.684 0.20 0.190 0.004 Average =
Sd Standard Deviation = 0.73 Sd Standard Deviation = 0.001 Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = 0.561 Confidence Coefficient = 0.001 Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy =1.20%Relative Accuracy =2.60%Relative Accuracy = RA - Relative Accuracy =
n = 9 9 0 n = 0 or RA of 1%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 =
E.L. Relative Accuracy = EMRA 75% EMRA
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
4. Performance and Equipment Specifications
4.3 Relative accuracy. The RA of the CEMSS shall be no grater than 20 percent of the mean value of the RM test data in terms of the
units of the emission standard or 10 percent of the applicable standard, whichever is greater
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
For SO2 emission standards below 0.20 lbs./MMBtu use 20 Percent of the emission standard;
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
12. Calculate the arithmetic difference between the RM and the CEMSS output for each run. The average of the nine (of more) data sets constitute the RA.
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 1 percent O2 or CO2.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
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"0606115467Thermo Electron 42I-ANMSDCB
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 2
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Date CO Dry CO Dry CO
4/11/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 14:42 15:03 Y 101.86 111.9 10.04 Y 0.119 0.128 0.009 448.33 565.2
2 15:32 15:53 Y 61.28 62.4 1.12 Y 0.072 0.072 0.000 264.74 311.7
3 16:05 16:26 Y 88.11 90.1 1.99 Y 0.103 0.104 0.001 382.60 451.4
4 16:37 16:58 Y 77.07 79.6 2.53 Y 0.091 0.092 0.001 337.68 398.7
5 17:10 17:31 Y 65.97 69.3 3.33 Y 0.077 0.08 0.003 288.41 345.9
6 17:44 18:05 Y 83.79 87.6 3.81 Y 0.098 0.101 0.003 368.46 440.9
7 18:17 18:38 Y 130.17 124.9 -5.27 Y 0.152 0.144 -0.008 572.04 620.7
8 19:01 19:22 Y 212.15 221.3 9.15 Y 0.256 0.262 0.006 922.19 1137.7
9 19:33 19:54 Y 255.57 257.3 1.73 Y 0.311 0.322 0.011 1125.35 1390.9
10
11
12
13
14
15
16
Average = 119.55 122.71 3.16 0.142 0.145 0.003
Sd Standard Deviation = 4.51 0.006
Confidence Coefficient = 3.466 0.005
RA - Relative Accuracy =5.50% 5.40%
n = 9 9 0
t0.975 = 2.306 2.306
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Passed Passed
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Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:0.12
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/11/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/11/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 14:42 15:03 Y 17.4 11.9 5.47 0.0464 174.74 1 14:42 15:03 Y 11.2 11.2 0.01
2 15:32 15:53 Y 14.9 15.6 -0.69 0.0398 147.19 2 15:32 15:53 Y 11.2 11.3 -0.09
3 16:05 16:26 Y 16.1 16.7 -0.64 0.0429 159.36 3 16:05 16:26 Y 11.2 11.4 -0.19
4 16:37 16:58 Y 15.1 15.7 -0.57 0.0406 151.49 4 16:37 16:58 Y 11.1 11.4 -0.26
5 17:10 17:31 Y 14.8 15.6 -0.82 0.0397 147.72 5 17:10 17:31 Y 11.1 11.4 -0.26
6 17:44 18:05 Y 15.9 16.5 -0.65 0.0423 159.36 6 17:44 18:05 Y 11.2 11.3 -0.09
7 18:17 18:38 Y 15.9 16.4 -0.55 0.0422 159.25 7 18:17 18:38 Y 11.2 11.4 -0.16
8 19:01 19:22 Y 16.4 17.1 -0.75 0.0451 162.46 8 19:01 19:22 Y 10.8 11 -0.15
9 19:33 19:54 Y 16.3 17.2 -0.89 0.0454 164.14 9 19:33 19:54 Y 10.7 10.9 -0.15
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 15.8 15.86 0.010 Average = 11.106 11.256 0.15
Sd Standard Deviation =2.06 Sd Standard Deviation =0.08
Confidence Coefficient =6.17 Confidence Coefficient =0.064
RA - Relative Accuracy =39.00%RA - Relative Accuracy =1.92%
n =9 n =0 n =0 n =9 or RA of 1%0.15%
t0.975 =2.306 t0.975 =t0.975 =t0.975 =2.306
BAF =No Bias
a For steam generators;b Average of three samples;Alterative RA
c Make sure that RM and M data are on a consistent basis either wet or dry.
RATA Semiannual Test Annual
SO2 RA < 10% RA < 7.5% OR < 12ppm
6.2 ppm
CO2 - The relative accuracy for CO2 monitors shall not exceed 10 percent. See Alternative Below
Pt. 75, App. A 3.3.3 The relative accuracy for CO2 monitors shall not exceed 10 percent. Alternative - If the mean difference of the CO2
monitor measurements and the corresponding reference method measurement, calculated using Equation A7
Up dated September 25, 2017
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which ever is greater.
Up dated January 17, 2006
Passed
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Passed
Thermo Electron 43I-ANSCB "0600514680
Thermo Scientific 7330258.83
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 2
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:0.26
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/11/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/11/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 14:42 15:03 96.7 Y 0.186 0.184 0.00158 699.37 1 14:42 15:03 6.0
2 15:32 15:53 100.8 Y 0.193 0.189 0.00443 715.53 2 15:32 15:53 6.0
3 16:05 16:26 102.1 Y 0.196 0.19 0.00587 728.22 3 16:05 16:26 6.0
4 16:37 16:58 101.7 Y 0.196 0.191 0.00523 732.11 4 16:37 16:58 6.0
5 17:10 17:31 101.5 Y 0.196 0.19 0.00589 729.31 5 17:10 17:31 6.0
6 17:44 18:05 100.8 Y 0.193 0.19 0.00342 728.29 6 17:44 18:05 6.0
7 18:17 18:38 101.2 Y 0.193 0.189 0.00448 730.41 7 18:17 18:38 6.0
8 19:01 19:22 100.5 Y 0.199 0.195 0.00418 717.66 8 19:01 19:22 6.0
9 19:33 19:54 99.3 Y 0.199 0.196 0.00270 718.59 9 19:33 19:54 6.0
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 0.195 0.190 0.00420 Average =
Sd Standard Deviation =Sd Standard Deviation =0.001 Sd Standard Deviation =Sd Standard Deviation =
Confidence Coefficient =Confidence Coefficient =0.001 Confidence Coefficient =Confidence Coefficient =
RA - Relative Accuracy =RA =2.70%RA =RA - Relative Accuracy =
n =0 n =9 n =0 n =0 or RA of 1%
t0.975 =t0.975 =2.306 t0.975 =t0.975 =
Use BAF 1.02
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
RATA Semiannually Annual NOx Multipliers
NOX RA < 10% RA < 7.5% Old Multiplier New Multiplier
Alternative RA
For units where the average of the monitoring system measurements of NOX emission rate during the RATA
is less than or equal to 0.20 lb./MMBtu, the mean value of the NOX continuous emission monitoring system
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
specification of 10.0 percent is not achieved.
di (Rmi - CEMSi)0.004
Alterative RA Passed
Thermo Electron 42I-ANMSDCB "0606115467
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Dry Volumetric Flow
dscfh
Run Date Start Time End Time RM CEM Diff
1 4/11/24 14:42 15:03 60,534,428.90
2 4/11/24 15:32 15:53 59,419,542.47
3 4/11/24 16:05 16:26 59,720,398.68
4 4/11/24 16:37 16:58 60,263,202.06
5 4/11/24 17:10 17:31 60,133,700.28
6 4/11/24 17:44 18:05 60,481,203.14
7 4/11/24 18:17 18:38 60,440,349.30
8 4/11/24 19:01 19:22 59,785,309.38
9 4/11/24 19:33 19:54 60,560,071.53
10 4/11/24
11 4/11/24
12 4/11/24
13 4/11/24
14 4/11/24
15 4/11/24
16 4/11/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Dry Volumetric Flow
dscfm
Run Date Start Time End Time RM CEM Diff
1 4/11/24 14:42 15:03 1,008,907.15
2 4/11/24 15:32 15:53 990,325.71
3 4/11/24 16:05 16:26 995,339.98
4 4/11/24 16:37 16:58 1,004,386.70
5 4/11/24 17:10 17:31 1,002,228.34
6 4/11/24 17:44 18:05 1,008,020.05
7 4/11/24 18:17 18:38 1,007,339.16
8 4/11/24 19:01 19:22 996,421.82
9 4/11/24 19:33 19:54 1,009,334.53
10 4/11/24
11 4/11/24
12 4/11/24
13 4/11/24
14 4/11/24
15 4/11/24
16 4/11/24
Average =
Standard Deviation
En
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PacifiCorp Huntington
Unit No. 2
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Actual Volumetric Flow
acfm
Run Date Start Time End Time RM CEM Diff
1 4/11/24 14:42 15:03 1,608,289.97
2 4/11/24 15:32 15:53 1,582,427.85
3 4/11/24 16:05 16:26 1,592,343.36
4 4/11/24 16:37 16:58 1,587,130.05
5 4/11/24 17:10 17:31 1,596,057.42
6 4/11/24 17:44 18:05 1,607,233.68
7 4/11/24 18:17 18:38 1,601,066.29
8 4/11/24 19:01 19:22 1,595,989.28
9 4/11/24 19:33 19:54 1,602,361.10
10 4/11/24
11 4/11/24
12 4/11/24
13 4/11/24
14 4/11/24
15 4/11/24
16 4/11/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
WET VOLUMETRIC FLOW
wscfh
Run Date Start Time End Time RM CEM Diff
1 4/11/24 14:42 15:03 Y 69,501,096.32 69490670.9 10,425.42
2 4/11/24 15:32 15:53 Y 68,335,970.07 68676632.3 (340,662.23)
3 4/11/24 16:05 16:26 Y 68,740,283.69 68842429.1 (102,145.41)
4 4/11/24 16:37 16:58 Y 68,765,981.68 68934429.1 (168,447.42)
5 4/11/24 17:10 17:31 Y 68,960,488.81 68627496.9 332,991.91
6 4/11/24 17:44 18:05 Y 69,359,000.25 69080907.4 278,092.85
7 4/11/24 18:17 18:38 Y 69,249,115.60 68589998.3 659,117.30
8 4/11/24 19:01 19:22 Y 68,873,756.34 70583163.1 (1,709,406.76)
9 4/11/24 19:33 19:54 Y 69,329,241.45 71615374.5 (2,286,133.05)
10 4/11/24
11 4/11/24
12 4/11/24
13 4/11/24
En
t
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Us
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
14 4/11/24
15 4/11/24
16 4/11/24
Average = 69,012,770.47 69,382,344.62 369,574.16
Standard Deviation 980,869
Confidence Coefficient = 753961
RA - Relative Accuracy =1 1.6%
n = 9
t0.975 =2.306
Wet Volumetric Flow
wscfm
Run Date Start Time End Time RM CEM Diff
1 4/11/24 14:42 15:03 1,158,351.61
2 4/11/24 15:32 15:53 1,138,932.83
3 4/11/24 16:05 16:26 1,145,671.39
4 4/11/24 16:37 16:58 1,146,099.69
5 4/11/24 17:10 17:31 1,149,341.48
6 4/11/24 17:44 18:05 1,155,983.34
7 4/11/24 18:17 18:38 1,154,151.93
8 4/11/24 19:01 19:22 1,147,895.94
9 4/11/24 19:33 19:54 1,155,487.36
10 4/11/24
11 4/11/24
12 4/11/24
13 4/11/24
14 4/11/24
15 4/11/24
16 4/11/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
En
t
e
r

Us
e
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 2
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024
Start Time 14:42 15:32 16:05 16:37 17:10 17:44 18:17 19:01 19:33
Stop Time 15:03 15:53 16:26 16:58 17:31 18:05 18:38 19:22 19:54
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68
As ft^2 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90
Cp (Pitot Tube Coefficient)0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84
Yd Meter Y Factor (unit less)0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970 0.9970
Pbar Barometric Pressure ("Hg)23.87 23.87 23.87 23.87 23.87 23.87 23.87 23.87 23.87 23.87 23.87 23.87
Pq (Static Pressure)-5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30 -5.30
Ps (Pressure of the Stack)23.48 23.48 23.48 23.48 23.48 23.48 23.48 23.48 23.48 23.48 23.48 23.48
Ts Stack Temp Avg. oF 115.30 115.70 115.90 113.80 115.40 116.10 114.80 116.10 114.60
Tm Meter Temperature oF 73.00 73.00 77.00 77.00 80.00 80.00 82.00 82.00 83.00
CO2 (carbon dioxide)11.21 11.21 11.21 11.14 11.14 11.21 11.24 10.85 10.75
O2 (oxygen)6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00
Md Molecular Weight Dry 30.03 30.03 30.03 30.02 30.02 30.03 30.04 29.98 29.96 #VALUE!#VALUE!
Ms Molecular Weight Wet 28.48 28.46 28.45 28.53 28.48 28.49 28.51 28.40 28.45 #VALUE!#VALUE!
N2 (nitrogen)82.79 82.79 82.79 82.86 82.86 82.79 82.76 83.15 83.25 #VALUE!#VALUE!
Vm Sample Volume (cf)50.36 50.36 50.53 50.53 50.55 50.55 50.53 50.53 34.05 0.00 0.00 0.00
Vm std Standard Volume (dscf)39.66 39.66 39.50 39.50 39.30 39.30 39.14 39.14 26.32
Vlc Moisture (g)126.50 126.50 133.80 133.80 121.20 121.20 131.80 131.80 87.10
Vwstd Moisture Volume (scf)5.95 5.95 6.30 6.30 5.70 5.70 6.20 6.20 4.10
Bws Moisture Content (%100)13.31%13.31%13.93%13.93%12.80%12.80%13.75%13.75%13.52%
S Bws (saturation moisture)12.90%13.05%13.12%12.36%12.94%13.20%12.72%13.20%12.65%
AvgSqrtDlp √∆P 0.722 0.709 0.717 0.716 0.717 0.722 0.721 0.716 0.721
Vs. Gas Velocity (ft./sec)47.20 47.20 47.20 47.20 47.20 47.20 47.20 47.20 47.20 47.20 47.20 47.20
Qa (stack actual flow rate) acfm 1,608,290 1,582,428 1,592,343 1,587,130 1,596,057 1,607,234 1,601,066 1,595,989 1,602,361
Qs (stack std. flow rate) dscfm 1,008,907 990,326 995,340 1,004,387 1,002,228 1,008,020 1,007,339 996,422 1,009,335 #VALUE!#VALUE!#VALUE!
Qsd (stack std. flow rate) dscfh 60,534,429 59,419,542 59,720,399 60,263,202 60,133,700 60,481,203 60,440,349 59,785,309 60,560,072
Qw (stack flow rate) wscfm 69,501,096 68,335,970 68,740,284 68,765,982 68,960,489 69,359,000 69,249,116 68,873,756 69,329,241
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 2
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024 4/11/2024
Heat Input - BTU/hr.
F factor - scf/MMBtu 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0 1800.0
Fuel Analysis - ft3/min 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0
Fuel Flow - ft3/min 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
Heat Input - BTU/hr.0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
SO2 Concentrations
Uncorrected 17.10 14.60 15.70 14.80 14.50 15.50 15.50 16.00 16.00
Dry Corrected 17.37 14.91 16.06 15.13 14.78 15.85 15.85 16.35 16.31
Wet Corrected
NOx Concentrations
Uncorrected 95.50 97.70 98.60 98.50 98.20 97.20 97.50 98.00 97.00
Dry Corrected 96.72 100.81 102.08 101.71 101.53 100.81 101.17 100.49 99.34
Wet Corrected
CO Concentrations
Uncorrected 101.60 60.20 86.90 75.50 63.20 82.70 131.30 209.30 254.10
Dry Corrected 101.86 61.28 88.11 77.07 65.96 83.79 130.17 212.15 255.57
Wet Corrected
CO2 Concentrations
Uncorrected 11.30 11.30 11.30 11.30 11.30 11.30 11.40 11.00 10.90
Dry Corrected 11.21 11.21 11.21 11.14 11.14 11.21 11.24 10.85 10.75
Wet Corrected
O2 Concentrations
Uncorrected 6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00
Dry Corrected 6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00 6.00
Wet Corrected
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.043 0.195 0.142 Average % concentration
lbs./hr.CO2 O2
ppm or % 15.85 100.52 119.55 11.11 6.00
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)4.64E-02 1.86E-01 1.19E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.887E-06 1.155E-05 7.406E-06
lbs./hr.174.74 699.37 448.33 11.21 6.00
ppm or %17.37 96.72 101.86 11.30 6.00
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)3.98E-02 1.93E-01 7.16E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.477E-06 1.204E-05 4.455E-06
lbs./hr.147.19 715.53 264.74 11.21 6.00
ppm or %14.91 100.81 61.28 11.30 6.00 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)4.29E-02 1.96E-01 1.03E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.668E-06 1.219E-05 6.406E-06
lbs./hr.159.36 728.22 382.60 11.21 6.00
ppm or %16.06 102.08 88.11 11.30 6.00 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)4.06E-02 1.96E-01 9.05E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.514E-06 1.215E-05 5.603E-06
lbs./hr.151.49 732.11 337.68 11.14 6.00
ppm or %15.13 101.71 77.07 11.30 6.00 Raw Value
Run 5
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)3.97E-02 1.96E-01 7.75E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.456E-06 1.213E-05 4.796E-06
lbs./hr.147.72 729.3055 288.41 11.14 6.00
ppm or %14.78 101.53 65.97 11.30 6.00 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
O2
CO2
Clear
lbs./MMBTU
Run 6
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)4.23E-02 1.93E-01 9.79E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.635E-06 1.204E-05 6.092E-06
lbs./hr.159.36 728.2895 368.46 11.21 6.00
ppm or %15.85 100.81 83.79 11.30 6.00 Raw Value
Run 7
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)4.22E-02 1.93E-01 1.52E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.635E-06 1.208E-05 9.464E-06
lbs./hr.159.25 730.41 572.04 11.24 6.00
ppm or %15.85 101.17 130.17 11.40 6.00 Raw Value
Run 8
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)4.51E-02 1.99E-01 2.56E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.717E-06 1.200E-05 1.542E-05
lbs./hr.162.46 717.66 922.19 10.85 6.00
ppm or %16.35 100.49 212.15 11.00 6.00 Raw Value
Run 9
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)4.54E-02 1.99E-01 3.11E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.710E-06 1.187E-05 1.858E-05
lbs./hr.164.14 718.59 1125.35 10.75 6.00
ppm or %16.31 99.34 255.57 10.90 6.00 Raw Value
Run 10
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
Run 11
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
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Huntington Unit 2 RATA RM 1, 2G, 3A, 6C, 7E, 10, & 19 (Tested 4-11-2024)-2G
Calibration Error Test
Test Date April 11, 2024 O2
CS - Cal. Span 20.00
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 10.00 10.00 0.00 0.00% Passed Cal.
High-level 20.00 20.00 0.00 0.00% 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 50.00%
100% of Cal. Span High-level 100.00%
Test Date April 11, 2024 CO2
CS - Cal. Span 17.82
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 8.93 9.00 0.07 0.421% Passed Cal.
High-level 17.82 17.60 0.22 1.235% 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 50.08%
100% of Cal. Span High-level 100.00%
Test Date April 11, 2024 SO2
CS - Cal. Span 63.53
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 0.315% Passed Cal.
Mid-level 26.88 26.70 0.18 0.283% Passed Cal.
High-level 63.53 64.20 0.67 1.055% 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 42.31%
100% of Cal. Span High-level 100.00%
Test Date April 11, 2024 NOx
CS - Cal. Span 331.40
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 -0.30 0.30 0.091% Passed Cal.
Mid-level 152.30 151.00 1.30 0.392% Passed Cal.
High-level 331.40 332.90 1.50 0.453% 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 45.96%
100% of Cal. Span High-level 100.00%
Test Date April 11, 2024 CO
CS - Cal. Span 325.30
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 -0.50 0.50 0.154% Passed Cal.
Mid-level 151.80 153.10 1.30 0.400% Passed Cal.
High-level 325.30 328.10 2.80 0.861% 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 46.66%
100% of Cal. Span High-level 100.00%