DAQ-2025-003133

1
DAQC-619-25
Site ID 10237 (B5)

MEMORANDUM

TO: CEM FILE – PACIFICORP HUNTER PLANT

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Rob Leishman, Environmental Scientist

DATE: June 27, 2025

SUBJECT: Source: Unit #3 – Coal Fired Steam Turbine Generators
Contact: Jay Howard – 435-748-6519
Tom Wiscomb – 801-220-2373
Location: State Highway 10, Castle Dale, Emery County, UT
Test Contractor: Montrose Air Quality Services, LLC
FRS ID#: UT0000004901500101
Permit/AO#: Title V operating permit 1500101004, dated September 4, 2020
Last Revised November 19, 2021
Subject: Review of Relative Accuracy/Performance Specification Test
Report dated December 12, 2024
On December 24, 2024, the Utah Division of Air Quality (DAQ) received a Relative
Accuracy/Performance Specification Test (RA/PST) report for the Hunter Power Plant Unit #3 CEM in
Castle Dale, UT. Testing was performed on November 20, 2024, to determine the relative accuracy of the
Flow, CO2, NOX, SO2, and CO monitoring systems. The DAQ-calculated test results are:

RA/PST EVALUATION:

Unit No. 3
NSPS RATA - Test Date – November 20, 2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status
SO2 Thermo Fisher 43i 07330258 71 ppm 25.344 23.691 3.4% Passed lbs/MMBtu 0.086 0.083 6.0% Passed
lbs/hr 158.889 139.850 14.6% Passed
CO2 Thermo Fisher 48i 07330258 92 % 8.820 8.580 3.1% Passed
NOx Thermo Fisher 42i 07330258 45 ppm 89.256 85.222 1.2% Passed lbs/MMBtu 0.218 0.214 0.9% Passed
lbs/hr 402.622 361.992 12.0% Passed
CO Thermo Fisher 48i 07330258 64 ppm 15.333 5.294 1.4% Passed lbs/MMBtu 0.023 0.008 8.7% Passed lbs/hr 42.122 13.716 1.4% Passed
Volumetric Flow Rate wscfh 37773827.9 39289902.6 4.5% 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. 3
Acid Rain Test - Test Date – November 20, 2024
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status Testing
Frequency
SO2 Thermo Fisher 43i 07330258 71 ppm 25.34 23.69 10.00% Passed Annual
NOx Thermo Fisher 42i 07330258 45 lbs/MMBtu 0.21 0.21 2.40% Passed Annual
CO2 Thermo Fisher 48i 07330258 92 % 8.82 8.58 3.10% Passed
NOx Relative Accuracy Tests that exceed 7.5% - For units where the average of the monitoring system
measurements of NOx emission rate during the RATA is less than or equal to 0.020 lbs/MMBtu, the mean value of
the NOx continuous emission monitoring system measurements shall not exceed +0.025 lbs/MMBtu of the
reference method mean value wherever the relative accuracy specification of 10.0 percent is not achieved.

SO2 Relative Accuracy Tests that exceed 7.5% and have a deviation that is < 12 ppm pass and qualifies for annual
testing.
Equation - Di (Rmi – CEMi)
Rmi = 0.2136
CEMi = 0.2178
Di = 0.0042 Passed

DEVIATIONS: No deviations were noted in this report.

CONCLUSION: Pacificorp Hunter Power Plant operates the continuous emissions
monitor (CEM) on the Unit #3 stack to measure Flow, CO2, NOX, SO2,
and CO emissions. The CEM was 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 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 Hunter Power Plant Unit #3 CEM system was operating
as required in R307-170 and 40 CFR 60.13 at the time of this evaluation.

HPV: No.

ATTACHMENTS: RATA Review Spreadsheets.
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name PacifiCorp Hunter
Company Contact:Terry Guthrie
Contact Phone No.435-748-6059
Stack Designation:Unit No. 3
Test & Review Dates
Test Date:11/20/2024
Review Date: 6/25/2025
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.1200 0.5500 0.2000 0.083 0.214 0.008
lbs./hr. 2406.0 13.716
ppm 53.9 343.6 838.00 23.691 85.222 5.294
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
307.44 515.523 0.9970 1.741 0.838 24.76 -5.5 24.355588
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
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Company PacifiCorp Hunter
Point Source Unit No. 3
Test Date 11/20/24
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
Load
MW
Heat
MMBtu/hr
Flow
WSCFH
7:43 8:04 1 37.8 0.021 8.4 13.2 438.3 0.238 93.3 153.1 0.083 23.4 185 1844.2 39352955.6
8:34 8:55 2 39.6 0.021 8.7 14.2 414.6 0.223 90.5 155.1 0.083 24.3 186 1855.5 38370414.9
9:08 9:29 3 47 0.025 8.9 17.3 399.1 0.215 88.7 160.9 0.086 25.7 184 1858.5 37668646.2
9:43 10:04 4 43 0.023 8.9 15.6 399.8 0.215 88.7 161.5 0.087 25.8 185 1863.4 37746550.7
10:17 10:38 5 42.6 0.023 8.9 15.6 395.6 0.213 88.3 161 0.087 25.8 184 1857.5 37567214.1
10:52 11:13 6 42.8 0.023 8.9 15.6 398.2 0.214 88.7 159.1 0.088 25.5 184 1858.1 376193201
11:26 11:47 7 42.7 0.023 8.9 15.7 393.8 0.214 88.3 151.8 0.083 24.5 185 1844.2 37357478.8
12:01 12:22 8 41.4 0.023 8.9 15.3 391.8 0.214 88.3 168.3 0.092 27.3 184 1830.9 37146817.4
12:35 12:56 9 42.2 0.023 8.9 15.5 392.4 0.214 88.5 159.2 0.087 25.8 185 1830.2 37135053.6
10
11
12
13
14
15
16
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:53.88 0.12
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
11/20/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 11/20/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 7:43 8:04 Y 21.4 23.4 -2.01 Y 0.0775 0.083 -0.005 Y 131.95 153.1 -21.1 1 7:43 8:04 Y 8.3 8.4 -0.14
2 8:34 8:55 Y 22.4 24.3 -1.91 Y 0.0792 0.083 -0.004 Y 134.13 155.1 -21.0 2 8:34 8:55 Y 8.5 8.7 -0.25
3 9:08 9:29 Y 23.8 25.7 -1.92 Y 0.0822 0.086 -0.004 Y 141.46 160.9 -19.4 3 9:08 9:29 Y 8.6 8.9 -0.25
4 9:43 10:04 Y 24.2 25.8 -1.58 Y 0.0838 0.087 -0.003 Y 141.63 161.5 -19.9 4 9:43 10:04 Y 8.6 8.9 -0.25
5 10:17 10:38 Y 24.2 25.8 -1.59 Y 0.0837 0.087 -0.003 Y 142.67 161 -18.3 5 10:17 10:38 Y 8.6 8.9 -0.25
6 10:52 11:13 Y 24.1 25.5 -1.42 Y 0.0833 0.088 -0.005 Y 140.78 159.1 -18.3 6 10:52 11:13 Y 8.6 8.9 -0.25
7 11:26 11:47 Y 22.8 24.5 -1.68 Y 0.0789 0.083 -0.004 Y 132.33 151.8 -19.5 7 11:26 11:47 Y 8.6 8.9 -0.25
8 12:01 12:22 Y 25.9 27.3 -1.37 Y 0.0897 0.092 -0.002 Y 149.96 168.3 -18.3 8 12:01 12:22 Y 8.6 8.9 -0.25
9 12:35 12:56 Y 24.4 25.8 -1.40 Y 0.0844 0.087 -0.003 Y 143.72 159.2 -15.5 9 12:35 12:56 Y 8.6 8.9 -0.25
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 23.7 25.34 1.65 0.083 0.086 0.004 139.9 158.889 19.039 Average = 8.580 8.820 0.238
Sd Standard Deviation = 0.24 Sd Standard Deviation = 0.001 Sd Standard Deviation = 1.709 Sd Standard Deviation = 0.04
Confidence Coefficient = 0.19 Confidence Coefficient = 0.001 Confidence Coefficient = 1.3 Confidence Coefficient = 0.027
RA - Relative Accuracy = RA 6.00%RA 14.60%RA - Relative Accuracy =3.08%
n = 9 9 9 n = 9 or RA of 1%0.24%
t0.975 = 2.306 2.306 2.306 t0.975 = 2.306
E.L. Relative Accuracy = 44% 3.42% 69%
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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Thermo Fisher 43i 07330258 71
07330258 92Thermo Fisher 48i
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PassedPassedPassedPassed
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Hunter
Unit No. 3
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:343.57 0.55
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
11/20/2024 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 7:43 8:04 Y 88.8 93.3 -4.5 Y 0.231 0.238 -0.007 Y 393.85 438.3 -44.45 1 7:43 8:04 9.0
2 8:34 8:55 Y 86.2 90.5 -4.3 Y 0.219 0.223 -0.004 Y 371.28 414.6 -43.32 2 8:34 8:55 9.0
3 9:08 9:29 Y 84.8 88.7 -3.9 Y 0.211 0.215 -0.004 Y 362.55 399.1 -36.55 3 9:08 9:29 9.0
4 9:43 10:04 Y 84.9 88.7 -3.8 Y 0.211 0.215 -0.004 Y 356.97 399.8 -42.83 4 9:43 10:04 9.0
5 10:17 10:38 Y 84.4 88.3 -3.9 Y 0.210 0.213 -0.003 Y 357.35 395.6 -38.25 5 10:17 10:38 9.0
6 10:52 11:13 Y 84.7 88.7 -4.0 Y 0.211 0.214 -0.003 Y 355.91 398.2 -42.29 6 10:52 11:13 9.0
7 11:26 11:47 Y 84.3 88.3 -4.0 Y 0.210 0.214 -0.004 Y 351.44 393.8 -42.36 7 11:26 11:47 9.0
8 12:01 12:22 Y 84.3 88.3 -4.0 Y 0.210 0.214 -0.004 Y 350.43 391.8 -41.37 8 12:01 12:22 9.0
9 12:35 12:56 Y 84.6 88.5 -3.9 Y 0.210 0.214 -0.004 Y 358.14 392.4 -34.26 9 12:35 12:56 9.0
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 85.2 89.3 4.033 0.21 0.218 0.004 361.99 402.62 40.63 Average =
Sd Standard Deviation = 0.21 Sd Standard Deviation = 0.001 Sd Standard Deviation = 3.461 Sd Standard Deviation =
Confidence Coefficient = 0.164 Confidence Coefficient = 0.001 Confidence Coefficient = 2.660 Confidence Coefficient =
RA - Relative Accuracy = Relative Accuracy = Relative Accuracy =12.00%RA - Relative Accuracy =
n = 9 9 9 n = 0 or RA of 1%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = 2.306 t0.975 =
E.L. Relative Accuracy = 25% 1.22% EMRA 39% 0.91% 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
07330258 45Thermo Fisher 42i
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PassedPassedPassed
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Hunter
Unit No. 3
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:838.00 0.200 2406.00
Date CO Dry CO Dry CO
11/20/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 7:43 8:04 Y 3.94 13.2 9.26 Y 0.006 0.021 0.015 Y 10.64 37.8 27.16
2 8:34 8:55 Y 6.66 14.2 7.54 Y 0.010 0.021 0.011 Y 17.45 39.6 22.15
3 9:08 9:29 Y 7.94 17.3 9.36 Y 0.012 0.025 0.013 Y 20.66 47 26.34
4 9:43 10:04 Y 7.34 15.6 8.26 Y 0.011 0.023 0.012 Y 18.79 43 24.22
5 10:17 10:38 Y 7.07 15.6 8.53 Y 0.011 0.023 0.012 Y 18.22 42.6 24.38
6 10:52 11:13 Y 7.04 15.6 8.56 Y 0.011 0.023 0.012 Y 18.02 42.8 24.78
7 11:26 11:47 Y 1.01 15.7 14.69 Y 0.002 0.023 0.021 Y 2.55 42.7 40.15
8 12:01 12:22 Y 0.55 15.3 14.75 Y 0.001 0.023 0.022 Y 1.40 41.4 40.00
9 12:35 12:56 Y 6.10 15.5 9.40 Y 0.009 0.023 0.014 Y 15.72 42.2 26.48
10
11
12
13
14
15
16
Average = 5.29 15.33 10.04 0.008 0.023 0.015 13.72 42.12 28.41
Sd Standard Deviation = 2.72 0.004 6.780
Confidence Coefficient = 2.091 0.002 5.21
RA - Relative Accuracy =
n = 9 9 9
t0.975 = 2.306 2.306 2.306
E.L. Relative Accuracy = 1%1.45%4% 8.65% 1% 1.40%
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
07330258 64
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 Passed
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Thermo Fisher 48i
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:53.88 0.12
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
11/20/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 11/20/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 7:43 8:04 Y 21.4 23.4 -2.01 0.0775 131.95 1 7:43 8:04 Y 8.3 8.4 -0.14
2 8:34 8:55 Y 22.4 24.3 -1.91 0.0792 134.13 2 8:34 8:55 Y 8.5 8.7 -0.25
3 9:08 9:29 Y 23.8 25.7 -1.92 0.0822 141.46 3 9:08 9:29 Y 8.6 8.9 -0.25
4 9:43 10:04 Y 24.2 25.8 -1.58 0.0838 141.63 4 9:43 10:04 Y 8.6 8.9 -0.25
5 10:17 10:38 Y 24.2 25.8 -1.59 0.0837 142.67 5 10:17 10:38 Y 8.6 8.9 -0.25
6 10:52 11:13 Y 24.1 25.5 -1.42 0.0833 140.78 6 10:52 11:13 Y 8.6 8.9 -0.25
7 11:26 11:47 Y 22.8 24.5 -1.68 0.0789 132.33 7 11:26 11:47 Y 8.6 8.9 -0.25
8 12:01 12:22 Y 25.9 27.3 -1.37 0.0897 149.96 8 12:01 12:22 Y 8.6 8.9 -0.25
9 12:35 12:56 Y 24.4 25.8 -1.40 0.0844 143.72 9 12:35 12:56 Y 8.6 8.9 -0.25
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 23.7 25.34 1.650 Average = 8.584 8.822 0.24
Sd Standard Deviation =0.24 Sd Standard Deviation =0.04
Confidence Coefficient =0.73 Confidence Coefficient =0.027
RA - Relative Accuracy =10.00%RA - Relative Accuracy =3.10%
n =9 n =0 n =0 n =9 or RA of 1%0.24%
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 RAc 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
2.4 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
Thermo Fisher 43i 07330258 71
Thermo Fisher 48i 07330258 92
Passed
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PassedPass _ Semiannual Test
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Hunter
Unit No. 3
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System:Serial No.:
Equivalent Emission Limit:343.57 0.55
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
11/20/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 11/20/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time
End
Time %c %c
1 7:43 8:04 88.8 Y 0.231 0.238 -0.00666 393.85 1 7:43 8:04 9.0
2 8:34 8:55 86.2 Y 0.219 0.223 -0.00373 371.28 2 8:34 8:55 9.0
3 9:08 9:29 84.8 Y 0.211 0.215 -0.00421 362.55 3 9:08 9:29 9.0
4 9:43 10:04 84.9 Y 0.211 0.215 -0.00386 356.97 4 9:43 10:04 9.0
5 10:17 10:38 84.4 Y 0.210 0.213 -0.00329 357.35 5 10:17 10:38 9.0
6 10:52 11:13 84.7 Y 0.211 0.214 -0.00347 355.91 6 10:52 11:13 9.0
7 11:26 11:47 84.3 Y 0.210 0.214 -0.00440 351.44 7 11:26 11:47 9.0
8 12:01 12:22 84.3 Y 0.210 0.214 -0.00445 350.43 8 12:01 12:22 9.0
9 12:35 12:56 84.6 Y 0.210 0.214 -0.00375 358.14 9 12:35 12:56 9.0
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 0.214 0.218 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 =2.40%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)-0.004
Alterative RA Passed
Thermo Fisher 42i 07330258 45
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Actual Volumetric Flow
acfm
Run Date Start Time End Time RM CEM Diff
1 11/20/24 7:43 8:04 900,350.61
2 11/20/24 8:34 8:55 874,584.77
3 11/20/24 9:08 9:29 868,274.77
4 11/20/24 9:43 10:04 853,489.57
5 11/20/24 10:17 10:38 860,232.61
6 11/20/24 10:52 11:13 853,427.71
7 11/20/24 11:26 11:47 846,437.21
8 11/20/24 12:01 12:22 844,179.22
9 11/20/24 12:35 12:56 859,892.36
10 11/20/24
11 11/20/24
12 11/20/24
13 11/20/24
14 11/20/24
15 11/20/24
16 11/20/24
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 11/20/24 7:43 8:04 Y 41,022,750.97 39352955.6 1,669,795.37
2 11/20/24 8:34 8:55 Y 39,848,779.84 38370414.9 1,478,364.94
3 11/20/24 9:08 9:29 Y 39,561,276.71 37668646.2 1,892,630.51
4 11/20/24 9:43 10:04 Y 38,887,617.41 37746550.7 1,141,066.71
5 11/20/24 10:17 10:38 Y 39,194,851.15 37567214.1 1,627,637.05
6 11/20/24 10:52 11:13 Y 38,884,798.75 37619320 1,265,478.75
7 11/20/24 11:26 11:47 Y 38,566,290.37 37357478.8 1,208,811.57
8 11/20/24 12:01 12:22 Y 38,463,409.35 37146817.4 1,316,591.95
9 11/20/24 12:35 12:56 Y 39,179,348.53 37135053.6 2,044,294.93
10 11/20/24
11 11/20/24
12 11/20/24
13 11/20/24
En
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Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
14 11/20/24
15 11/20/24
16 11/20/24
Average = 39,289,902.56 37,773,827.92 1,516,074.64
Standard Deviation 315,425
Confidence Coefficient = 242457
RA - Relative Accuracy =1 4.5%
n = 9
t0.975 =2.306
Wet Volumetric Flow
wscfm
Run Date Start Time End Time RM CEM Diff
1 11/20/24 7:43 8:04 683,712.52
2 11/20/24 8:34 8:55 664,146.33
3 11/20/24 9:08 9:29 659,354.61
4 11/20/24 9:43 10:04 648,126.96
5 11/20/24 10:17 10:38 653,247.52
6 11/20/24 10:52 11:13 648,079.98
7 11/20/24 11:26 11:47 642,771.51
8 11/20/24 12:01 12:22 641,056.82
9 11/20/24 12:35 12:56 652,989.14
10 11/20/24
11 11/20/24
12 11/20/24
13 11/20/24
14 11/20/24
15 11/20/24
16 11/20/24
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
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Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Hunter
Point Source Unit No. 3
Contact Phone No.Terry Guthrie
Stack Designation:Unit No. 3
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 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024
Start Time 7:43 8:34 9:08 9:43 10:17 10:52 11:26 12:01 12:35
Stop Time 8:04 8:55 9:29 10:04 10:38 11:13 11:47 12:22 12:56
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)307.44 307.44 307.44 307.44 307.44 307.44 307.44 307.44 307.44 307.44 307.44 307.44
As ft^2 515.52 515.52 515.52 515.52 515.52 515.52 515.52 515.52 515.52 515.52 515.52 515.52
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)24.76 24.76 24.76 24.76 24.76 24.76 24.76 24.76 24.76 24.76 24.76 24.76
Pq (Static Pressure)-5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50 -5.50
Ps (Pressure of the Stack)24.36 24.36 24.36 24.36 24.36 24.36 24.36 24.36 24.36 24.36 24.36 24.36
Ts Stack Temp Avg. oF 106.00 106.00 106.00 106.00 106.00 106.00 106.00 106.00 106.00
Tm Meter Temperature oF 53.00 53.00 57.00 57.00 59.00 59.00 60.00 60.00 61.00
CO2 (carbon dioxide)8.26 8.45 8.65 8.65 8.65 8.65 8.65 8.65 8.65
O2 (oxygen)9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00
Md Molecular Weight Dry 29.68 29.71 29.74 29.74 29.74 29.74 29.74 29.74 29.74 #VALUE!#VALUE!
Ms Molecular Weight Wet 28.57 28.60 28.62 28.62 28.62 28.62 28.62 28.62 28.62 #VALUE!#VALUE!
N2 (nitrogen)82.74 82.55 82.35 82.35 82.35 82.35 82.35 82.35 82.35 #VALUE!#VALUE!
Vm Sample Volume (cf)45.54 45.54 45.37 45.37 45.59 45.59 41.98 41.98 27.05 0.00 0.00 0.00
Vm std Standard Volume (dscf)38.66 38.66 38.21 38.21 38.25 38.25 35.15 35.15 22.61
Vlc Moisture (g)88.00 88.00 111.90 111.90 91.30 91.30 115.80 115.80 53.80
Vwstd Moisture Volume (scf)4.14 4.14 5.27 5.27 4.30 4.30 5.45 5.45 2.53
Bws Moisture Content (%100)10.22%10.22%12.69%12.69%10.55%10.55%13.98%13.98%11.64%
S Bws (saturation moisture)9.52%9.52%9.52%9.52%9.52%9.52%9.52%9.52%9.52%
AvgSqrtDlp √∆P 0.457 0.443 0.444 0.436 0.437 0.433 0.434 0.433 0.438
Vs. Gas Velocity (ft./sec)29.11 29.11 29.11 29.11 29.11 29.11 29.11 29.11 29.11 29.11 29.11 29.11
Qa (stack actual flow rate) acfm 900,351 874,585 868,275 853,490 860,233 853,428 846,437 844,179 859,892
Qs (stack std. flow rate) dscfm 618,637 600,933 596,597 586,438 591,071 586,396 581,593 580,041 590,838 #VALUE!#VALUE!#VALUE!
Qsd (stack std. flow rate) dscfh 37,118,206 36,055,973 35,795,835 35,186,294 35,464,286 35,183,744 34,895,551 34,802,463 35,450,259
Qw (stack flow rate) wscfm 41,022,751 39,848,780 39,561,277 38,887,617 39,194,851 38,884,799 38,566,290 38,463,409 39,179,349
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Hunter
Point Source Unit No. 3
Contact Phone No.Terry Guthrie
Stack Designation:Unit No. 3
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 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024 11/20/2024
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 21.40 22.40 23.80 24.40 24.30 24.00 22.90 26.00 24.30
Dry Corrected 21.39 22.39 23.78 24.22 24.21 24.08 22.82 25.93 24.40
Wet Corrected
NOx Concentrations
Uncorrected 88.20 85.70 84.10 84.10 83.50 83.80 83.40 83.30 83.50
Dry Corrected 88.83 86.21 84.79 84.93 84.36 84.69 84.31 84.30 84.58
Wet Corrected
CO Concentrations
Uncorrected 3.00 3.90 4.80 3.70 2.80 1.80 1.00 0.10 -0.60
Dry Corrected 3.94 6.66 7.94 7.34 7.07 7.04 1.01 0.55 6.10
Wet Corrected
CO2 Concentrations
Uncorrected 8.40 8.60 8.80 8.80 8.80 8.80 8.80 8.80 8.80
Dry Corrected 8.26 8.45 8.65 8.65 8.65 8.65 8.65 8.65 8.65
Wet Corrected
O2 Concentrations
Uncorrected 9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00
Dry Corrected 9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00 9.00
Wet Corrected
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.083 0.214 0.008 Average % concentration
lbs./hr.13.72 CO2 O2
ppm or % 23.69 85.22 5.29 8.58 9.00
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.12E-02 3.35E-02 9.06E-04 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)7.75E-02 2.31E-01 6.25E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.555E-06 1.061E-05 2.866E-07
lbs./hr.131.95 393.85 10.64 8.26 9.00
ppm or %21.39 88.83 3.94 8.40 9.00
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.18E-02 3.26E-02 1.53E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)7.92E-02 2.19E-01 1.03E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.720E-06 1.030E-05 4.841E-07
lbs./hr.134.13 371.28 17.45 8.45 9.00
ppm or %22.39 86.21 6.66 8.40 9.00 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.25E-02 3.20E-02 1.82E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.22E-02 2.11E-01 1.20E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.952E-06 1.013E-05 5.770E-07
lbs./hr.141.46 362.55 20.66 8.65 9.00
ppm or %23.78 84.79 7.94 8.80 9.00 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.27E-02 3.21E-02 1.69E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.38E-02 2.11E-01 1.11E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.025E-06 1.015E-05 5.339E-07
lbs./hr.141.63 356.97 18.78 8.65 9.00
ppm or %24.22 84.93 7.34 8.80 9.00 Raw Value
Run 5
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.27E-02 3.19E-02 1.62E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.37E-02 2.10E-01 1.07E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.023E-06 1.008E-05 5.137E-07
lbs./hr.142.67 357.3524 18.22 8.65 9.00
ppm or %24.21 84.36 7.07 8.80 9.00 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
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Hunter
Unit No. 3
O2
CO2
Clear
lbs./MMBTU
Run 6
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.26E-02 3.20E-02 1.62E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.33E-02 2.11E-01 1.07E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.001E-06 1.012E-05 5.121E-07
lbs./hr.140.78 355.9124 18.02 8.65 9.00
ppm or %24.08 84.69 7.04 8.80 9.00 Raw Value
Run 7
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.20E-02 3.18E-02 2.31E-04 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)7.89E-02 2.10E-01 1.52E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.792E-06 1.007E-05 7.319E-08
lbs./hr.132.33 351.44 2.55 8.65 9.00
ppm or %22.82 84.31 1.01 8.80 9.00 Raw Value
Run 8
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.36E-02 3.18E-02 1.27E-04 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.97E-02 2.10E-01 8.39E-04 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.309E-06 1.007E-05 4.030E-08
lbs./hr.149.96 350.43 1.40 8.65 9.00
ppm or %25.93 84.30 0.55 8.80 9.00 Raw Value
Run 9
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)1.28E-02 3.19E-02 1.40E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.44E-02 2.10E-01 9.23E-03 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.054E-06 1.010E-05 4.433E-07
lbs./hr.143.72 358.14 15.72 8.65 9.00
ppm or %24.40 84.58 6.10 8.80 9.00 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
Pacificorp Hunter Unit 3 RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10, & 19 - RA (Tested 11-20-2024)
Calibration Error Test
Test Date November 20, 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 November 20, 2024 CO2
CS - Cal. Span 17.85
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 8.94 9.10 0.16 0.874% Passed Cal.
High-level 17.85 17.80 0.05 0.280% 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 50.11%
100% of Cal. Span High-level 100.00%
Test Date November 20, 2024 SO2
CS - Cal. Span 146.90
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 -0.10 0.10 0.068% Passed Cal.
Mid-level 65.02 65.20 0.18 0.123% Passed Cal.
High-level 146.90 147.60 0.70 0.477% 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 44.26%
100% of Cal. Span High-level 100.00%
Test Date November 20, 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 151.40 150.30 1.10 0.332% Passed Cal.
High-level 331.40 333.30 1.90 0.573% 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 45.68%
100% of Cal. Span High-level 100.00%
Test Date November 20, 2024 CO
2406 CS - Cal. Span 328.30
838 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 0.60 0.60 0.183% Passed Cal.
Mid-level 150.50 151.00 0.50 0.152% Passed Cal.
High-level 328.30 328.40 0.10 0.030% 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 45.84%
100% of Cal. Span High-level 100.00%
Yr.*slflF."g"n"r Hunter Plant
1000 South Highway l0
P.O. Box 569
Castle Dale, UT 8451 3
RE:
December 12,2024
Mr. Bryce Bird, Director
Utah Department of Environmental Quality
Division of Air Quality
195 North 1950 West
P.O. Box 144820
Salt Lake ciry, uT 84114-4820
Attention: Rob Leishman
2024 Relative Accuracy Test Audit - Hunter Power Plant Units 3.
(Title V Permit #150010f004)
Dear Mr. Bryce Bird:
The annual Relative Accuracy Test Audits (RATAs) for the Continuous Emission Monitoring Systems
(CEMS) in service at PacifiCorp's Hunter Power Plant were completed per the provisions found in 40 CFR
Parts 60 and 75. This report is for; Unit 3: CEMS for Volumetric Flow, CO, CO2, NOx, and SO2. The
RATAs were conducted during the period of November 19 -20.
Enclosed are the RATA Test Reports for Hunter Units 3.
I am authorized to make this submission on behalf of the ownens and operators of the affected source
or affected units for which the submission is made. I certiS under penalty of law that I have
personally examined, and am familiar with, the statements and information submitted in this
document and all its attachments. Based on my inquily of those individuals with primary
responsibility for obtaining the information, I certi$ 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 statements and information,
including the possibility of fines or imprisonment.
Should you have any questions regarding this information, please contact Jay Howard, Hunter Plant Senior
I Analyst at [phone].
Managing Director Hunter Power Plant
Responsible Official
Enclosures:
Director, USEPA Region VIII, w/enclosures
Terry Guthrie - Hunter Plant
Tom Wiscomb - PacifiCorp
[)i\/I.SION OF AIR QUAI.ITY
Source Test Report for 2O24 RATA
Unit 3
PacifiCorp
Hunter Power Plant
Castle Dale, Utah
Prepared For:
PacifiCorp
L4O7 W North Temple, Suite 210
Salt Lake City, Utah 84116
Prepared By:
Montrose Air Quality Services,
990 West 43rd Avenue
Denver, Colorado 80211
LLC
For Submission To:
Utah Division of Air Quality
195 North 1950 West
Salt Lake City, Utah 84116
Document Number: GPO43AS-O36892-RT-1768
Test Dates: November 19 & 20, 2(J24
Submitta! Date: December 20, 2024
Testing
rcMODAVCF .r[OlM MgNT+PIT srAe
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:
December 5,2024
Craig Kormylo Project Manager
I have reviewed, technically and editorially, details, calculations, results, conclusions, and
other appropriate written materials contained herein. I hereby ceftify that, to the best of my
knowledge, the presented material is authentic, accurate, and conforms to the requirements
of the Montrose Quality Management System and ASTM D7036-04.
Signature:
Name:
December 5,2024
Matthew Parks QA/QC Specialist
GP043AS-036892-RT- 1 789 Page 2 of 195
Table of Contents
Paqe
1.0 Introduction...... ............... 5
1.1 Summary of Test Program .................5
L.2 Key Personnel.......... .................7
2.0 Plant and Sampling Location Descriptions...... ,................9
2.t Process Description, Operation, and Control Equipment.... .................9
2.2 Flue Gas Sampling Locations ................. 9
2.3 Operating Conditions and Process Data...... ................10
2.4 CEMS Description ................10
3.0 Sampling and Analytical Procedures ............11
3.1 Test Methods........... ..........11
3.1.1 EPA Method 2G..... .......11
3.1.2 EPA Method 2H.,.... .........13
3.1.3 EPA Method 4.....,....... .........14
3.1.4 EPA Methods 3A, 6C, 7E, and 10 ...... .........16
3.2 Process Test Methods...,........ .............t7
4.0 Test Discussion and Resu1ts............ .......,.....18
4.L Field Test Deviations and Exceptions........ ...,.....18
4.2 Presentation of Resu1ts........... .............18
5.0 Internal QA/QC Activities .........19
5.1 QA/QC Audits .........19
5.2 QA/QC Discussion. .............19
5.3 Quality Statement ......19
List of Appendices
A Field Data and Calculations....... ................20
A.1 Sampling Locations.. .........2L
A.2 RATA Resu1ts.,......... ......23
A.2.1 Unit 3 ............. ......24
A.3 Field Data .....32
A,3.1 Unit 3.....,, .............33
A.3.1.1 High-Load Flow Data ............34
A.3.1.2 Mid-Load Flow Data.. .....51
A.3.1.3 Low-Load Flow Data .........7O
A.3.1.4 InstrumentalTest Method Data......... .....,............92
A.4 Example Calculations.,. ...........,.100
GP043AS-036892-RT- 1789 Page 3 of 195
B Facility Process Data........ ...109
B.1 Unit 3 ..............110
B.1.1 High-Load Flow RATA ................111
8.1.2 Mid-Load Flow RATA.. ..........121
8.1.3 Low-Load Flow RATA. ............131
B.1.4 Low-Load Gas RATAs .................t42
C Quality Assurance/Quality Control ..........153
C.1 Units and Abbreviations..... ...............154
C.2 ManualTest Method QA/QC Data........ ..........162
C.3 Instrumental Test Method QA/QC Data........ ..........L67
C.4 Calibration Gas Ceftificates..... .............183
C.5 Accreditation Information/Certifications .................191
List of Tables
Table 1-1 Summary of Test Pro9ram............. ............. 5
Table 1-2 Summary of RATA Results - Hunter Unit 3.........,... ..............6
Table 1-4 Test Personnel and Observers........... ..............8
Table 2-1 Sampling Locations............ ..............9
Table 2-2 CEMS Information ...............10
List of Figures
Figure 3-1 EPA Method 2G Sampling Train ...........12
Figure 3-2 EPA Method 4 Sampling Train........ ...............15
Figure 3-3 EPA Methods 3A, 6C, 7E, and 10 Sampling Train .............L7
GP043AS-036892-RT- 1789 Page 4 of 195
1.O Introduction
1.1 Summary of Test Program
PacifiCorp contracted Montrose Air Quality Services, LLC (Montrose) to perform a RATA test
program at Hunter Power Plant located in Castle Dale, Utah. The tests were conducted in
accordance with the requirements of UDEQ Operating Permit 01500101004 and (as
applicable) 40 CFR Pafts 60 and 75.
The specific objectives were to:
. Perform annual RATAs on the Volumetric Flow Rate, Carbon Dioxide, Sulfur
Dioxide, Nitrogen Oxides and Carbon Monoxide CEMS installed on Unit 3.
. Conduct the test program with a focus on safety
Montrose performed 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 repofting units are not
defined. Please refer to the list for specific details.
This report presents the test results and suppofting data, descriptions of the testing
procedures, descriptions of the facility and sampling locations, and a summary of the quality
assurance procedures used by Montrose. The average emission test results are summarized
and compared to their respective peformance specifications in Table 1-2. Detailed results
for individual test runs and all suppofting data can be found in the appendices.
The testing was conducted by the Montrose personnel listed in Table 1-3. The tests were
conducted according to the test plan (protocol) that was submitted to and approved by
UDEQ.
GP043AS-036892-RT-1 789 Page 5 of 195
rt/79/2024 Volumetric Flow Rate MTA
Volumetric Flow Rate RATA EPAM2G/H,3,4
Volumetric Flow Rate MTA
Oz, COz, SOz, NOr, CO EPA M3A, 6C,7E, and 10
Table 1-2
Summary of RATA Results - Hunter Unit 3
November 19 & 20, 2024
Part 6O
Sulfur Dioxide (SOz)
lblmmBtu PS-2 < 20.0olo of RM 5.4o/o
lblhr PS-6 < 20.0olo of RM 3.3o/o
Nitrogen Oxides (NO, as NOz)
ppmvw PS-2 < 2o.Oolo of RM 4.9o/o
lb/hr PS-6 < 20.0olo of RM O.9o/o
Carbon Monoxide (CO)
ppmvw PS-4A < 5olo of AS l.1o/o
lblmmBtu PS-6 < 10.00/o of AS 6.8o/o
lb/hr PS.6 < 10.0olo of AS l.Oolo
Paft 75
Volumetric Flow (Low Load)
wscfh App. B Sect, 2.3.1.2 Annual: < 7.5olo of RM 4.9o/o
Volumetric Flow (Mid Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 3.60/o
Volumetric Flow (High Load)
wscfh App, A Sect. 2.3.1.2 Annual: < 7.5olo of RM l.2o/o
Carbon Dioxide (COr)
o/o volume wet App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 2.5o/o
Sulfur Dioxide (SOz)
ppmvw App. B Sect. 2.3.1.2 Annual: ldl S 12.0 ppm !dl=1.6 ppm
Nitrogen Oxides (NOx as NOz)
lblmmBtu App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 2.60/o
Page 6 of 195GP043AS-036892-RT- 1 789
1.2 Key Personnel
A list of project participants is included below:
Facility Information
Source Location:
Project Contact:
PacifiCorp Hunter Power Plant
State Highway 10
Castle Dale, Utah 84513
Tom Wiscomb Jay Howard
Sr. Environmental Analyst
PacifiCorp
(43s) 748-6sL9
Jay. Howa rd @ Pacifi Corp. com
Role: Sr. Environmental Advisor
Company: PacifiCorp
Telephone: [phone]
Email : [e-mail]
Agency Information
Regulatory Agency:
Agency Contact:
Telephone:
Email:
Utah Department of Air Quality
Rob Leishman
(801) s36-4438
[e-mail]
Testing Company Information
Testing Firm:
Contact:
Title:
Telephone:
Email:
Montrose Air Quality Senrices, LLC
Craig Kormylo
District Manager
(303) 49s-3e36
CKormylo@montrose-env. com
GP043AS-036892 -RT- 1 789 Page 7 of 195
Test personnel and observers are summarized in Table 1-4.
Table 1-4
Test Personnel and Obserwers
Craig Kormylo
Project Manager
Qualified Individual (QI)
Trailer operator
Sample train operator
Mitchell Simmons
Sample train operator
Calculations and report preparation
Test CoordinatorTom Wiscomb
Plant Representative
GP043AS-036892-RT- 1789 Page 8 of 195
2.O Plant and Sampling Location Descriptions
2.1 Process Description, Operation, and Control
Equipment
The Hunter Plant comprises three pulverized coal-fired boilers. Hunter Unit #1 is a dry-
bottom, tangentially-fired boiler rated at 480 gross megawatts (GMW) and equipped with a
fabric-filter baghouse for particulate matter (PM) control and a flue gas desulfurization
(FGD) scrubber for sulfur dioxide (SOz) control. Hunter Unit #2 is a dry-bottom,
tangentially-fired boiler rated at 480 GMW and equipped with low-NO, burners and overfire
air for nitrogen oxides (NO,) control, a fabric filter baghouse for PM control and an FGD
scrubber for SOz control. Hunter Unit #3 is a dry-bottom, wall-fired boiler rated at 495
GMW and equipped with low-NO, burners and ovefire air for NOx control, a fabric filter
baghouse for PM control and an FGD scrubber for SOz control. In accordance with
Conditions II.B.2 and II.B.3 of Utah Department of Environmental Quality (UDEQ)
Operating Permit 1500101004, the Unit #1, Unit #2 and Unit #3 exhaust stacks are
equipped with Continuous Emission Monitoring Systems (CEMS) to quantify carbon dioxide
(COz), SOz and NO, emissions. Units 1, 2 and 3 are equipped with CEMS to quantify carbon
monoxide (CO) emissions for comparison to UDEQ permit limits.
2.2 Flue Gas Sampling Locations
Information regarding the sampling locations is presented in Table 2-1.
Table 2-1
Sampling Locations
See Appendix A.1 for more information.
Sample location(s) were verified in the field to conform to EPA Method 1.
GP043AS-036892-RT- 1 789 Page 9 of 195
2,3 Operating Conditions and Process Data
Emission tests were pefformed while the source/units and air pollution control devices were
operating at the conditions required by the relevant pefformance specifications. The units
were tested when operating within the load levels required by 40 CFR Part 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
2.4 CEMS Description
Information regarding the monitoring systems is presented in f able 2-2.
Table 2-2
CEMS Information
Teledyne Monitor Labs Model 150
Hunter Unit 3
Exhaust Stack
Thermo Fisher Model 410iQ
Thermo Fisher Model 43iQ
Thermo Fisher Model 42iQ
Thermo Fisher Model 48iQ
GP043AS-036892-RT- 1789 Page 10 of 195
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:
. Method Options:
o None
. Method Exceptions:
o None
. Target and/or Minimum Required Sample Duration: 5 minutes
The typical sampling system is detailed in Figure 3-1.
GP043AS-036892-RT- 1789 Page 11 of 195
Figure 3-1
EPA Method 2G Sampling Train
GP043AS-036892-RT- 1 789 Page 12 of 195
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 particulate 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:
. Method Options:
o None
. Method Exceptions:
o None
GP043AS-036892-RT- 1 789 Page 13 of 195
3.1.3 EPA Method 4
Determination of Moisture Content in Stack Gas
EPA Method 4 is a manual, non-isokinetic 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 series of pre-weighed impingers containing methodology-
specific liquids and silica gel immersed in an ice water bath. The impingers are weighed
after each run to determine the percent moisture.
Pertinent information regarding the performance of the method is presented below:
. Method Options:
o None
. Method Exceptions:
o None
The typical sampling system is detailed in Figure 3-2.
GP043AS-036892-RT- 1 789 Page 14 of 195
I
Figure 3-2
EPA Method 4 Sampling Train
SAA,PLE LINE
t
IN STACK FILTER
(ffitttlb)VACUUM.- uNE
BYfASS VALVEfi,4'+ VACUUI GAUGETHERilOCCUPLES I 1II
IiANOilETER +
GP043AS-036892-RT- 1 789 Page 15 of 195
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
(lnstrumental 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 pefformed across a grid of 12 points
determined using EPA Method 1 in accordance with 40 CFR Paft 60,
Appendix B, PS2 58.1.3.2 and 40 CFR Paft 75, Appendix A, $6.5.6.1.
Stratification testing is performed for two minutes per traverse point in
accordance with 40 CFR Part 75, Appendix A, $6.5.6.1(c). If diluent and
pollutant concentrations are within 5o/o of their mean concentrations,
subsequent gas RATA testing is peformed at a single point in the stack as
allowed by 40 CFR Part 60, Appendix B, PS2 58.1.3.2 and 40 CFR Part 75,
Appendix A 56.5.6.3(b). If diluent and pollutant concentrations are within
lOo/o of their mean concentrations, RATA testing is performed at three
points located 0.4 meter, 1.0 meterand 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, $6.5.6.1(a).
The typical sampling system is detailed in Figure 3-3.
GP043AS-036892-RT- 1 789 Page 16 of 195
Figure 3-3
EPA Methods 3A, 6C, 7E, and 1O Sampling Train
3.2 Process Test Methods
The test plan did not require that process samples be collected during this test program;
therefore, no process sample data are presented in this test repoft.
B.hrust
/ C.5.rim G8s
E$ault
Sr* /Cahralim Gas
'ttm'ioILttRSwrxfwcclEwE3
lltiorr*Ttiwth rt(rrrcoiltictn*
*l
r-:
HEATED
SAI'PLE
UNE
#l
gtFmwrs.
iOIXIIMTBfLffcdndwEs
GP043AS-036892-RT- 1 789 Page 17 of 195
4.O Test Discussion and Results
4.1 Field Test Deviations and Exceptions
No deviations or exceptions from the test plan or test methods were identified by the
project manager during this test program.
4.2 Presentation of Results
The average results are compared to the permit limits in Tables 1-2 through 1-4. Emissions
are reported in units consistent with those in the applicable performance specifications.
Additional information is included in the appendices as presented in the Table of Contents.
GP043AS-036892-RT- 1789 Page 18 of 195
5.O Internal QA/QC Activities
5.1 QA/QC Audits
The meter boxes and sampling trains used during sampling pefformed 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 34, 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 D7036-04 (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 peformed 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 7.2.1 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).
GP043AS-036892-RT- 1789 Page 19 of 195
Appendix A
Field Data and Calculations
GP043AS-036892-RT- 1789 Page 20 of 195
Appendix A.1
Sampling Locations
Page 21 of 195
PacifiCorp Hunter Power Plant Sampling Locations
Pollutant Stratification Test Points
DH
Stack Cross Section (A-A)
Unit123
Diameter (D) 322.6' 340.7" 307.4"
Upstream Distance (A) 199' 2A7' 218"
Downstream Distance (B) 269' 27O' 269"
Sample Point Distances from Stack Wall
Traverse Point 1
Traverse Point 2
Traverse Point 3
14.1" 14.8" 13.4"47.2" 49.9', 45.0'95.4" 100.8', 91.o',
Volumetric FIow Rate Sample Points
Unlt123
Diameter (D) 322.6" 340.7" 307.4"
Upstream Distance (A) 199' 207' 218"
Downstream Distance (B) 269' 270' 269"
Sample Point Distancos from Stack Wall
Traverse Point 1
Traverse Point 2
Traverse Point 3
Traverse Point 4
10.4" 11.0"33.8', 35.7"62.5" 66.0"104.3', 110.1',
9.9"
32.2"
59.6"
99.4',
+++ + + +++
t2 3 4 4 3 2 t
Stack Cross Section (A-A)
GP043AS-036892-RT- 1 789 Page 22 of 195
Appendix A.2
RATA Results
GP043AS-036892-RT- 1 789 Page 23 of 195
Appendix A.2.L
Unit 3
GP043AS-036892-RT- 1 789 Page 24 of 195
P.cmcorp
Huntei 3
Hith load Flow RATA
tl.lt9l2024
Peramater:Exheust Gas Flow (wsclhl wAF Applied?
RATA Results
No
Run f
1
2
3
4
5
6
7
8
9
10
11
L2
Start Tlme Stop Tlme Unlt Load RM
64,2L2,W
64,506,000
64,104,000
64,426,@O
64,679,OOO
64,392,00O
65,075,000
65,609,000
65,308,000
CEM
64,401,000
g,222,OOO
64,405,000
54,475,000
54,431,000
64,761,000
54,852,000
64,293,0@
64,006,0@
Dlfference U3e?-189,000 Yes284,000 Yes-301,000 Yes
-49,0m Yes
248,000 Yes-369,000 Yes223,000 Yes
1,316,m0 Yes
1,302,000 Yes
No
No
No
12:0O 12:05l2:O7 L2:12
12:14 12:19
72:28 12:33
12135 L2:4O12:42 12:4772:49 12:54
12:56 13:01
13:03 13:08
446
448
446
'148
447
M7
448
448
449
Number of Runs: 9
T-value 2.306
Standard Deviation 633,314
Confidence Coefficient 486,808
Relatave Accuracy (%RM) 1.18%
Bias Adjustment Factor 1.000
RAslO% (Semi-AnnuaU
AvGnge il,r0,.,222 aA27,ttt 271,89
GP043AS-036892-RT- 1 789 Page 25 of 195
PaclflCorp
Hunter 3
Mld Load Flow RATA
ttirgl2o24
Parameter:Erhrust Gas Flow (wscfhl WAF Applied? No
Runfl StartTlme StopTime Unltload RM cEM Dlfference Use? RATARBults
1 14:11 14;16 29A 48,494,000 49,547,0@ -1,053,000 Yes NumberofRuns: 9
2 14:18 14:23 298 49,514,000 49,789,000 -275,000 Yes T-value 2.305
3 14:25 14:30 301 49,259,000 49,435,000 -177,000 Yes Standard Deviation 740,826
4 14:58 15:03 298 49,465,000 49,987,0ff) -522,000 Yes Confidence Coetficient 559,1148
5 15:05 15:10 300 49,502,000 50,935,000 -1,433,000 Yes Relative Accurary (%RM) 3.57%
5 15:12 75:17 298 49,384,000 51,411,000 -2,027,000 Yes Bias Ad,ustment Factor 1.000
7 15:19 15:24 297 49,858,000 52,033,000 -2,t75,W Yes
8 15:25 15:31 297 51,072,000 52,727,@0 -1,655,000 Yes P75 Relativc Accurecy Standards
915:3315:383o15o,571,ooo52,1o5,ooo-l,534,oooYesffi
10 Yes RA<10% (Semi-Annual)
11 No
Average 299 49,579,89 501t5,556 -,.,20/5,6'
GP043AS-036892-RT- 1789 Page 26 of 195
PacifiCorp
Hunter 3
Low Load Flow RATA
ttl20l2024
Paramater:Erh.urt Gas Flow (wscrh)
Run fl
1
2
3
4
5
5
7
8
9
10
11
12
Stert nme Stop Time Unlt Load
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
10:17 10:37
10:52 11:12
11:26 11;46
LZ:OL 12:21
12:35 12:55
185
186
184
185
184
184
185
184
185
WAF Appllad?
RATA ResultsDifferance U*?
1,722,W Yes
1,436,000 Yes
2,179,000 Yes
1,421,000 Yes
1,550,000 Yes
1,258,000 Yes
1,641,000 Yes
L,748,OOO Yes
L2O7,W Yes
No
No
No
RM
41,075,000
39,805,000
39,848,000
39,158,000
39,217,000
38,877,000
38,998,000
38,895,000
39,336,000
CEM
39,353,00O
38,370,000
37,669,0m
37,747,OOO
37,557,000
37,619,000
37,357,000
37,747,@0
37,135,000
Number of Runs:
T-value
Standard Deviation
Conf idence Coeff icient
Relative Accuracy (%RM)
Bias Adjustment Factor
9
2.306
322,470
247,472
4.92%
1.045
Averate 39,t16,8,889 ,r,773,774 1,595,111
P75 Relatlv. Accuracy Standards
RA<7.5% (Annual)
RAs10% (Semi-Annual)
GP043AS-036892-RT- 1789 Page 27 of 195
Job Code PROJ-036892
PaciflCorp, Hunter Unlt 3
Test Datc: l,.l20l24
Parameter:cO2 (%vw)
Run #
1
2
3
4
5
6
7
8
9
10
11
72
13
14
15
Start Time
7:43
8:34
9:08
9:43
lQ:L7
10:52
11:25
12:01
12:35
End Time
8:20
8:54
9:28
10:03
10:37
11:12
11:46
17:27
12:55
Load
185
185
t84
185
184
184
185
184
185
RM
8.3
8.5
4.7
8.7
8.7
4.7
8.7
8.7
a.7
CEM
8.4
8.7
8.9
8.9
8.9
8.9
8.9
8.9
8.9
Difference
-0.1
-0.2
-o.2
-0.2
-0.2
-o.2
-0.2
-0.2
-0.2
Used?
x
x
x
x
x
x
x
x
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: ()2 / CO2 %
9
2.306
0.0
0.0
7.5%
nla
nla
n/a
Relative Accuracy Limit:
RA<7.5%ot tO.7%
Average 185 8.6 8.8 -0.2
Parameter:NOx (lb/mmBtu)
Run fi
I
2
3
4
5
6
7
8
9
10
11
72
13
14
15
Start Time End Time
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
lO:17 10:37
10:52 !l:L2
11:26 11:46
12:01 L2:21
12:35 12:55
Load
185
185
184
18s
184
184
185
184
185
RM
0.231
0.219
0.210
0.211
0.209
0.210
0.209
0.209
0.210
CEM
0.238
o.223
0.215
0.215
0.213
0.214
0.214
0.274
o.274
Difference
-0.007
-0.004
-0.005
-0.004
-0.004
-0.004
-0.005
-0.005
-0.004
Used?
x
x
x
x
x
x
x
x
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
0.001
0.001
7.6%
nla
n/a
1.000
Relative Accuracy Limit:
RAs7.5% or 10.015 lb/mmBtu
Average 185 0.213 0.218 -0.005
Parameter:SO2 (ppmvw)
Run fl
1
2
3
4
5
6
7
8
9
10
11
L2
13
L4
15
Start Tlme End Tlme
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
LO:17 10:37
10:52 11:12
lL:26 11:46
12:01 12:2!
L2:35 12:55
Load
185
186
184
185
184
184
185
184
185
RM
2t.4
22.4
23.8
24.4
24.4
24.L
22.9
25.9
24.4
CEM
23.4
24.3
25.7
25.8
25.8
25.5
24.5
27.3
25.8
Dlfference
-2.0
-1.9
-1.9
-t.4
-L.4
-1.4
-1.5
-1.4
-1.4
Used?
x
x
x
x
x
x
x
x
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: SO2 / Nox ppm
9
2.306
0.3
0.2
7.5%
n/a
n/a
1.000
Relative Accuracy Limit:
RA<7.5% or t12.0ppm
Averate
GP043AS-036892-RT- 1 789
185 21.7 25.3 -1.6
Page 28 of 195
Job Code PROJ-036892
PacifiCorp, Hunter Unit 3
Test Date: lt l20l24
Parameter:NOx (ppmvwl
Run fl
1
2
3
4
5
6
7
8
9
10
11
L2
13
74
15
Start Time End Time
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
7O:77 10:37
10:52 17:72
L7:26 11:46
12:01 12:27
12:35 12:55
Load
185
186
184
185
184
t84
185
184
185
RM
88.9
85.2
84.8
84.9
84.4
84.7
84.3
84.2
84.5
CEM
93.3
90.5
88.7
88.7
88.3
88.7
88.3
88.3
88.5
Difference Used?
-4.4 x
-4.3 x
-3.9 x-3.8 x
-3.9 x
-4.0 x
-4.0 x
-4.7 x
-3.9 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Conf idence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P50, PS2: SO2 / NOx ppm
9
2.306
o.2
o.2
4.9%
nla
n/a
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 185 85.2 89.3 -4.0
Parameter:SO2 (lblmmBtu)
Run S
1
2
3
4
5
6
7
8
9
10
11
72
13
t4
15
Start Time End Time
7'.43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
lO:17 10:37
10:52 1L:L2
ll:26 11:45
12:01 t2:2L
12:35 12:55
Load
185
186
184
18s
184
184
18s
ta4
185
RM
o.o77
0.079
0.082
0.084
0.084
0.083
o.o79
0.089
0.084
CEM
0.083
0.083
0.086
0.087
0.087
0.086
0.083
0.092
0.087
Difference Used?
-0.006 x
-0.004 x
-0.004 x
-0.003 x
-0.003 x-0.003 x
-0.0&l x
-0.003 x
-0.003 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adiustment Factor
P5O, PSz: SO2 / NOx ppm
9
2.305
0.001
0.001
5.4%
n/a
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 185 0.082 0.086 -0.m4
GP043AS-036892-RT- 1 789 Page 29 of 195
Job Code PROJ-036892
PacifiCorp, Hunter Unit 3
Test Date: lll20l24
Parameter:so2 (lb/hr)
Run fl
1
2
3
4
5
6
7
8
9
10
11
t2
13
t4
15
Start Time End Time
7:4! 8:20
8:34 8:54
9:08 9:28
9:43 10:03
7O:L7 lO:37
70:52 1l:12
Ll:26 1l:46
l2:Ol l2:2L
12:35 12:55
Load
185
185
184
185
184
184
185
L84
185
RM
145.9
148.2
157.5
158.9
159.4
15s.8
t48.2
157.5
159.6
CEM
153.1
155.1
150.9
151.5
161.0
159.1
151.8
168.3
159.2
Difference
-7.2
-5.9
-3.4
-2.6
-1.5
-3.3
-3.6
-0.8
0.4
Used?
x
x
x
x
x
x
x
x
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
2.5
2.0
3.3%
^/an/a
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 185 1SS.7 158.9 -?.2
Parameter:NOx llb/hr)
Run f
1
2
3
4
5
6
7
8
9
10
11
72
13
L4
15
Start Time End Time
7:43 8:20
8:34 8:54
9:O8 9:78
9:43 10:03
10:17 lO:37
10:52 ll:t2
ll:26 11:45
12:01 77:2L
12:35 12:55
Load
185
185
L84
r85
184
184
185
184
185
RM
435.8
409.9
403.3
397.0
395.1
393.1
392.6
391.3
397.5
CEM
438.3
4L4.6
399.1
399.8
395.6
398.2
393.8
391.5
392.4
Difference
-2.5
-4.7
4.2
-2.8
-0.5
-5.1
-t.?
-0.3
5.1
Used?
x
x
x
x
x
x
x
x
x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P5O PS6: Mass Emissions
9
2.306
3.6
2.7
os%
nla
nla
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 185 40L.7 4IJ2.6 -0.9
GP043AS-036892-RT- 1 789 Page 30 of 195
Job Code PROJ-036892
PaciflCorp, Hunter Unit 3
Test Date: LLl2Ol24
Parameter:CO (ppmwl
Run fl
1
2
3
4
5
5
7
8
9
10
11
72
13
74
15
Start Time End Time
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
10:17 LO:37
10:52 17:12
11:26 11:45
72:OL 72:21
12:35 12:55
Load
185
186
184
185
184
184
185
184
185
RM
3.9
6.6
7.9
7.3
7.1
7.0
7.0
5.6
5.1
CEM
L3.2
L4.2
t7.3
15.6
15.5
15.6
15.7
15.3
15.5
Difference
-9.3
-7.6
-9.4
-8.3
-8.5
-8.6
-4.7
-4.7
-9.4
used?
x
x
x
x
x
x
x
x
x
RATA Results
Number of Runs: 9
T-value
Standard Deviation
Conf idence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6Q PS4A: CO ppm <200
2.306
0.6
0.5
138.8%
838
t.L%
n/a
Relative Accuracy Limit:
10% RM or 5%EL or I d | +CC<Sppm
Average 185 6.6 15.3 -8.7
Parameter:CO (lb/mmBtul
Run fl
1
2
3
4
5
6
7
8
9
10
11
!2
13
t4
15
Start Time End Time
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
lO:17 10:37
10:52 11:12
ll:26 1l:45
12:01 12:21
12:35 12:55
Load
185
186
184
185
184
t84
185
184
185
RM
0.006
0.010
0.o]-z
0.011
0.011
0.011
0.011
0.010
0.009
CEM
0.021
o.o2L
0.02s
0.023
0.023
0.023
0.023
0.023
0.023
Difference
-0.015
-0.011
-0.013
-0.012
-0.012
-0.012
-0.012
-0.013
-0.014
Used?
x
x
x
x
x
x
x
x
x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adiustment Factor
P6O, PS6: Mass Emissions
9
2.306
0.001
0.o01
L34.6%
o.2
6.8Yo
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 185 0.010 0.023 -0.o13
Parameter:co (tb/hrl
Run #
I
2
3
4
5
6
7
8
9
10
11
72
13
!4
15
Start Tlme End Time
7:43 8:20
8:34 8:54
9:08 9:28
9:43 10:03
10:17 10:37
10:52 Ll:!2
lL:25 lL:46
12:01 L2:2t
12:35 12:55
Load
185
185
184
185
184
184
185
184
185
RM
11.5
19.1
22.9
20.8
20.1
19.9
19.9
18.7
77.3
CEM
37.8
39.6
47.0
43.0
42.6
42.8
42.7
4t.4
42.2
Dlfference
-25.2
-20.5
-24.1
-22.2
-22.5
-22.9
-22.8
-22.7
-24.9
Used?
x
x
x
x
x
x
x
x
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 Emlssions
9
2.305
7.7
1.3
129.3%
2406
L.O%
nla
Relative Accuracy Limit:
2O% RM or 10%EL
Average 18.9
GP043AS-036892-RT- 1 789
185 -2?.2
Page 31 of 195
Appendix A.3
Field Data
Appendix A,3.1
Unit 3
GP043AS-036892-RT- 1 789 Page 33 of 195
Appendix A.3.1.1
High-Load Flow Data
Clicnt PaclflCorp
Unit lD Hunter 3
Load Hlgh
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H20)
02 (%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
Pn Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ('R)
Vm(rto Volume of Water Condensed (scf)
VmGtd) Sample Gas Volume (dscfl
Stack Gas Temperature ('C)
B** SaturatedMoistureContent(%/1ml
B* Measured Moisture content (%/100)
B*, stack Gas Moisture Content (%/10o)
24.47 24.47 24.47
-5.50 -5.50 -5.50
7.5 7.s 7.5
12 L2 12
24.47 24.47 24.47
-5.S0 -5.50 -5.50
24,47 24.47 24.47
-5.50 -5.50 -5.50
7.5 7.5 7.s
12 72 L2
7L,2 71.2 77.2
25.944 26.944 26.9M
0.997 0.997 0.997
L.7 L.7 t.7
58 58 58
24.60 24.60 24.60
518 s18 518
3.35 3.35 3.35
22.sO 22.s0 22.50
45.1 45.2 45.1
0.118 0.119 0.118
0.130 0.130 0.130
0.118 0.119 0.118
(s.rur.!!d) (gru,.tcdl {S.tur.ted)
83.8 83.8
33.595 33.596
0.997 0.997
7.7 L.7
55 56
24.60 24.60
516 515
3.94 3.94
28.25 28.25
44.9 45.2
o.Lt7 0.119
0.123 0.123
o.Lt7 0.119
(s.turated) (saturatedl
7.5
t2
83.8 7t.2
33.696 26.9M
0.997 0,997
L.7 L.7
56 58
24.60 24.60
516 518
3.94 3.35
78.75 22.50
45.0 45.0
0.118 0.118
0.123 0.130
0.118 0.118
(s.tur.tedl (S.tur.tedl
7.5 7.5
L2 L2
71.2 7t.2
26.944 26.944
0.997 0.997
7.7 L.7
58 58
24.60 24.60
518 518
3.35 3.3s
22.50 22,50
4s.2 45.1
0.119 0.118
0.130 0.130
0.119 0.118
{s.tu,at.dl lsatur.tedl
GP043AS-036892-RT- 1 789 Page 35 of 195
High toad Run fl
l@tlon: Huntar I
tod (MW): t!r6
D.E: L7|L9/1O24
SEd Tlh.: t2fl
End Tlmr:
Probe / Gas Data
Unadiusted Results
ft/rc
Qsw: Q,2I2,O2O w*llhr
Adlusted Results
Va(avtl: 46.21 ltlsccqswi 63,569,900 wr<t/hr
56,133,323 ds<r/hr
Prcbc {1 R@: 0 d.tE
Proba 12 Re: 0 daares
Probc 11 R$o: -0J d.tr.c.
Fhbc 12 Rsro: -1, d.!e.
8.,: o.Uro talroo
Md: 30,22 lb/b-.hol.
M,: 2E.79 lb/lb.m6l,.
P*: 2a.1, ln Ha
P.: -5.50 ln HrO
P,: 2a,0, ln Ba
t(COr: 12.0 t6
"4Oi 7SX
,a<Ot O.O *
80.5 t6
Flow RATA Traverse Data
Polnt lO P6bc lD
Corrcctad
StectT.mp Y.wAndc Y.wAntlc PI-PI
lFl ldcrl o- (del lln H.ol
Un.dlustcd Rcpl.c.mcnt Polnt U*d I wAF
Ari.l VGlBtty khl Vcloclty lor Point
v- attlec) v- {ft/sl wAF? us.dL
001 1o -8 7.9 0.44 0.E09 n1 116
002 10 E 7.9 0.s6 0.8090 17.321
m3 I -il 1q o.61 o.aBo 48.923 nla
oo4 2 {oil oaM so.1s6
005 10 -5 4.9 0.49 0.8090 4l.7SI
006 10 4 -3.9 0.60 0.8090 44.478
007 4 3.9 o.52 o.am i19.323
008 I 4 3.9 0.64 0.8090 50.112
@9 115 4 2.2 0.37 0.8380 39.669
010 115 -4 -2.7 0.,1,1 0.8380 43.259
011 115 -s -3.2 0.54 o a3to 47.444
o12 115 -5 4.2 0.50 0.83E0 50.417
o13 115 7 -5.2 o.38 0.83t0 40.066 nla nla
o14 115 -5 47 o.53 o.a380 47 sas
o15 115 -3 L,2 0.55 o a3m 4.3S
016 115 4 2.2 0.@ 0.8380 50.516
InaB 112.r -s.0 4.1 0.S4 0.8235 6.679 nl. nlz
GP043AS-036892-RT- 1789 Page 36 of 195
High Load Run #2
lootion: Huntar 3
lod (Mw): 444
D.E: LLlL9l2O24
St.rtTim.: l2to7
End Tlm.: 12t12
Probe / Gas Data
Probr Il R@: 0 da3a4a
Prcbc 12 R6: 0 d.trcc.
P,ob. ll Rro: -Ol d.ara.
Prob. 12 Rao: -1.t d.tr.G.
a-, ------;;;tr6lroo
Mr: 30.22 lb/lb-molc
Mr: 2t.rl lb/lEdolc
Pb,: 24.,17 In Ht
Pr: -S.5o ln Hro
P.: 24.07 ln Ht
'{,CO2I l2.O 96
rcrt ,.5 X
%CO: 0.0 9a
80.5 X
Flow RATA Traverse Data
Point lD Ptobe lD
Corractcd
StckTcmp Yaw^ni. YewAn3lc Pt-P2
lFl (drt) (L ldcr) (ln H,ol
Un.dru.t.d Rcpl.emni Polnl u*d I wAF
Arl.l V.l*lty Arlal VGlo.ltV for Poln6
V. (fV*.) v. (ft/c) wAF? usdq
001 1 -9 -8.9 0.44 0.809
002 I -6.9 o.s6 o.8090 46.702
m3 2 -5 .4.9 0.64 o8m 50.107
004 72 -4 3.9 o.65 0.8090 50.s64
005 I ,6.9 o.4s 0.8090 41.828
m6 2 -6 ,5.9 o.s6 o_m90 46.793
M7 2 -5 -4.9 o.63 0.4090 49.7L4
008 I -5 {.9 0.54 0.8090 s0.063
00!)15 4 .2.2 o.37 o.4380 39.5E3
010 5 7 o.5s 0.4380 48.219
011 15 7 -5.2 0.57 0.8380 49.0E8
012 15 -3.2 o.51 o.4380 50.911
01l 15 -5 1.2 0.35 0.8380 ta se
014 15 -5 l.z 0.52 0.8380 47.006
015 15 -5 -n2 os8 0.8380 49.587
o15 5 4 2.2 0.61 o g?ao 50_953
113.3 -5.7 -4.7 0.55 0.8235 t16.9:t4 nh nl.
GP043AS-036892-RT- 1 789 Page 37 of 195
High toad Run fl3
lqllo: Huntar 3
tod(Mwl: w
D.E: tllL9l2o24
Start Tlm.: 12:14
End Tlre: 12:19
Probe / Gas Data
Unadiusted Results
iavgl: 46.62trtscc
Qsw: 64,1O4,125 wsc/hr
Prcbc 11 R@: 0 dct E.
Ptobc 12 Re: 0 d.t.es
Probc ll Rao: .Ol d.&.er
Prob.l2 &Lo: -13 de!c.
I,a,: o.tlrt taltm
Md: 30.22 lb^Emolc
Mr: 2t.7t lb/lb,mol.
Pe: 24.{, ln H!
P.: -5.5O ln HrO
P,: 24.07 lh Ha
t{COr: 12O ta
.t1ort _L!Y.taCO: OO '.XN,: to.s f
Adjusted Results
Va(awl: 46.15 ltl*c
Qsw: 63,463,0t4 wrcf/hr
Qsd: 95,985,794 d*tlht
Flow RATA Traverse Data
Polnr lo P@br lO
Coractad
SiaclTrmp Y.w^ntla Y.wAn3l.
lFl ld.d (Lld.rl
PI-P2
lln H,ol
Un.dlun.d R.plemnt Polnt U$d * wAF
Arlrl Vcloclty Arl.l V.lo.lw lor Polnt3
v.lftle.l v- Ift/Gl WAF? Ur.dc
m1 -a -7.9 o_45 om 41_147
oo2 1 -5 4.9 0.56 0.8090 46,82r
003 2 -7 -5.9 o.6t 0.8090 48.733
004 2 4 -3.9 0.63 0.8090 19.771
mq to -7 -69 o.45 oam a72 S
006 I s -4.9 o.57 0.8090 47.237
007 I -4 ,3.9 0.63 0.8090 49.724
008 111 4 -3.9 o.62 o.ao90 49.312
009 15 -5 3.2 o.36 0.8380 39.104
010 15 -5 3.2 0.47 0.8380 44.68r
011 1S -7 -5.2 0.58 0.E3ao 49.507
o12 1S -4 -2.2 o_62 o.8380 s1.360
013 15 7 -5.2 0.37 0.83E0 39.142 nla
014 15 ,5 4.2 0.51 0.83t0 46.491
o15 115 -5 -3_2 o.s6 o.8380 44.771 nla
016 15 -5 4.2 om 0.8380 50 426
lrcntes 113,1 -5.6 -4.5 0.54 0.E235 46.627 nl. nla
GP043AS-036892-RT- 1 789 Page 38 of 195
Hith toad Run #4
lqtlon: HuntGr 3
ted (Mw): a48
Dd.: 1r,lL9l2024
Sbn Tlm.: l2t2t
End Tlm.: 12:31
Probe / Gas Data
Adjusted Results
avg): 46.39 ft/scc
qswi 53,782,057 wct/hr
Probc {1 Rm: 0 d.tter
Probc 12 R@: 0 d.tr.ca
Prob€ tl R.@: -Ol dctraet
Prcb. 12 Rqo: -t.6 drtrer
8..r 0.u78 X/tq)
Mdi 30.22 lb/lEmolc
M,: 2t.r8 lb/lb-molc
Pb,:-llglnH3
P.: -5.50 ln Hro
P.: 24.0, ln Ht
co2t 12.O )a
'fir'
-l:!'t
xCO: 0,0 9{
e).5 x
Flow RATA Traverse Data
Polni lD P@b. lD
Corredcd
StekT.mp Y.wAnd. Y.wAnah Pl-P2
Itl (.tct) O- (d.d (ln H,ol
Unadlu.t d Rcpl.cmcnt Polnt UEd t WAf
Arl.l V.leity tui.l Vcloclty for Polnts
v.(rtlE.) %(ft/sl wAF? uEdc.
ml 10 -10 -9.9 o.45 om 11.467
002 1 -5 -5.9 0.57 o.8090 47.159
003 1 -5 59 o.53 o.8m i!9.579
m4 2 4 t.9 0.63 o.8mo 19.111
005 10 -5 .4.9 0.44 0.8(}90 41.456
006 1 -4 -3.9 o.s9 0.8090 48.123
007 2 3 2.9 0.51 o.8m 49.026
oo8 2 4 3.9 0.62 0.E090 49.!75
00!)15 -4 .2.2 0.39 0.8380 40.734
010 15 -5 4.2 0.55 0.8380 14.279
o11 15 3 1.2 o.s8 0.8380 {9 701
012 15 7 .5.2 0.55 0.8380 52.410
013 15 -4 o35 0.8380 38.589 nla nla
ol4 5 3 1.2 0.39 0.E3E0 40.755
015 1S -5 4.7 0.61 0.8380 50.845
015 15 7 o65 0.8380 52.410
lvetattt 113.r -5.1 42 0.54 o-423s 45.455 nlz nl"
GP043AS-036892-RT- 1 789 Page 39 of 195
High toad Run f5
Leation: Huhter 3
Ldd (Mwlr ul
D.t.: L,.ll9l2024
Sbrt Tlm!: 12:35
€nd Tlm.: 12:40
Probe / Gas Data
Probr 11 R.m:
ruc12Re:
Probc tl R.D:
Prob. 12 Rao:
0 datrC.t
0 d.trat
{r.,' d.tr@!
-1.8 d.tlB
8,.: 01187 t 10o
Md: 3022 lb/lEmolc
M,: 2t.77 lb/lL6ol.
Pb: 2il.il7 ln Ht
Pr: -5.50 ln Hro
P.: 24.0, ln Ht
XCOri 12,0 f
"aort _!2rt6CO: 0.0 ta
tt .s t6
Flow RATA Traverse Data
Polnt lD Prob. lD
Correcaad
St.cl Thp Y.w Arlt|. Y.w Antlc P1-P2
lFl ld..l o-. lddl lln H-ol
Un.drudcd Rcpl.@runt Polrt Urd t WAF
Arl.1 Vclclty A{.1 VGI*ity lot PolnB
v-tft/{.| v-lh/..c1 wAF? UsldC
001 11 -9 -8.9 o.47 0.809 42.540
m2 t2 7 .6.9 0.s6 o_8090 46.702 ale nla
mt )5 {.q o63 oam n9 71n
004 2 0.63 0.8090 49.714
@5 -5 -5.9 o.17 0.8090 41.8r1
m5 4 3.9 0.57 o.8090 47.309 nla
007 2 Jg 0.63 0.8090 49.111
008 2 3 2.9 0.64 0.8090 50.226
oo9 115 4 2.2 0.43 0.8380 42.740
o10 1 11S -4 -2.7 0.56 0.8380 48.820 nla
011 5 5 3.2 0.61 0.8380 50.911
012 5 7 -5.2 0.60 0.8380 so.363
013 4 -2.2 0.16 0.8380 39.143 nla
014 1g -{-72 o39 o a1m 40.742
015 5 4 2.2 0.61 0.8380 50.953
016 15 5 ,.2 0.60 0.8380 50.492
lveratas 113.3 -5.1 -4.1 0.55 0.t235 47.060 ala nla
GP043AS-036892-RT- 1 789 Page 40 of 195
Hith Load Run #6
Loatlon: Hular 3
lo.d (Mwl: 141
D.tc: lllL9l2024
St.nllm!: l2,az
E?dTlm.: 12t17
Probe / Gas Data
Prcbe 11 Re: O d.rre3
Proha 12 RD: O datrer
Probctl R{o: {J d.tres
Prob. f2 Rsto: -r-8 d.aruGt
B-: 01t82 tallq,
Ma: 30.22 lb/b-molc
M.: 28.rt lblb-moh
Pb,: 24.4, ln il3
P.l -5.5o ln HrO
P,: 24.0, ln Ht
t{CO,: 12.0 X
'tor.-LLxtaCO: 0.0 t6
60.5 r
Flow RATA Traverse Data
Polnt lO Prcbr lD
Cotrdcd
sta.lT.mp Y.wAntlc Y.wAndG PL-PI
lcl ldpl d ldEl lln H-Ol
Un.drurtcd R.pLqmnt Polnt u3.d I WAF
Axl.l VGloclty Axl.l Vcloclty lot Polntr
v- aft,lql V- lftlcl W F? UsGdL
m1 1 I -8 .7.9 0.46 0.809 42.190 nla
002 1 -7 ,6.9 o.57 o_4o90 47.O71 lle
003 t I '6 .5.9 oa oam a9_976
M 1 12 .4 .3.9 o.63 0.8090 49.776 nla
m5 I .6 -5.9 o.45 o.8o:x)41.906
006 I t {-3S osa o.8G)O a1.1ta
007 1 tL2 4 ,3.9 0.62 0.6090 49.379 nla
@8 112 .5 {.9 o.55 0.togo 50.'192
009 2 115 -6 -4.2 o_44 0.8380 43.186
010 2 115 7 -s.2 0.54 0.8380 47.774
011 115 .5 -3.2 o.50 0.8380 50.488 nla
012 2 115 -1.2 o.63 0.838n S1.8oil nle
013 2 115 -0.2 0.34 0.8380 38.065 nla nla
014 11S -3 -1.2 o.35 0.8380 34.512 nla nla
015 2 115 {-77 o60 o.a3a0 50_529
016 2 115 -5 -3.2 o.@ 0.8380 50.444 nle
113.2 -4.9 -4.0 0.54 0,E235 45.E41 nla nla
cP043AS-036892-RT- 1 789 Page 41 of 195
High toad Run #7
Loetlon: Hunter 3
Lo.d (MW): tr4t
D.tc: L7ll9l2024
Start Tlme: 12:49
End Tlm.: 12:54
Probe / Gas Data
Adjusted Results
Va(avg): 46.85 ft/rcc
Qsw: 64,424,716 *scllht
Qsd:
Prob! 11 RM: 0 dcarc.t
Prob. 12 Re: 0 da3r43
Probc rl Rao: -ol dcarc..
Probc 12 Rsrc: -13 d.tr.Gt
8..: o.11t2 t{100
Md: 30,22 lb/lb-molc
M,: 26.7t lb/lEmoL
Pb,: 24.4, ln Xt
P.: -5.50 in Hro
P,: 24.0, ln Ht
t{COr: 12.o X&,'----------11*
XCot 0.0 t(
e).5 x
FIow RATA Traverse Data
Polni lD Plobc lD
Condcd
StaclTamp YawAndc Y.uAntlc
lFl ld..l C lddl
?L.P2
lin H,ol
un.dluttcd Rcpl&rent Polrt usd t wAF
Arlal v.loclty Arl.l V.lo.lty lor Polnls
v. (ttlml V. (fr/cl WAF? usdc.
001 -8 7.9 0.45 o.809 41_719
m2 -8 t.9 0.58 0.8090 t7 175
ml 2 -6 -5.9 0.62 0.8090 19.232
004 s "4.9 o.53 0.8090 49.709
@5 5 {.9 0.47 o amo 42.898
ffi 5 {.9 0.58 0.8090 47.654
oo7 -6 -5.9 0.62 0.8090 49.189
fi)8 2 4 3.9 0.65 o.aoln 50.560
009 5 4 2.2 0.39 0.8380 40.738
o10 15 -3.2 o.57 0.8380 49.209
011 l5 {2.1 o.60 0.E380 50.529
012 t5 -6 -4.2 o.55 0 a3ao 52.490
013 15 8 -6.2 0.37 0.8380 39.477
014 l5 7 -s_7 o.s1 0.8380 46.41A
015 l5 -3 o57 o.a3m 49.275
015 115 -5 3.2 0.6t 0.8380 50_s7
Etatcs 113.2 -5.6 -4.6 0.5S 0.8235 47.337 nla nla
GP043AS-036892-RT- 1789 Page 42 of 195
Prob. rl R@:
Prob.12 R@:
Piobc 11 &E:
Probc 12 Rao:
0 drtrea
0 degrccr
-O.l dalrae3
-1,t d.!Gt
8..: o.Utg ral100
Md: 30.22 lb/lb-mol.
M.: 2t, lblFmolc
Pb: 2a.iu In Ht
P.: -5.50 in HrO
P; 2aA I,Bt
t{coi: l2O X
.t(or, _!!X,.cO. 0.0 X
8{r.5 r
High toad Run #8
Loetlon: Huntc. ,
Lo.d (Mwl: 4$
o.te: L,.llg/loz4
St 'lllm.: 12:56
End nm!: 13:01
Probe / Gas Data
Adiusted Results
Va(avgf: 47.26 ttttx
Qsw: 64,953,1EE wcflhr
Qsd:
Flow RATA Traverse Data
Polnl lD Prob. lD
CorrGCtGd
StackT.mp Y.wArSlc Y.wAntlG Pl-P2
(rl ldc.l (L ldd) lln H,ol
un.dlunGd Rcpl.c.m.nt Polnl Usd f wAF
Arhl Vclctty Arhl V.ldity io. PolnG
v.(fv.ecl V.(ft/*cl waF? ustdc-
001 -9 .8.9 0.17 0.809 42.542
m2 112 9 .ag o.56 o.8Glo 45.474
m1 112 -5 -4.9 0.61 0.8090 48.920
004 112 -4 -3.9 o.62 0.8GX)49.386
005 111 -59 o.45 0.8090 41.830
m5 112 -6 -5.9 0.57 0.8090 47.211
007 172 4 ,3.9 0.62 0.8090 il9.386
008 t12 -5 {.9 0.53 0.8090 49.716
m 115 2 4.2 0.45 o.4380 ir4.281 nla
010 r15 1 0.8 0.57 0.8380 49.2m
011 t15 .4 .2.2 0.63 0.8380 51.7E4
o12 115 3 I o65 o.a3m s2.617 nla
013 115 7 -5.2 0.44 0.83E0 43.130 ^la014115"6 4.7 o.53 0.8380 41.404
015 115 7 osa o a3m 49.S19
016 115 ?-s.2 o.60 0.8380 50.365
,.13-4 -5.4 {.4 0.55 0.8235 47,742 ^1. ila
GP043AS-036892-RT- 1 789 Page 43 of 195
High toad Run lr9
l@tid: Huntar 3
t@d (MW): ia49
D.t : ,llL9l2o24
Stanllm.: 13:03
End nre:
Probe / Gas Data
l3:Ot
Adjusted Results
Va(avgl: 47.O? ttlsc<qsw: 64,654,55E wrl/hr
: 57,qr9,657 dscilh.s7
Probc *r. Re: 0 dctr...
Prob.l2 RM: 0 d.t@.
Prob. 11 Rao: fl dqras
Probe fl2 Rsro: -l-8 dclrear
8,.: 0.1182 tUloo
Md: 30.22 lbflb"holt
M,: 28.78 lbflb-moh
Pb,: 24.4, itr Hg
P.: -5.5O io Hro
P,: 2i1.07 ln Ht
'*cozi l2.O X
'(Ort , S ,a
rco: 0.0 ,6
to.s ta
Flow RATA Traverse Data
Poinr lD Probc lD
corrad.d
St.ctTCmp Y.wAnllc Y.rAntl.
lFl ld.rl o. ldEl
Pt-?2
aln H.ol
Un.dlurt d Repl.@.nt Polnt Ued , WAf
Axl.l Valelty Arl.l Vclelty lo. Polntt
v-ltt-/re.l v-lft/s.cl wAf? uedC
00r 111 .9 -8.9 0.45 0.809 47 677
002 111 '7 -6.9 o.56 0.8090 46.557
m3 112 6 -s.9 o.62 0.8090 49.232
004 -3 -)9 o.52 o_amo 49.430
005 lll -7.9 o.47 0.8090 17 546
005 1lt -4 .3.9 0.58 0.8090 47.7$
m7 111 .5 .4_9 o.61 0.809,0 44.471
008 112 .3 .2.9 0.63 o 80qo 49_A27
009 11s .3 -1.2 o.44 0.8380 43.293
010 11s -2.2 0.53 0.8380 47.490
01t 115 {.2.2 o.64 0.8380 52.1E5
012 115 .6 4,2 o.u 0.8380 52 045
013 115 .1 .5.2 0.45 0.83E0 43.612 nla
o14 115 -7 .s.7 o.51 0.8380 46.424
015 .7 -52 os6 o.83m 4_551
016 115 .,0.50 0.8380 50.358
\waacs 113.2 -5.6 4,7 0.55 0.823s 47.507 nle nla
cP043AS-036892-RT- 1789 Page 44 of 195
o3 b {q?
,tolectGode c-+fi<r Lt Lrurttetrlc lhcssurr l.llrl :2,L1.9 -t UmOhnt?r,r- ,* t, ta.,?itrdc Prcssuru ("HrOl:-6 5 &rSoutta:H c,nlr j
Att / LL
Probc lD/Alhnment 155 / b./ProbcColrdtdon ,/tz.?opcrlbr[s]:lO Cqrsole lD:P 3D-t cor lrl)ats;lq - ZLt helChcdr('HrOl:Ilr)7,s
lit' ,
EPA lUlethod 2F "Fast Ftow', Datasheet
. fi ;5 r,, Lo".,)
lun I ilenTfnc:.4 l2co i-tpTlme:lacsInucrrc Polnt
iPort-Polntl
SactTcml
fFt
YewArgtc
t Dar
vdodyaPfHrOl
(P1-P2l
PldrapfHpl
(P4451
Commcnts:
-l tb -cl o. Ll Ll-2 llo *t o.rc6-3 _t{o e t-4,l,a-'^Ll C ('ta-lto -5 O LICI-f I lct _11 o 60-3 ll t -9 o (.e_.f ill _L,o,6 Ll
lun I Strrt T[nc:I ).,O I ItopTbnc:ta,2
Commcnts:,oft
StsdrTcml
rn
YawAr6ls
tDct
V:lodtyAP ('H:Ol
(Pr+21
PhctraPf}l1ol
lP0+stItt0.Ltcl-J,,, a.-7 o. s63t,L -t O. 6tt-q ta -(-l O CS
<:( -,--1 o.,Ll5-a la -6 o163,rl -5 O,6,1 ill --5 0.bLl
GP043AS-036892-RT-1789 Reviewed: FPM_face_4SBM gs
,rolectGode o Stn qr{z latmrctrlc Prrcruru l'l{rl:2'+ . '+
-t RroEthrrhr,*itorP ltsde Prcsrut ('HrOl:- 5.c,Rroloura:r a, l-lnatC/ProbG lD /Alhnrncnt rl_l Probc CmdltbnOpcretor{sl:A1 lDGonsolc tD:lvtA-)6 cor lrgl).tr:lllqtT+LetChcdr(.HrOl:q 0.1
EPA lUethod 2F "Fast Flow'. Datasheet
lml I ItertTlnc:r:-O O ibplmq:LOA
hancr:c Polnt
lPort-Fdrtl
SleckTrmg
r+l
YrwArgh
t Dc!
ValodtyAPl'ltpl
(Pr+21
PkhaPrHlol
lEr.DEt
Eommcnts:
Ll il5 -u . _<Jzt \q;, rJJ-{
7 r15 -ci ,5q{lr5 -(,,(,j t ttb -'t \
2 I r5 -o .57tlL5-a 5a{tlo -q t laf\
lun I 2-TETITTmG:L O-t ibpltnc:,-lL
Port
SreclTamp
(T)
YruA4la
t Ocr
VclofiyAP l-ltz0l
lPr+z)
P|tdTAP('HrOl
lFa+st
Gomrnqnts
-)ll6 -7t 5
2 lt6 -l lF-t
3 t15 -l 51LI15-5 ,I_[l16 -r)?5 \
2 tt6 -5 , C't'l \-)lt?-(,,69
7-L{t16 -q (,I
ilun I 5 It lt llmc:t+tE-tzlr'l ftopftnc:%*te+- tZ rq
Fort
StectTcml
frt
Yrwlngls
t Dct
vclodtyaP fHlol
(P1+2t
PtEhaPl,ttol
l9r.DRl
Eommcntr:
a t\5 -6 . i(o
z I\D -v)u-1
1 tt6 --1 5B.i t\6 .-+. fo)-\!t it6 .--I 7
2 r\6 -o 5r
?t16 -,,5G
5 ll€)-b n0
GP043AS-036892-RT- 1 789 Reviewed: FPM page 4rmr95
EPA Method 2F "Fast Ftow. Datasheet
H,.sh L",qc)
Gb<l 2
,rolccl Code o4+r4f-- Ar Bercmctdc Pr:sruru l,ltl:-ar t j U!,rlctlr P".c.C; C", n ldcPnsglru l'1l.Ol:-5 s lroSourtr:lJ ,., 'l _z hobG lD / AlLrrnGnC l3s 1 ,-Probe C.ondldor l/Opcnbdrt:l( /r L lD C.onrole lD:3P-
'
corfil lz, oh:,r- rq-.1q Iaek Chcct (']lrOl:D, (xl 7.5
tun t Ll ttrttTlnc:t)a.r ftopInc:,t ? <
CommrnE:Iranrrc Fohrt
lPorf,Poml
StactTcml
rn
YewArrfh
t Der
VclodtyAP l'HrOl
lPr-P:il
Plrdr.PrHpl
- (F+Pslut-xt- ? ,-l I tc;-to 0+4q o,o.'l 5- -).ltt -C (\, s7-3 Ut 6 e 3.-ti tf.'-1 oe3a-,lo -s Dl -l-f.Itt -t,O. !r dl \-3 rI -3 o,(. I'cl lr f.-Ll oc e
tmt q ileilfhnc:I ar5 ttopllm:la,.l0_
Port
StectTcml
(Tl
YewAqlo
i DGE
ValocftyaPfHpf
(P1-P2l
PltchAPfHpl
lPa-Dsl
Commants:
-l Ir -1 o11-L ila o, s16
-3 la -5 (),L, .5
'-1 ,-l -s O.(,3?-r-t lt *t 6.Lt 7It I -{o. L7-?l,a -5 O.tt 5-q ld -?o (r1
Run I c lnrtTlma:I ollo Itop llmc:).17
Port
StertTcmg
tT)
YewAlrh
tDG(
vfftyAP('Hpl
lPr+zt
PlldraPrHrol
lP4+sl
Cqnmsnts
-l tlt oLl 6-J.ll -1 Osr
--?-6 oGtl
-11 ta -Lr o63a-tll O.t<*.f.n -Ll g fi6 \-3 ,-(-q 2 (A
-Ll ,,e -(o65
GP043AS-036892-RT- 1789 Reviewed : FPM_jEsq4CBI/t_gE
EPA Method 2F "Fast Ftow', Datasheet
ttolcctCodc Oat{77-lemmartrlc pt:rsra l'llll:24.t7 lrm
Ohnt 7^-; [.}. .,r>SCtkPresuru ('HrOl:-5.<n""
burcal ll.l*.to, 7 PrcbelD/Alhnmcnt lt?Probc Condldst
Ipcntor{rl:ilr'L(lD Conroh lD:ill-Z o cor lfl t2. o
Datr:llltq lzt [crk Chadr ('HrOl:r'o: (t3l 7.s
lun I 4 Itrrtfrna:tzzb ibprhc:)233
Inurrsc Polnt
lPort+ohl
StrdcTcrn;
(oFl
YewAlalc
t Der
velodty6PfHpf
(P1+21
PltdraPf}f,pl
lP'l-P5l
Eommcnts:
5 /Iri -a .3q
2 n5 -t ,55
I t/{'3 .58
cl ur'-7 .L5qIt/<- l.l ,35
2 t/s -3 .39
4 //<-(..Ltqtl5, (,5
lun I {It rtTlmG:I 23<itopr!rG:I Z*o
,ort
StedrTcml
frt
YawAqh
tDe
VclodtyAP ('ll20l
lPt+21
PldraP(-ttol
lP.0+Sl
Eoarmentr:
3 (ilt -Ll 4t
2 ltt -L/tf6
3 il5 -1't6l
q l6 -7 ,LOIIt t.t -.1 ,36
2 lts .U ,31
3 Irs .L ,61
Ll Ir<-.(,,o
lun I L lbrtThnc:t24L Itollnre:t^1?
Dort
ItedrTcmS
fF)
YewArylc
tDGr
VclodtyAPfHrO
lPl+2t
PftdraP fHrol
IF+PsI
Commentr:
,?I lt<,l {!{
2 ttl ,5Ll
4 t/5 -5 LO
u It5 -j ,c 3
I_tt tt5 -7 ,3h
7 lr{-3 ,35
3 Irl -q ,60
hJ )t<-a ,LO
Profcct Codc +-g4;-$-] A,leromeElc Prr,rsura l'Hd:ZLl 9z qEdhntPo, .(,( n,',-,lCtlc Ptes$rr l'l{,Ol:-5 5 lrobrre:v) ,. ^l ..Prolc lDlAlLnrncnt l35/ u''hobcCoodldon j/Denbr(rl:AL /c r 3O C.onsolc tD:<D 0orlxl lZ. otl - lq - eq lueroracrfnpl:q lxl 7.,{
EPA illethod 2F "Fast Flow', Datasheet
lun !StartTtnc:i).11 ttopTlme:la r?
Irrurre Foftrt
IPoftfolntl
SiedTcml
(?YtwArgh
t Dcr
Vclodty6P fH2O!
(Pr+a
Prul aP rHto,
lP+Pst
Conuncntr:
ir ^8 e#+ AL c'lf t-l l,l -8 ().5 >t-3 la -6 o6r^1 tti -5 o,6 3d-l,l -5 o '17
-"1 ,-5 o p*(
-3 ,, I -e o. B',e-Ll t2 -1 o65
lun I K Shrt[mc:Itoo Tlnr:t)) G lsol
Port
Stact Tcmg
rFt
YawA4te
t DGt
Vslocltr6P fX.Ol
lPr+21
PldrAPl'ttOl
(P{.Pst
0onrmcnis:
t tl _rl 0.Ll'7-)lr?.-1 O so-3 It ?.-5 o 6t-cl ,ra -"1 U'10.4a-lr -a O,qs-a ,a *C o 57-3 lra - (-l U.Gd-q ll3.Ot
Run I "l ItartTtne;ftogTtne:l3o )I 30:d-
Port
StectTcmg
fF,
YrwAndc
tDlr
Vdoclty AP ('ttiOl
lPl-P2l
Ptrdt
lt
oPrH.Ol
t&psl
Eqnmcnts
-t ill _rl o\f-)ll I -)o,{-d-f ,f.-C o 6d-q l,a -3 o,6 )llt -6 o.'t7-f,,ll -L,os(
r)\ltl -s o b,- ..t ,,a.-3 0 r,-)
GP043AS-036892-RT-1 789 Revlewed: FpM p"ge a{fryhs
EPA ltiethod 2F ,'Fast Flow., Datasheet
,to GGtCodG c,3[a Bq 2-lenrnctle pr:rnrra (. l{rl:2+,+7 UaClhnr)n r',{irn,rD ldcPressum l'l{Jll:-,5,,L!burtc:U,3 H\JnT T Prubc lD/Allnnrcnt:l-PtolG condhloo v-Opcretor{rl:N5 lD Conrolc lft ,tlh- )A corlxl /Zr*Dlte:I lln ft+Laet Chcct (.HrOl:orlrl 7. r-
Nun !1 lbrtflnlG:1r+cl llopTlmc:t lL5 L
fr.vcrrcDolnt
IPort+olntl
ItrdTcmS
('Fl
VrwAlfh
t DGr
VdodtraPl'ltpl
(P1+21
PlldraPrHpl
lF|.pst
Eommcnt$
1 6 -L 7C
2 I €,-6 6-t
4 lt€,-L{(.f\
rl t6 -b ("C>{\c)-s \1
2 lc)-l ,51z\5 -a ,61r{()-5 (ol
lun t ,\r ItrrtTlmc:TJ,O bplnr:r?o
Port
lEdrTrnT
fFl
VruAnjla
t D.r
vdalrvlPfHpt
lPl-P'il
PHr aP fHpl
lF+Psl
Eommrrlr:
3 I lc-,+to216-l .^l
1 ib _L{. ll?,L{It5 -?- ('rrf'l't I 16r -1 ,-tL+
Z I t6:-(,,5b
7)I \tr)-l .2qLtlt5--7 . ta(
lun I q ftrrtfht!:i?YL Itaallm: ilfi 30R
Port
StrctTamg
tTt
YruAfh
t Drt
vcbdyaPfHOl
lPl+21
Pftdr6Pl.Hpl
ID!.DEI
Eommcnts:
Z \ rr>*7-.uu
7 \6 -L{,AZ
2)\16 -Ll ,fu+\il \ \c)-t [oltr5t l6)--t u6 \2 ri6 - --l ,bljt\b --l u cJb4l6'r --t .bo
GP043AS-036892-RT-1 789
Revlewed: FPM*, *#;pIU_
Appendix A.3.1.2
Mid-Load Flow Data
GP043AS-035892-RT- 1 789 Page 51 of 195
Client PaclfiCorp
Unit lD Hunter 3
Load Mid
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H2O)
O, (%vd)
CO, (%vd)
Vr. Volume of Water Condensed (mL)
V. Volume of Stack Gas Collected (dcfl
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
T. Temperature at Gas Meter ('F)
Calculations
Pil Absolute Pressure at Gas Meter ("Hg)
T. Absolute Temperature at Gas Meter ('R)
Vwcl:rd) Volume of Water Condensed (scf)
Vmtstdl Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
Bs,.t Saturated Moisture Content (%/100)
B* Measured Moisture Content (%/100)
Bs StackGas Moisture Content (%/100)
24.47 24.47 24.47
-5.50 -5.50 -5.50
888
11.s 11.s 11.s
24.47
-5.50
8
11.5
24.47 24.47
-5.50 -5.s0
88
11.5 11.5
75.6 76.6
27.099 27.099
0.997 0.997
1.7 t.7
62 52
24.60 24.60
522 522
3.60 3.50
22.46 22.46
43.6 43.5
0.110 0.109
0.138 0.138
0.110 0.109
(Saturated) (saiurated)
24.47 24.47 24.47
-5.s0 -5.50 -5.50
888
11.5 11.5 11.5
76.6 75.6 75.5
27.099 27.099 27.099
0.997 0.997 0.997
L.7 1.7 1.7
62 62 62
24.60 24.50 24.60
s22 522 s22
3.60 3.50 3.60
22.46 22.46 22.46
43.3 43.5 43.4
0.108 0.109 0.108
0.138 0.138 0.138
0.108 0.109 0.108
(satur.tcdl (srturatcd) (s.tur.tcd)
70.4 70.4
26.256 26.256
0.997 0.997
L.7 1.7
61 61
24.60 24.60
52L 527
3.31 3.31
21.80 21.80
43.3 43.5
0.108 0.109
0.132 0.132
0.108 0.109
(Satunted) (ktur.ted)
70.4 76.6
26.256 27.099
0.997 0.997
t.7 L.7
61 62
24.50 24.50
52L 522
3.31 3.50
21.80 22.46
43.4 43.4
0.108 0.108
0.132 0.138
0.108 0.108
lgtureted) (S.turated)
GP043AS-036892-RT- 1 789 Page 52 of 195
Mld Load Run fl1
l@tlon: Huntar 3
load (MWl: 29t
Dd.: rlll9l2024
St dnmc: la:U
End Tlm: 14:15
Probe / Gas Data
Probc Il Re: o dclr43
Prob.l2 R@: 0 d.tres
P.ob! 11 Rao: -Ol d4.*3
Problt2Rslo: .13 dcarei
8,.: 0.10rS tillq,
Md: 30.15 lblEhoL
M.: 2t.85 lbflb-doL
Pb: 2i1.4, ln Ht
P.: -S.5O ln HrO
P.: 2a.0, ln Ht
XCOI: llj X
!(Or: t.0 X
t{ao: 0O X
m.s x
Flow RATA Traverse Data
Point lD Prob. lO
Coractcd
tt*tlamp Y.wA.rtb Y.wAntL Pl-P2
trl ldell o. ld..l aln H,ol
unadlurEd i.pl..!mnt Polnt ur.d t wAF
Arl.lvclelty Arl.lvclodty lor Polnts
v- lttlcl v.lftlrG.l wAF? U3.dc-
001 107 o)6 om 1 450
m2 1 108 .1 o.9 0.32 0.8090 35.38r
003 1 109 o 0.1 0.3s 0.4090 37.039 nla
flx 1 1o:)0 ol ot oam 3S.95S
00s 107 -1 o.9 0.24 0.8090 30.61il ^la00610800.1 0.32 0.4090 35.385 nla nla
007 1 108 I -0.9 0.36 0.8090 1 \)7
008 I 101'0 0.1 0.36 0.8090 37.565
009 2 109 I 0.8 0.1s 0.8380 25.115 nla nla
010 2 2 -1 4.7 o.77 0.4380 13.747
011 2 2 .1 0.E 0.33 0.83E0 37.349
o12 2 12 1 0.8 0.34 0.8380 37.911
013 2 1.7 o.25 0.83m 32.501
014 2 2 .1 0.8 0.32 o ,3m 36.779
o15 2 12 -2 -0.2 0.34 0.8380 t7.914 nla
016 72 .2 -o.2 0.3s 0.8380 38.458
iwat6 1Gt.9 -1.1 -{r.2 0.3r o.a23s ls.o72 nl. nla
GP043AS-036892-RT- 1789 Page 53 of 195
P,ob. tl RM: 0 d.3r43
Pobc 12 Re: O d.3Rs
Piob€tl Rro: 4l d.lrEs
Pob. 12 RrLo: -18 dclrei
B-: 0.1089 X/10o
M.: 30.16 lbflb-molc
M.: 28.t4 lbnb-molG
Pb: 24.47 ln Ht
P.: -5.50 ln ]tto
P.: 2it.0, ln H!
XCO,: l1s xrc,'----------i9x
t(CO: O.O ta
&r.5 x
Mid Load Run #2
[@tion: Huntlr 3
Load (MW): 29t
D.t.: 1,.ll9l2o24
St.nTim.: l4:lt
Endlim.: l4t2t
Probe / Gas Data
Unadiusted Results
v.(aw); 35.84 ttlrc
Qsw: 49,511,875 s*llhr
Flow RATA Traverse Data
Polnt lD PmbG lD
cord.d
St.cl T.mp Yaw Antlc Y.w An3L
lFl ldetl o.ld.il
PL.?2
(ln HJI
Un.dlun.d lcplemnt Polnl U..d I WAF
Arl.l v.lclty Arl.l v.loclty lor PolnB
v.lft/se.l v.(ftl3el WAF? U$dc-
001 108 -5 4.9 0.23 oam 29.898
m2 109 2 - 1.9 0.33 0.8090 35.9s5 nla
ool 109 3 -2_9 o.35 0.8090 37.003
oo4 lm o o.l o.35 o_aBo 37.S7S
005 108 I {.9 0.25 oms tl.242
005 108 2 -1.9 0.32 0.8090 35.376
m7 1m 0 0.r 0.34 0.8G)0 36.517
008 109 o o.r 0.35 o.mo 37.0S0
009 2 2 4.2 0.27 0.8380 33.796
010 2 1 0.8 0.29 0.8380 35.023
011 2 2 4.7 0.34 0.E380 t7.925
012 2 3 1.2 0.33 o.83ao 37.3S5 nl.
013 2 {2.2 o.21 0.83E0 3.772
o14 2 3 -t.2 0.35 0.8380 38.471
015 -0.2 o.34 o.8380 37.925
015 2 3 1.2 0.35 0.8380 1A_477
\EEtcs 110.3 -2.1 .1.1 0.32 0.t2rs 35.t37 nl. nla
GP043AS-036892-RT- 1 789 Page 54 of 195
Mid Load Run #3
loatior: Huntar 3
Lo.d (Mw): 3Ol
D.tc: l,.lL9l2024
StanTimrr 14t25
t7d Tlm.: l4:3O
Probe / Gas Data
Prob. l1 Re: 0 d.trc.r
P@bc t2 Re: 0 dctrei
Proball Rao: -Ol datret
Proba 12 Rsro: -1.t d.!re.s
e*, -------i.iii x/roo
M.: 30.16 lb/lb-noh
M.; 28.65 lb/lb-mola
Pb:-llLglnHt
P.: -5.5{, ln KrO
P,: 24.07 ln Ht
XcO2: ll5 t(
rc,'__________l9x
%CO: 0.0 t6
80.5 ta
Flow RATA Traverse Data
Polnt lD Prob. lD
CorrcctGd
St.ct Tmp Y.w Angl. Y.w And,. Pl-?2
lFl lhrl O fddl 116 H-Ol
Un.dlurt d Repl.cmant Polnt UFd I WAF
Aial Vrldlty Axl.l Vclodty fo. Polils
u-[fi/*rl v- lftl$cl wAF? U$da
001 107 4 -3.9 o.24 o-a09 30.550
002 I 108 -2 -1.9 o.32 0.8(x}0 35.370
003 1 108 -2.9 0.35 omo 35.964
m 1 109 t.9 0.33 0.8(DO 35.950
005 108 "0.9 0.24 0.8090 30.644
005 I 108 1.9 o.3l o_amo 34.813
m7 1 108 1.9 o.36 o.8090 37.516
008 109 -1.9 0.35 0.8090 37.549
0(x)2 2 '0.2 0.26 0.4380 33.159
o10 2 0.8 0.32 0.8380 36.783
011 2 0.8 0.34 0.8380 37.9L5
012 2 2 o.a o.35 0.4380 38.i|69
013 2 4.2 0.25 0.83E0 32.s15
014 2 .t.2 o.31 0.8380 35.200 nla
015 2 2 o1l o.a3m 37.v9
015 2 2 4 2.2 0.35 0.8380 38.ir44110.1 .2.2 -1.2 0.31 0.823s 35.637 nla nla
cP043AS-036892-RT- 1 789 Page 55 of 195
Mid Load Run #4
[c.tlon: Hlntar 3
toed (Mw): 294
D*.: 1t/1gl2024
St.nllm.: 14:5t
endllm.: 15:03
Probe / Gas Data
Adjusted Results
Va(avtl: 35.43 ft/nc
Qsw: 48,97O,26E w*tlht
,315
Prob. 11 RM: o dctrc.i
Preb€ 12 Rel 0 delret
Prob. l1 Raoi -ol dct.4s
Probcl2Rsro: -l.t d.tress
8-: 0.t0E3 X/lql
Mi: 30.16 lblb-mol.
M.: 2a.84 lblb.moh
Pb,:-l!jqlnHg
P.: -5.5{, ln HrO
P,: 2a.07 ln Bt
XCOr: 115 t(
t6or: t.0 X
9(EOt 0.0 9(
dr.5 x
Flow RATA Traverse Data
Polnt lO Probc lO
Corradad
skt TCmp Y.w And. Y.r Anth Pl-P2
lrl ld.rl o.ldrl lln HJI
Un.drurt.d Repl.rGm.ht Polrt UrGd t wAF
Axl.l Vcloclty Axt l V.lo.lty fot Pohts
v-ltt/3ccl v-(ft/sel wAF? usdC
00,108 .2.9 o.24 0.809 10 510
m2 108 1.9 0.34 0.8090 t5.450
003 108 o o.1 o_3s o.8090 t7.013
@4 1G'0 o1 o36 o amo 37.571
005 108 ,1.9 0.24 0.E090 to 513
ffi 108 4.9 0.31 0.8090 lil.829
oo7 108 {9 o_34 0.8090 36.476
008 109 0 0.1 o.35 0.8090 37.m5
009 0.8 0.29 0.8380 3S.018
010 0.8 0.32 0.8380 t6.745
011 2 4.2 o.32 0_a3a0 36.7E8
012 0.8 o.17 0.8380 19 5S4
o13 112 3 1.2 o.24 0.83E0 t1.853
014 3 1.7 o.31 0.8380 36.201
015 112 {o3 o a?m 37.331
016 7 112 0.8 0.35 0.8380 38.471
110.1 .1.6 -{r.6 0.32 0.823s 35.790 nl. ^la
GP043AS-036892-RT- 1 789 Paqe 56 of 195
Mid toad Run #5
Ldaiion: Huntcr 3
Ldd (MW): 3{X,
o.E: ,117912024
SEft Tlm.: 15:05
End Tlm.:
Probe / Gas Data
l5:10
Prcb.Il Roo: O dctE.
Prcbc 12 Re: 0 d.trcc!
Probc 11 Rs: {l det,ces
Prcbt 12 RsLo: -1,t d.a@3
a.,,-------6.Gix/roo
Md: 30.16 lblb-m|.
Mr: 28.t3 lbllb.molc
Pb,: 24.4, ln Ht
P.: -5.50 in Hro
P.: 2il.0, In H3
"lCO.t lL.s'As,'----------i9x
XCO: 0.0 X
&r.5 r
Flow RATA Traverse Data
Polnl lD Prcb. lO
Corffiad
St clYcmp Y.wAhtl. YilAndG P1-P2(Fl ld.tl q (dcl lln H,ol
Un.dlurtcd R.pl.emcnt Polnt Usd I waF
Axl.l Vrlclty Axlal Vcloclty fo, ,blntt
v.(fVG) v.lft/sl wAf? urcdq
ml 109 3 2.9 0.24 0.809 30.646
m2 110 o o.1 o.34 0.8090 36.555
003 110 2 ols o.8090 37.O58 ale
m4 109 o 0.,0.35 0.8090 t7 0s6
005 1m 3 -2.9 0.25 0.E090 31.2s'
006 109 0 0.t 0.32 o-8{x}o 35.432 nla
007 109 2 1.9 0.35 0-8090 37.036 nla
00E 1o!)0 0.,0.35 0.E090 37.056
00{,2 4 0.27 o.8380 31.777
010 2 {2.2 0.31 0.8380 36.193
011 2 1 0.8 0.33 0.8380 37.366
012 2 -2 {_2 o.35 0.43E0 39.031 nlz
013 2 1 0.8 0.24 0.83E0 tl s5
014 2 -2 -0.2 0.32 0.8380 36.799 ^la015{-2_2 o.34 0.83E0 37.9()4 nla
016 2 3 1.2 o.35 o.a3m 14.477
110.6 -1.9 -1.0 0.32 0.823S 35.845 nlz nl.
GP043AS-036892-RT- 1789 Page 57 of 195
Mid toad Run fr5
L4rtlon: Huhtcr 3
tdd lMwl: ,98
o.tc: ltlL9l2o24
Slad Tlmc: 15:12
fnd Tlm: 15:17
Probe / Gas Data
Unadiusted Results
avg): 35.75 ftlcc
Qsw: 49,?4,4O7 wscllht
Prob! 11 RD: 0 dcf..3
Prcb. ,2 Re: 0 d.t.ei
Prcb. tl Rs: -ol d.lr4s
Ptob. 12 Rao: -L8 d.lret
B,: 0.1091 r/lOO
Md: 30.16 lb/b-mol.
M,: 2t.83 lb/lb-mol.
Pb,: 24.a7 ln Ha
P.i -5.50 ln HrO
P,: 24.07 ln Ht
,(Cor: lls tarc,r--------i9xtaCO: 0.0 X
Adjusted Results
Va(avg|: 35.39 ftlscc
Clsw: 48,890,563 w*t/hr
Qsd: 43,557,8tE dtrf/hr
Flow RATA Traverse Data
Polnt lD Prob. lO
Corradad
Stacllcmp YawAntlr Y.wAntlc
lfl ldc.l (L (ddl
PI"P2
lin H,ol
Un.dluit.d R.pl.c.m.nt Polnt Ued I WAF
Axl.l Vclclty Ai.l VGlodty for Polnts
v.lft/*.} v.lft/*cl wAF? uxdc
m1 1m 3 .1.9 o.2s o ao9 11.247
oo2 109 0 0.1 0.35 0.8090 37.05
oo3 109 1 o.9 o.35 0.8090 37.O47
ool 110 0 0.1 o.35 o.8090 37.084
mq 1m 4 -3.9 o.74 omo 30.s84
o06 108 0 0.1 0.33 0.8090 35.946
007 1 1(x)2 ,1.9 0.35 o.8090 37.031
m8 109 2 1.9 o.3s o.ao90 37.031
o09 2 -5 t.2 o.26 o_a3ao 33.11il
o10 2 3 1.2 o.31 0.8380 36.207
oll 2 2 4.2 o.32 0.8380 36.794
012 1 o_8 o.36 o aqao 39.023
013 2 I 0.E 0.23 0.8380 31.19r nla nla
014 2 1 0.8 o.31 0.8380 36.2r2
o15 I o.8 o.34 o_834o 37.923
016 0.35 0.8380 1A 472
lvc6tas 110.4 -l.E {.9 0.32 0.8235 15.747 nl. nla
GP043AS-036892-RT- 1789 Page 58 of 195
Mid Load Run S7
L6ii6: Hunter 3
Lo.d (MW): 297
D.tc: tlllgl202l
Strfr Tlme: l5r!9
End llre: 1514
Probe / Gas Data
ftob. *1 Re: O d.trs
P,obG 12 R@: 0 det@t
Prob. ll q@: {l d.tret
Prcb.12 Rsro: -1,t d.!m.
a-, ------if6ii x/roo
M.: 30.16 lblEmh
M.: 28.E5 lb/lb"mol.
Pb: 2l.i|7 ln Ht
P.r -5.50 ln HrO
P.: 2a,0, l6xt
96COr: U'5 tarc,'----------i9*
96CO: 0.0 96m-s;
Flow RATA Traverse Data
Polnt lD Prcbr lD
Co,rratGd
StackT.mp YawAndc Y.wAntl.
l;l ldel O ldel
P1.P2
lln HJI
Un.dluncd R.pL@nt Polnt UFd t wAF
Arl.l VclGlty Arl.l V.lo.lty lor Polnt!
v- ltrlc.l v- lltl*l waF? u*dL
m1 107 3 2.9 0.23 o aog 29 q36
002 lo7 1 -o.9 0.34 o.8090 35.439
003 l08 {_9 o.35 o.8090 37.529 nla nle
004 108 2 1.9 0.37 o8M 14.o30
m5 r08 l 2.9 0.25 0.8090 31.238
006 t08 o 0.1 0.36 o.80!)o 37.533
007 108 I {.9 0.38 o.8090 38.557
008 r09 0 0.1 0.38 o.8(xl0 38.596
009 112 -5 3.2 o.22 o.8380 30.452 ^la nle
010 t12 2.2 0.31 o.a3m 16.174
o11 112 -2 {.2 0.34 0.8380 37.916
012 112 4 -2.2 0.36 o.8380 38.987 nle ala
013 Ll2 3 1.2 0.2s o a3ao
o14 112 I 0.8 0.3,0.8380 36.201
015 112 -1 0.8 0.33 0.8380 37.351
015 1L2 I o8 o37 o.a380 39.SSO
lErarct 1Gr.9 -2,O -1.1 0.32 0.8235 36.052 nl. Bl.
GP043AS-036892-RT- 1789 Page 59 of 195
Probr ll Re: 0 deir4i
P.obG ,2 R@: o dctiGca
Probcll Rao: -01 detre3
P.obc 12 &to: -l.t dGt@5
B-: 0.1091 X/1q,
M.: 30.16 lb/lb-nol.
M,: 2E.E3 lb/lb-mol.
Pbl 2,l.iu ln Ha
P.: -5.50 ln HrO
P,: 2a.0, lnHt
ticorr 11.5 f
taor: 8.O X
t(CO: oo 9(tal{': 8O.3
'6
Mid Load Run fl8
Mtlon: Huhtar t
Lo.d (Mw): 297
o.t.: ltlt9l2o24
Slrn Tlh.: 15:26
Unadiusted Results
Va(aW): 35.97 ftlscc
O,sw: 51,O1L,732 *xtlht
End Tlm.:
Probe / Gas Data
15:31
Adjusted Results
Va(avt): 36.60 tVrccqsw: 50,561,015 *scrlhr
Qsd: 45,O46,L17 ds<llhr
Flow RATA Traverse Data
Polnt lO Prcb. lD
Cormcd
Stacll.mp YiwAndc Y.wAntl. P1-P2
lFl (d.d (L lddl lln HJrl
Uh.drun.d RepL@mnt Polnt Ut d t WAF
ArLl v.lGlty Arl.l vGloclty for Polntt
v- (ltl*.l v- lft./cl wAF? U..dc
001 r08 -)9 o.26 o.809 31.865
002 109 -0.9 0.35 0.8090 t7 M7
003 109 0 0.1 0.36 0.8090 ,1.577m1m-1 1.9 o.17 0.8090 38.074
oo5 108 o2q o 8mo 31.214
006 109 .1.9 0.36 0.8090 37.5s6
007 109 "2 1.9 0.38 0.8090 18.586 nla nla
mt 1m o o.1 o_39 o.8090 39.111 nla
@9 .0 0.25 0.8380 32.522
o10 0.32 0.8380 t6.7A7
o11 112 -2 0.35 0.8380 39.026 nla
o12 12 {o_17 o_a380 39.565 nla
o13 -4 0.29 0.6380 t5 m2
014 2 12 ,4 0.3s 0.E3EO t8.452
o15 2 12 o.8 o.36 0.8380 t9.023 n/a
016 2 0.8 ota o a3m ilo.0!12
lv!nt6 110.4 -2.1 .1.1 0.:14 0.8235 il6.!169 nlz n/a
GP043AS-036892-RT- 1789 Page 60 of 195
Mid Load Run r#)
l@tld: HuntCr 3
Lo.d (MW): 3Ot
O.t.: Llll9l2024
Shn Tim.: t5:33
EndTl6.: 15r3t
Probe / Gas Data
Prcb.lt RD: 0 datl..t
Prcb.l2 RD: 0 d.tret
Probc 11 R{o: -ol d.ttet
Probc 12 RsLo: .1.8 d.!rc.t
8E: o.1@5 tallm
M.: :10.16 lb/lb-mlc
M.: 2t.tl lbnb-moh
Pb: 2a.il, ln H!
P.: -5.50 ln H2o
P,: 2a.0, ln Hg
t{COt: lls tasrt----------Ex
,(COt Oi r,(
: tO.S X
Flow RATA Traverse Data
Polnl lO Prob. lO
co.rd.d
St*lTrmp YawAntl. Y.*An3lG ?r-Pz(Fl (d.rl (L (dal (ln H,ol
un.dlurt.d Rcpl.ccmcnt Polnt U3.d lwAF
tuhlvddlty Arhlvdodty ,or Polnts
v. (lv*c) v. (ft/*cl wAF? u*dq
m1 1 104 4 3.9 0.26 0.809 31.828
002 104 {.9 o.34 0,8090 36.477 nla
oo3 1 10E 9 o35 0.8090 37.519
oo4 1 109 0 0.1 0.37 0.8090 38.091 nla
00s 108 4 -3.9 o.25 0.8090 31.210
0(x 1 108 {_9 o3s 0.8(})O 37.010
007 1 109 o 0.1 0.37 0.8090 34.091 ^la nla
m 1 1011 1.9 0.3t 0-8090 38.581 nla
009 2 0.8 o.27 0.8380 33.791 nla nle
010 2 2 4.2 0.3,o.a3m 36.210
011 2 {.2 0.34 0.83to 3t.922 nla
ot2 2 112 -2 4.2 0.35 0.8380 39.021 ile nla
013 2 4.2 0.28 o a1s 14 ala nla nla
o14 1 0.8 0.32 0.E380 36.786
015 2 -1 o.8 o.35 0.8360 34.472 nla nlz
015 2 3 0.38 o.a3m 40.m2
lwEaas 110.2 -l.t .0.8 0.33 0-423s 36.5!r4 nla il.
GP043AS-036892-RT- 1 789 Page 61 of 195
knplnac.
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GP043AS-036892-RT- 1 789 Page 62 of 195
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GP043AS-036892-RT- 1 789 Page 63 of 195
ffiCodG ortr€+Neromatrlc Pressurc l- llrl:,?1 .q )[.-
dhrtt 'rr. ,(: Co r o idc Presrur: l'Hfl:-ss n"t
lourca:ll u.nler 3 ProbclD/Alknmcnt t3s./,-PtobsCondhbn l/lpcntor{d:At /t L lD Consolc lD:?D-Or(xl lt. s
DlE:- lc, -,1 (,lcel Chedr (']&Ol:02(rl E,A
EPA Method 2F "Fast Flow', Datasheet
t, i' : , i'''f i' 'i i '' ri! /'.:i';
r:! ,rr:\ttl. .r'. 1.. \.
36 scla
lun I iltN It rtTLnG:t1 ll lbpTlmc:lrl lL
lrevrrse Polnt
lPm+ohtl
StadTaml
frt
VrwArqlc
t Dcr
vdodtyaPrHpl
(Pr-P:il
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(P+Psl
Conrrnents:
lo7 ..1 o, J,c
-)t o15 .,IDJE-3 loq o 6 35
-"1 toq'o o.3 3a-t ln'7 A. -J "{
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iun t ?ilrnrlmr:lL) t1 itopTlmc:lla:
,ort
StrclTcmg
("F)
YawAr6lc
t DGr
VclodtyAP('H1Ol
(Pr+21
PtEhAP(.Xpl
(Ptt+s)
Comments:
-l lo4 -s o a3-a to1 -a p.-3s
-3 to'l -3 o.s s
.. c1 lol )O,36
lox -l 7.es
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tEdrTcmS
(T)
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Commcrts:
lo-t -11 o,a1.J t04 - rr1 o,5a
-3 I O<l -3 o.35
-Lt locl -e o.33
t06 h.A1--)tos -a o..3 I-3 loq -,o3c-q toq .-a o.,3 6
GP043AS-036892-RT- 1 789 Reviewed: FPMe.s. 6a GtMq
ProhctCodc 03ta*2-leromctrlc Pr:rrurr l,llrl:z+,\-,ReoCthnB[Lr;{;cr*o Itedc Prcsrurc ('HrOl:-5, r)Loburcc:U 1 Ltuntt f Ptobc tDlAlhnmant:t\1 Probc Condltl,oalpqntodrl:/13 lDConsolc lD:&.6-Lo cch lrlDrtc:tllrqtz+LartChcd('H1Of:or lrl g.o
EPA Method 2F ,'Fast Flow" Datasheet
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GP043AS-036892-RT- 1 789 Page 65 of 195
EPA lUlethod 2F '.Fast Flow', Datasheet
holact Gode sSrr-s-I lerurcrtrlc ptrrsura (. l{tl:e1,q7 U6dhft1cif ;( ^r.,lEdc Prcssuc ('H,Ol:-5 s-&oSouttc:ilrnlcr 3 Probe lDlAlLnmcnt t)5/ u'Probe Condhbn?rnor(sl:AL /cL lD Conrolc tD:3D* t qqlxr It.;)eE:tr^11-aL,Leat Chcct l.H2Of:or(r)8. o
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toq -3 o.Jf.f locl o O ss--J lo4 D.3s--q I tts o O.3 s-)-lou -L.l o. ag-J ,D g ,A c.3 3-]loq D.35qlocl-N-t o.-3i
Proiact Codc o<(6 Eqz Elrcmsrlc Pcsruru (,lld:Z{ ' {2'lemIlcntt'k,,S.'.oro ldcPrrssurc l.H0l:-6,?)hLlourcr:u 3 Hurner PttbelD/Alfnnmr t\ -7 ,robG Condhbnopcnbr(rl:A3 ,D C.onrolc lD:*1.D--7.!Eilrl ll,f
-lq /zq LcetChcd(.HrOl:or(rl
EPA Method 2F .'Fast Ftow" Datasheet
tun I rl /'4, d 5tnftnc:iq5.ItopTlmG:1503lrrrcrre Polnt
Port+olml
llect Tcml
frt
Yew&Uc
t Dcr
vclodyaPfH1ol
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PlldraPfHlo,
lPf{st
Eonmcnts:
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GP043AS-036892-RT- 1789 Revleurcd: FpM+aEe6+SIybsr_-
PnDrGGt Code .e*t+'&:t flt Barorrr strlc Pnsure l'Hrl :&Y9z R.-thnr f...{,Coro Hc Prcsqrn I'H'O!:'s b Rto
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GP043AS-036892-RT-1 789 Reviewed: FPM o^g. nn 6ip{U5__
ProhclGodG fr 1(o*[L BarlllrGttlc Prllsure l,lld:2L{ .ql LEtrhntRrcif; cort)Itrtls Pr:snnr (.]LOl:* c) rQ)!""iourca:u4 hlunlti Probc lD /Alfnmm+.r\-1 lroboCondlthn/tt 5,rE.agltr:lO Cql5olc lD:P|€r- 7A qqlrt ll,r
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EPA Method 2F '.Fast Ftow" Datasheet
t ,'tt"".'" i ' t. ', ,.
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GP043AS-036892-RT- 1 789 Reviewed: FpMaseess6pt{s____
Appendix A.3,1.3
Low-Load Flow Data
Client Paclflcorp
Unlt lD Hunter 3
Load Low
EPAMethod3&{Data
lnpsts
Barometric Pressure ("Hg)
Stack Static Pressure ("H20)
O, (%vd)
CO, (%vd)
Vr. Volume of Water Condensed (mL)
V. Volume of Stack Gas Collected (dcfl
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("H2O)
T. Temperature at Gas Meter ('F)
Calculations
Pm Absolute Pressure at Gas Meter ("H8)
T. Absolute Temperature at Gas Meter ('R)
Vwc6ta) Volume of Water Condensed (scfl
V.1,ta1 Sample Gas Volume (dscf)
Stack Gas Temperature ('c)
B*., saturated Moisture content (%/100)
B* Measured Moisture Content (%/1001
B* stack Gas Moisture content (%/100)
24.76 24.76 24.76
-5.50 -5.50 -s.50
999
9.5 9.s 9.5
24.76 24.76 24.76
-5.50 -5.50 -5.50
999
9.5 9.5 9.s
24.76 24.75 24.76
-5.s0 -s.50 -5.50
999
9.5 9.5 9.5
88 88 111.9 111.9
45.538 45.538 45.367 45.367
0.997 0.997 0.997 0.997
1.7 1.7 1.7 1.7
54 54 58 58
91.3 91.3 115.8 115.8 53.8
45.s85 45.585 47.978 4L.978 27.048
0.997 0.997 0.997 0.997 0.997
L.7 L.7 r.7 \7 1.7
60 50 51 61 61
24.89 24.89 24.89 24.89 24.89 24.89 24.89 24.89 24.89
s14 514 518 s18 520 520 521 521 szL
4.t4 4.14 s.27 5.27 4.30 4.30 s.45 5.45 2.53
3a.77 38.77 38.33 38.33 38.37 38.37 35.26 35.26 22.72
4t.L 41.1 4L.t 41.1 4L.t 4L.L 41.1 41.1 41.1
0.095 0.095 0.09s 0.095 0.095 0.095 0.095 0.095 0.095
0.096 0.095 0.121 0.121 0.101 0.101 0.134 0.134 0.100
0.095 0.095 0.095 0.095 0.095 0.095 0.095 0.095 0.095
{S.turated) (s.turetrd} (s.tur.ted) (Satlr.tcdl (Saturat.d) (Situr.ted} (Satur.tedl (s.turatcd) (Saturated)
GP043AS-036892-RT- 1 789 Page 71 of 195
Low Load Run fll
l@tlon: Huntar 3
Lo.d {Mw): 18t
o.tc: 1112012024
SiadTlm.: 7ta3
End Tlm.:
Probe / Gas Data
P,ob! 11 RD: 0 d.tr..t
Pioba f2 R@: 0 d.treg
Probclt RsE: -01 d.tres
t"obc 12 Rsto: -l.8 d.!@i
8,,: 0.0949 '6/lq,M.: 29.tt lb/lEmolc
M,: 2t.75 lb/lb-mol.
Pb,: 24.16 ln Hg
P.: -5.5o ln H2o
Pr: 21.36 ln H8
tacor: 95 X
xo2: 9.0 X
XCO: 03 t{
!6,f,: al.s X
Adjusted Results
Va(avgl: 29.15 ftl*c
Qsw: 41,074,511, **tlht
Flow RATA Traverse Data
Polnt lO Prob. lO
Corrdad
St.clT.mp YawAntl. Y.wAntlc P1-P2
lfl ldc.l q ldc) (ln HJII
un.dlu.t.d RcpL@mcnt Polntuad twAF
Arlal vclclty Arl.l V.lo.lty ior Polnis
V. (fvs.) V. lft/Gl WAF? Usrdc-
ool 2 106 0.8 0.16 0.838 2s.7@
oo2 2 106 o 1a o)1 o alao 29 Sm
oo3 2 106 0 1.8 0.23 0.8380 30.873
004 2 106 0.8 0.25 0.8380 32.2m
00s 2 106 .2 4.2 0.18 0.8380 27.325
006 2 106 0.8 0.20 0.8380 28.801
007 2 106 -o.2 o.22 0.8380 30.209 nla
008 2 106 4.2 o.24 0.8380 31.552
m 106 {.2 0.15 o.8380 24.944
010 2 106 o 1.8 0.22 o a3ao 30.194
011 2 106 0 1.8 o.22 0.8380 30.194
o12 2 106 0 1.8 0.25 0.8380 32.187
013 2 106 o8 o14 o a3ao 24.096
014 2 105 0.8 0.23 0.8380 30 gas
015 2 106 0.8 0,21 0.8380 t0.885
016 tffi 0.8 o.74 0.8380 31.549
{waatc3 106.0 -o.9 0.9 0.21 o.a3ao 29-4/[7 nl. nl"
GP043AS-036892-RT- 1 789 Page 72 of 195
Low Load Run S2
l,oetlo.: Hunld 3
Lo.d (MWl: 186
D.tG: Lll2Ol2O24
St rt 1m.: 8r3/i
tnd Tlm: t:54
Probe / Gas Data
Adjusted Results
avd: 28.25 nlwqsw: t9,8O5,887 rnflhr
Prob.ll REi o dttr4s
P.ob! 12 R@: 0 daaret
Prob.rl Rao: -01 d.trer
Prcba 12 Rlo: -1.t d.trei
8$: o.09a9 tall(x,
Mdr 29.t8 lb/lb-molc
M,: 2t.75 lb/lEmol.
Pe: 24.76 ln Ht
P.: -5.50 l6HrO
P.: 2a.36 lnH!
%COr: 95 r(rc,r------!9xtaCO: 0.0 X
al.s t6
Flow RATA Traverse Data
Polnt lO Prcb.lO
Cortctad
St.d Tmp Y.w &[1. Y.u AntL
lFl td.tl o.ld..l
P1.P2
aln H.ol
Uradlurd R.demht Polnt UFd I WAF
Arl.l Vcleltv Arl.l V.lclty lor Polnts
v- (ft/*.l v. tftlsl wAF? uEdc
001 2 106 2 -0.2 o 14 o_a3a 24.44
m2 2 105 -2 o.2 0.20 0.8380 28.803
003 1m I 0.8 0.21 0.8380 29.512 nlz
0(N 106 0 18 o.23 0.8380 30-873
005 2 106 1.8 0.15 0.E3EO ?4.932
005 2 106 0.8 0.20 o.83&)2a_m1
007 106 0.8 o23 o.8380 30_8a5
008 2 106 0.8 0.23 0.8380 30.88s
009 106 o.8 0.15 0.83E0 24.942 nla
010 106 o o.20 0.8380 28.801
011 2 106 0.8 0.20 0.8380 28.801
o12 106 0 1.8 o.25 o.a3ao 32.187
013 2 106 o8 0.13 0.a3ao 21.220
014 2 106 .0.2 0.20 o atao 28.803
o15 2 106 0.8 o.2l 0.83E0 29.512 nla
016 2 106 o.8 o_74 o.a3m 11.549 nla
lEEtcs 105.0 -1.0 0.6 0.20 o.a3a0 24.534 nla nla
GP043AS-036892-RT- 1 789 Page 73 of 195
Low Load Run S3
ldatloo: Hunla, 3
Lo.d (MW)r 184
OdG: Lll2ol2o24
St.rtllme: 9:08
End ImGi 9:2E
Probe / Gas Data
Prob. tl RD:
Proba 12 Re:
Probe 11 ns:
Probc 12 RsLo:
o datres
O dctract
-{rl d!!r.ci
.1.8 d.t@t
8r.: 0.09a9 X/lm
tr4: 29.8t lb/b.hoh
M,: 2t.75 lb/lb.mol.
Pb,: 2'1.76 ln Ht
P.: -5.q, lnHro
P,: 21.36 In H!
,aCOr: 95 9a
XOi: 9.o t6
)aco, 0.0 f
81.5 r
Flow RATA Traverse Data
Polnl lD hb.lD
Corrd.d
St.d( Tmp Yaw &r3lr Y.r AntL Pl-Pz
lIl ld..l o. lddl lln HJI
Unrdlurt.d R.pl*m.nt Polnt Utad , WAF
ArLl VGlelty Adal VGl,o.lg lor Pohts
v- artlecl v- lft/ql wAF? UsdC
001 106 -l 0.8 0.13 0.838 23.220
m2 2 106 I 0.8 0.19 0.83E0 24.071 nla
m3 2 tG -1 o.8 o.21 o.a3m 29.512
004 2 t06 oa o?)o a3ao 30-206
005 2 106 0.8 0.16 0.8380 75.7@
ffi 2 106 0 .8 o.20 0.E3EO 2E.769
oo7 2 106 o 1_8 o.21 o_a3ao 29.500 nla
008 2 106 0 .8 o.2x 0.8380 30.873
009 2 106 o .8 o.14 0.8380 24,O47
010 1 106 0 .8 0.20 0.8380 28.749
011 2 106 0.a o.21 o_alao 29.512 nla
012 2 r06 .1 0.8 0.23 0.8160 30 s5
013 2 106 1 0.8 0.18 0.83E0 27.323 nla
o1a )105 .1 0.8 0.20 0.8380 28.801 nla
015 2 l05 oa o77 o atm 30.206
015 2 106 .1 0.8 o.24 0.8380 31.549
{veLaas 105.0 4,1 1.1 0.20 0.8380 28.s68 nla nla
GP043AS-036892-RT- 1789 Page 74 of L95
Low Load Run #4
Ldtion: Huhtti 3
Ldd (MWl: lEs
D*.r l,.l2ol7024
Strrl Tlm.: 9:43
EndTlma: lor03
Probe / Gas Data
Piobc 11 Re: 0 drt@5
ProbG 12 Re: 0 d4ret
Prob€ tl qro: il dctret
Prcb.12 Rsro: -1.t d.aretg-,-------6.6vroo
M.: 29.tt lb/lFmol.
M.: 28.rS lbflEdol.
Pb,: 2il.r6 lnH!
P.: .3.50 lnHro
P,r 2i1.35 lnHt
t6COr: 9.5 f
&r'-----------!9*
taCO: 0.0 t6
t1.5 ta
Flow RATA Traverse Data
Poinl lD Prob. lO
Coractad
St.clT.mp YawAnd. Y.wAnd. P1-P2
lFl (ddl (L lddl lln H,o)
Uhrdlu*.d R€plemcnt Polnt Usd t WAF
Arl.lv.ldlty Ant lvcloctty ,or Polnts
v. (fv*rl v. (ft/Gl wAF? u*dc-
001 2 106 0.8 0.12 0.838 22.309 nla
002 2 l05 o.8 o.1a o.8380 27.323 ila ila
m?2 106 .1 0.8 0.21 0.8380 2q s12
(xX 2 1ffi I 0.8 o.22 0.8380 30.206 nla nlz
005 2 106 o8 o.16 0.8380 24.G)5 nla
M 2 105 .1 0.8 0.18 0.8380 27.323
007 2 1(r I 0.8 0.20 0.8380 28.801
008 2 106 0.8 o.22 0.834O 30.206
009 2 106 -1 0.8 0.14 0.8380 24.095
010 106 0.8 0.20 0.8380 28.801
011 2 106 1.8 o.23 0.6380 30.873
012 2 106 .1 0.8 0.23 o.a?ao 30_95
013 2 106 0 1.8 0.15 0.8380 24.932 nla nla
014 2 106 o8 o 21 0.8380 29.512 nla
o15 2 105 -L 0.8 o.22 o atm m2m
015 106 -1 0.8 o.22 0.8380 30.206 nla
lrcnt6 106.0 {.9 0,9 0.19 0.8380 28.080 nl. nla
GP043AS-036892-RT- 1789 Page 75 of 195
Low Load Run #5
Lqtlon: Hunlar 3
lo.d (MW)r 184
D.te: L,.lzOlZO2[
srn nm.: 10:17
End nm.: 10:37
Probe / Gas Data
Page 76 of 195
Probc fl R@:
P@b.12 RM:
Prob. t1 Rao:
Proba 12 RsLo:
0 d.trer
---------id.t*t{.1 d.trer
-1.8 d.tr.Gt
B$: 0.0949 X/loo
M;: 29.88 lblb-.molc
M,: 2t.75 lb/EmoL
P!: 2i1.76 ln Ht
P.: -5.50 ln HrO
P,: 2a.t6 ln H8
tacor: 9.5 X
xor: ------------!qxXCO: 0.0 x
E1.5 r
Flow RATA Traverse Data
Polnt lD P.obc lD
Co.rdcd
St.ctl.mp YawAaal. Y.wAnal,. Pl-P2(rl ldcrl Q. (d{} lln H,0}
Un.djun.d Rcplemnt Poirt Urcd I wAF
AIl.1 V.lcity Axl.l Vcloclty fo. Polnts
v. (ftlr.c) v. (ltls) waF? us.dc-
001 2 106 I 0.8 0.15 0.838 24.942
m2 2 1G 1 o.8 o.1a o.8380 27.323
oo3 2 106 0 1.8 o.21 0.8380 29 5m
oo4 2 105 I 0.8 o.22 0.8380 30.206
oo5 2 105 1 0.8 o.14 0.E380 24.095
006 2 106 "1 o.8 o_77 o.8t80 26.553
007 2 106 I 0.8 o.20 0.8380 28.tO
008 2 106 I 0.8 o.22 0.8380 30.206
m 2 106 1 0.8 0.16 0.8380 25.160
010 2 106 "1 0.8 o.20 o.8380 28.EO'
011 2 105 0.8 o.22 0.E3E0 30.206
012 2 105 0.8 0.23 0.8380 30.885
01?2 106 o.8 o.14 0.8380 24.V)6 nla
014 2 106 0.8 0.19 o a3ao 24.O7'
015 2 106 1.8 o.22 0.8380 30.194
o16 2 106 0.8 o.72.0.8380 30.206
lrcta8t5 106.0 -{t.9 0.9 0.19 ot3ao 28.115 nlz ila
GP043AS-036892-RT- 1 789
Low Load Run #5
lootion: Hunt!.3
lo.d (MWl: l8/t
D&: lu2ol2o21
St rtTln.: 10:52
End Tlm: 11:12
Probe / Gas Data
Prcba Il R@: o d.tret
Prob. t2 Re: o dra@r
Proba tl iao: fi dearcat
Proba 12 RsLo: -1.t daaru.r
8.,: 0.0949 X/loo
Mi: 29.88 lb/lb-moL
M,: 2t.75 lblEmolc
Pb,: 24.76 ln H3
P.: -5.50 ln Hro
P.: 24.:6 lnHa
XCOa: 9J ta
XOr: 9.0 X
XCO: 0.0 t{
t1.9 X
Flow RATA Traverse Data
Pdnt lD Pmb. lD
corcctcd
st.cllcmp Y.w^r{le Y.wan3L
aFl ldr.l (L ld.rl
PI.P2
lin H,ol
Un.dFn.d Rcpl.emnt Polnl U*d I WAF
Ard.lv.h.l,ty Axhlv.lodty lor Pokn5
V- {ft/*c} v. (ft/Gl wAF? Usdc-
001 105 o.a o.14 o.818 24.095
002 106 1 0.8 o.17 o a3ao ?6.553
m3 106 '0.2 o.2o 0.83E0 28.803 nla
004 1m I o_a o.77 0.8380 30.206 nla
m5 106 1 0.E 0.15 o tlm 7^ q)
ffi 106 0 1.8 0.19 0.E3E0 28.060
007 106 o 1.8 0.20 0.8380 24.749
008 106 I 0.8 o.21 0.8380 29 S12 nla
m 105 0 1.8 0.13 0.8380 23.271
010 106 0 1.8 o-20 0.834O 24.149
011 106 0 l8 o.21 0_a3m 29.Sm
012 105 0 1.8 o.22 o.a3m 30.1q
o13 106 0 1.8 0.14 0.8380 24.O47 nla nla
014 1m -2 -0.2 o.20 o.4380 28.803
015 106 0 1A o)o afm 30. lq
o15 105 I 0.8 o.22 0.8380 30.206 nla
106.0 -0.6 t.2 0.19 0.838()27.472 nla ala
GP043AS-036892-RT- 1 789 Page 77 of 195
Low Load Run fl7
Lootlon: Huntar 3
ted (MW): 185
O.t.: lll2ol2o24
St rl Tlm.: U:26
End nru: 1l:a5
Probe / Gas Data
Pob.Il Re: 0 d.trG
Prob€ 12 Re: 0 d.aci
ProbGU Rao: {.1 dcaret
Piob. t2 RsLo: -l.t detE.
8,,: O.O9/t9 X/lm
M.: 29.88 lb/lb-mole
M,: zt.rs lb/lEmol.
Pb: 24.16 ln N!
Pr: -5.5O ln HrO
P.: 2a.35 ln h!
t(aor: 9.s X
fori 93 X
COt 0.0 96
61.5 t6
Fiow RATA Traverse Data
Polnt lD P@b. lD
Corcctad
stftl Tmp Y.w A.tlG Y.r Andc Pl-P2
lFt {d!rl o.ldnl lln H,ol
Ur.dlurt.d Repl@mni Polnt U$d t wAf
Arl.l V.lelty tulal v.lodty ior Polnts
v- lltl*.| v. lft/cl wAf ? Uedc
001 2 106 0 1.8 0.15 0.838 24.912
002 2 106 0 1.8 0.16 0.8380 25.750
ml 106 o.8 o.20 0.8380 28.801
@4 2 106 o8 o.77 o.a3m 29.5t2
005 2 106 .1 0.8 0.15 o t?m 2!.942 nla
ffi 106 -1 o.8 0.18 0.83EO 27.323
oo7 2 r06 o_8 o.21 0.8380 29.s12
008 2 106 -2 -o.7 0.22 o a3a0 30.209
009 2 106 .1 o.E 0.13 0.8380 23.220
o10 r06 o.8 0.20 0.8380 28.801
01,2 r06 0 t.a o.27 0.8380 30.194
012 2 105 .1 0.8 0.23 0.8380 30_BS nla
013 7 106 1 0.8 0.14 0.8380 24.096 nla
ol4 IG o.8 o.19 0.8380 24.07L nla
015 2 106 o8 o))o.a3m 30.205 ^la015106.1 0.8 0.23 0.8360 30 m5 nle
rcratat 106.0 {t.9 0.9 0.19 0.8380 27.959 nla nl.
GP043AS-036892-RT- 1 789 Page 78 of 195
Low Load Run #8
leatlon: Huntcr 3
load(Mlvl: lU
D.t : lu20l2024
St 'lllm.: 12101
End Tlrc: t2t2l
Probe / Gas Data
Proba ll Re: 0 dct.ea
Prob.l2 R@: 0 d.tEr
Probell R$o: -01 d.trcc.
Ptobc t2 Rsro: -13 d.tE
8..: o.(,!riag X/!Oo
M.: 29.tt lb/b-holc
M,: 2t.r5 lb/lEmolc
Pb: 24.16 in Ht
P.: -S.50 ln HrO
P,: 2a.36 ln H3
,*Or. 95 X
XOr: 9.0 X
XCOi 0.0 ta
81.5 r
Flow RATA Traverse Data
Polnt lO Prob. lD
Co.rGcttd
st.ckTcmp YlwAnd. Y.wAntlc Pl-P2
lrl lde.l o.ldal lln HJI
Unrdlurtcd Rrpliaemcnt 9olnt Usd I WAF
Arlel V.loclty Axl.l Vclo.lty fo, Polnt3
v- 4ftl*.1 v- lft/*l wAF? u$dc.
001 2 106 0.8 0.14 o 834 24 096
fiz 2 106 0.8 0.18 o.83m 27.X23
003 2 106 o.a o.20 0.8380 28.EOl
004 2 106 0.8 0.21 o.83ao 29.511
m5 2 106 0.8 0.16 0.t3t0 25.7@
005 7 106 0.8 0.18 0.8380 27.323
007 2 106 4.2 0.20 o.8380 28.803
fi)8 2 106 0.E o.21 0.8380 29.512 nla
009 2 106 0.8 0.13 0.8380 23.220
010 2 106 oa o?o o.83ao 2a.801
011 2 106 0 1.8 0.21 0.8380 29.5m
072 2 106 0 1.8 o.22 0_a3m 30.194
013 2 106 o8 o14 0.8380 24.66
014 2 106 0.8 0.20 0.8380 2a_801
o1s 2 106 -1 0.8 o.22 0.8380 30.206 nle ila
016 2 105 oa o71 0.4380 30.206
lwntcs 106.0 .o.9 0.9 0.19 0.E3m 27.U5 nla nla
GP043AS-036892-RT- 1 789 Page 79 of 195
Low Load Runll!)
l@tioni Huntar 3
Lo.d (MW): 185
D.t.; l,.l2ol2o24
St.rtllm.: 12:35
End Tim: 12:SS
Probe / Gas Data
Probc ll Re: 0 d.t@t
Prob.l2 Rr: 0 d.t.ct
Probc 11 Rs: -Ol dctl.et
Probcr2islo: .1, d.!re.
B$: 0.0949 X/tm
Md: 29.Et lbllEmole
M,: 2t.75 lb/b{olc
Pb: 2,1.76 ln Ht
P.: -5.50 ln HrO
P,: 2i1.36 ln Ht
t(COr: 95 ra
taor: 9.0 X
t(CO: 0.0 f
'(llr: 81.5 '{
Flow RATA Traverse Data
Polni lO Prob. lO
Corrdad
staclT.mp Y.wArtlc Y.wAntlc
lEl ld..l o ad,l
PL.P2
lln H-Ol
Un.dlunCd
Axl.l Vcldlty
V- lft-l*cl
lcpl.mnt Polnt U$d t waF
Axl.l V.lo.lty ior Polnts
v- lfi/Gl waf ? urcdL
m1 106 0 1.8 0.13 0.83E 21.211
002 2 106 o.8 o.17 0.a380 26.553
003 2 106 ,1 0.8 0.21 o.83ao ?9.572
004 2 106 "1 0.8 o.27 0.8380 30 ,06
ms 2 106 0.8 0.16 0.83E0 25,1@
oo6 2 105 o_8 o.20 0.8380 28.801
007 2 106 0.8 o.22 0.8380 10.206
m8 7 105 0.8 o.22 o.a380 30.206
009 2 105 0.8 0.15 0.8380 24.942
010 2 106 o_8 o.20 0.8380 28.801
011 2 106 0.8 0.20 0.8380 28.401 nla
o12 106 0.8 0.23 0.8380 30.8a5
013 2 106 0.8 0.14 0.8380 24.0116 nla nla
014 2 106 0.8 o21 0 aSao 29.512
o1s 2 106 0.8 0.21 0.8380 29 S12
o16 l05 0.8 o.22 0.8380 30.206
lrcntcs l(r.o .{1.9 0.9 0.19 o.t3t0 28.201 nla nla
GP043AS-036892-RT- 1789 Paqe 80 of 195
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Page 81 of 195
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GP043AS-035892-RT- 1 789
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GP043AS-036892-RT- 1 789
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Page 82 of 195
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GP043AS-036892-RT- 1789 Revlewed: FPM Page 8CtM95
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GP043AS-036892-RT-1 789 Pevlawpd' FPM p39s 8481t195
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GP043AS-036892-RT- 1789 Page 94 of 195
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GP043AS-036892-RT- 1 789 Page 95 of 195
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8.8 21.2 83.6 4.1 {.3
8.t 21.4 t3.6 5.5 -O.2
8.9 71.1 41.7 5.5 -O.7
t1 9:1812 9:19
13 9:20
14 9i21
15 9i22
16 9:23
t7
18
19
9:24
9:25
9126
20 9:27
21 9:2t 8.9 24.3 84.3 5.2 -O.2 21 10:03 8.8 24.1 83.8 4.s -0.1
q
c,
c-
Clrractad AErrta:
0.0 "o.2 .0.3 -3.3
0.0 0.0 -0.3 -3.4
0-0 {-l .o.3 .3.4
9.1 65.4 150.7 151.4
9,1 65.1 150.1 151.0
9.1 65.3 1SO.'r 151.2
8.9 65.0 151.4 150.5ffi
Core
q
c. ".
c-c-
Co.rGd.d Anntt:
0.0 0.0 -0.3 -3.4
0.o {.3 {.3 {.3
0.0 -{r.2 -{r.3 -t.9
9.1 65.1 150.1 151.0
9.t 65.4 150.2 150.8
9.1 55.1 1SO.2 15t.9
8.9 65.0 151.4 150.5ffi
GP043AS-036892-RT- 1 789 Page 96 of 195
Pior{r36t9l
P.clf,Corp
Hlnl.r Unh 3
,rnol2o21
T.st Run 15
St.rt Time
Run Length
Stop Iime
10:17
2l
10i37
D.ta
PR(},{36192
P..lfiCorp
Hunt.r Unh 3
11lml2or.
Tcn Run t5
St.rt Tlme
Run L.ngth
Stop Tlme
1O:52
27
11:12
D.t.Uncoarected Uncordad
Mlnd.
1
2
3
4
5
6
7
I
9
10
11
L2
13
L4
15
15
L7
18
19
20
Tlm
10r17
10ilE
10:19
10:20
10r21
LOt22
10:23
10:2tl
10:25
10:26
10:27
10:28
10:29
l0:30
10:31
10r32
10:33
10:34
10r35
10r36
cor sor I{q co Nor
*o. ppmw ppmw ppmw pPmw
8.9 22.1 83.5 2.6 -0.1
8.8 23.4 82.4 3.3 {.2
8.8 23.8 82.1 3.il -0.1
8.8 23.9 82.8 3.6 -O.2
8.9 24.4 83.4 3.7 {.2
8.8 24.6 83.4 3.2 0.0
8.t 21.1 83.1 3.2 -0.1
8.8 25.1 83.6 3.1 {.1
E.E 25.0 63.2 2.6 -O.1
t.8 24.9 84.1 1.7 .O.3
8.8 25.0 84.0 4.1 -0.2
E.8 24.a 84.1 3.O -O.1
E.E 71.a E4.3 3.2 0.0
8.8 24.4 43.7 3.0 0.0
8.8 24.4 83.8 1.0 0.1
8.8 24.2 U.6 1.9 -0.1
E.9 24.9 85.2 2.8 -0.1
t.9 24.! 83.4 2.' -0.1
8.8 24.3 82.3 2.4 -0.2
8.8 24.1 83.0 2.4 4.2
Mlnutr
1
2
3
4
5
6
?
8
9
10
11
72
1l
t4
15
16
,7
1t
l9
20
21
Ttm
10:52
10:53
10r54
10rSS
10:55
10t57
10:5E
10:59
11:00
11:01
11|02
11:03
11:04
11:05
11:06
11:07
11:08
1l:09
1l:10
11:1!
11:12
cor so, M), co lor
'6w ppmw ppffi ppnw ppnw
8.S 25.5 83.5 2.1 -0.18.8 25.2 83.3 1.2 -O.28.8 2'1.3 t3.1 L.7 -0.r.
t.8 22.5 83.5 1.0 {.28.9 22.2 84.1 L.4 -0.28.8 22.3 t3.4 2.5 4.28.8 22.7 t3.3 2.1 -0.1t.t 27.o 83.2 0.4 -0.18.8 22.a t3.7 r.7 -O.28.8 23.7 t3.8 t.t -0.1
8.8 21.2 83.8 1.4 0.0E.9 24.4 U.2 2.? 0.18.8 24.4 t4.1 1.5 -O.1
8.9 25.0 84.5 L.7 0.08.8 24.5 83.s 1.1 0.18.8 24.9 &3.6 3.3 {.28.8 24.7 83.9 1.7 4.2t.9 25.1 U.7 3.2 {.18.9 25.2 t4.9 2.0 {.18.E 2S.0 84.3 L.7 0.08.8 24.6 83.0 2.3 0.021 10:37 A.a 23.8 83.8 1.6 -0.1
AE..t! t.t 2a.3 t3.5 2.t '0.1 AEnt.
q
c.c-
Corcctrd AEntt:
qF
q
c-n
q
c*
Cor.cd AEnfr:
0.0 -0.3 {.3 -4.3
o.0 {.1 {.3 -4.7
0.0 4.2 -{r.3 4.5
9.1 65.4 150.2 150.8
9.1 A.a 1SO.0 151.2
9.1 65,1 150.1 1s1.0
E.9 55.0 151.4 150.5ffi
o.o {-1 -o.3 4.7
0.0 0.0 {.3 -6.3
0.0 {.1 .0.3 -5.5
9.1 54.E 150.0 151.2
9.1 65.0 150.1 149.E
9.1 6i1.9 150.1 15{r.5
E.9 65.0 151.4 150.5@
f,iVlSrON OF AIR Ol-lA'l ITY
GP043AS-036892-RT- 1789 Page 97 of 195
PXrr-0:r5ar2
P.cmcsp
Huntd Unlt 3
ttl2ol2oza
T.lt Run rT
Start Time
Run Length
Stop Time
11:26
21
11:46
PROJa36t92
P*mCorp
Huntcr Unlt 3
7112012021
TGt Run ,t
St.d Time
Run l-antth
Stop Time
12:01
21
12:21
Uncorreated Analyrer Oata Uncotrded Analyrer Data
Mlnd.
1
2
3
4
5
6
7
8
9
10
11
t7
13
14
15
16
11
18
19
20
21
?tm
11:26
11:21
11:28
11:29
11:30
11:31
11:32
11:33
11:34
11:35
11:35
11t37
11r38
11:39
11:ilo
11:iU
Ll142
11:43
11:44
11:45
11:il5
co, 5(), M)t co ilor
t6w pplrw ppmw ppltw ppm
8.8 24.1 83.9 r.7 -0.1
8.9 24.4 83.5 2.4 -0.1
8.9 24.7 82.5 1.6 '0.38.8 24.1 81.9 1.s {.2
E.E 24.1 42.2 1.3 -0.2
8.8 24.1 82.3 1.t 0.0
8.8 24.4 83.0 1.3 -0.1
8.8 24.4 83.4 {.4 -0.2
E.E 24.2 t3.2 0.3 -O.2
8.8 24.2 42.7 0.8 0.1
8.8 24.4 83.S 1.0 4.28.9 23.O E3.8 1.5 -0.2
E.9 22.4 E4.ir 1.5 -0.1
8.9 22.4 84.9 1.4 0.1
a.9 72.4 &.S 1.8 -O.2
8.8 22.5 83.9 0.9 -O.2
8.8 22.2 83.3 0.6 -0.1
8.8 20.9 t3.5 -0.5 -0.1
8.8 19.5 84.0 -0.5 -0.2
t.E 1E.5 t3.4 0.3 -O.2
8.7 18.0 83.2 4.7 -O.1
Mlnut.
1
2
3
4
5
6.,
8
9
10
11
L2
13
14
15
15
77
1E
19
20
21
Tlm
12:01
12iO2
12:03
12:O4
12:05
12:06
L2t07
12|08
12:09
12:10
12:11
12:12
12:13
12iL4
12:15
12:16
L2i!7
12:18
12:19
12t2O
12t2!
cor sor ro, co Nor
Xw ppliw pphw ppmw ppmw
8.8 28.5 83.0 -0.4 4.2
E.8 28.4 82.9 -0.3 0.2
E.E 28.s E3.6 -O.7 0.0
8.t 2t.9 84.1 '1.3 0.1
8.8 28.5 43.7 0.2 -0.3
8.9 28.5 U.t -0.5 0.0
8.9 28.1 43.7 -0.2 .O.1
E.t 27.4 83.0 0.4 {.1
8.8 26.6 83.2 0.0 'O-3
8.9 26.5 83.8 1.s 4.2
8.E 26.2 E3.4 1.4 -0.1
8.8 25.0 83.1 -O.2 -O.2
8.8 21.7 82.9 0.6 4.2
8.8 24.5 81.8 -0.6 0.0
8-8 24.4 82.0 0.6 0.0
8.8 23.9 82.3 0.9 0.1
8.8 23.9 82.5 0.1 -0.1
8.8 23.t 83.6 {.5 4.2
8.8 23.2 84.0 {.5 -O.2
8.8 22.9 83.6 1.3 -O.2
8.8 23.1 83.5 0.1 -0.1
AEr{.
q
c-
cD
Coractad Arcrata:
1.0 -o,l Arcrala
c.
c.
c..
CsEtrd Aar!3.:
E.E Z5.O E3.t O.t {,1
0.0 0.0 -o.3 .6.3
0.0 0.0 -0.3 -7.2
0.0 0.0 .{r.t -6.8
9.1 5S.5 149.9 149.2
9.1 U.9 149.8 144.6
9.1 6s.2 149.9 raa.9
8.9 55.0 151.4 150.5ffi
0.0 0.0 -0.3 -6.3
0.0 0.0 -0.3 -6.3
0-0 0.o -0.t 4-,
9.1 5S.0 150.1 149.8
9.1 65.5 149.9 L49.2
9.1 6s.3 tso.o 149.5
8.9 65.0 L5L.4 150.5ffi
GP043AS-036892-RT- 1 789 Page 98 of 195
Piors6tlr2
PemCqp
Hunt.r Unlt 3
ttl20l70.21
l.rt lun 19
Start Time
Run Lendh
Stop Time
12:35
2t
12:55
Uncoreded Analyler Data
Mlnd.
1
2
3
4
5
6
7
8
9
10
11
t2
13
Tlm
12:35
12:36
L2t37
12:38
12:39
12:'10
L2t4l
12t42
12:43
72:44
12:4S
12:46
L2:47
cor sor ,{o, co f,or
taw ppttw pDow ppltw ppN
8.8 2S.1 83.2 4.7 0,0
E.9 25.1 82.9 -O.2 0.0
8.E 25.1 82.E 0.4 0.0
8.8 24.5 83.3 {.il {.1
8.8 24.L 82.7 0.6 0.1
8.8 24.0 42.7 -O.7 0.1
E.9 24.3 83.5 4.4 0.0
8.9 74.'t 84.6 0.4 0.0
8.8 24.2 84.0 0.3 -0.2
8.9 24.7 84.6 {.3 4.2
8.8 24.2 E3.7 4.7 0.0
8.t 21.8 83.5 -1.0 0.O
8.9 24.2 84.9 -t.2 -O.1
8.E 24.2 83.9 -1.3 {.1
a.a 71.1 83.7 -1.8 -O.2
8.t 24.3 83.5 -1.s 0.1
t.E 23.8 83.6 -1.5 0.0
8.8 24,O 82.8 -1.4 0.1
8.8 24.L E2.8 {.8 {.2
8.8 74.2 t3.7 -0.9 {.1
14 12r4a
15 12149
16 12i50
17
1t
19
20
12:51
12tS2
12:53
12:5421 12:5s 8.8 243 E4.1 '0.5 0.0
Ac.tG t.t 2a', lB.5 '{r.6 0'0
Qr
q
q
c-
Cort(d Annac:
0.0 0.0 {.3 -7-2
o.0 -0.1 -o.4 {.6
0.0 -{r.r. {!.4 -6.9
9.1 U.9 149.8 1/18.6
9.1 e[.8 149.7 148.5
9.1 6'1.9 rag.t !tt.6
8.9 65.0 151.4 150.5ffi
GP043AS-036892-RT- 1 789 Page 99 of 195
Appendix A.4
Example Calculations
GP043AS-036892-RT- 1 789 Page 100 of 195
P.cmCorp
Huntar 3
ttlzol2024
nun t1 sempl. Calculetlons
EPA Mlthod a: Drtcmln:tlon ol Molsturo Cm@ntntlon ln St ck G.s
(rO CfR P.^ 60, Appendk A-31
P-= Pu,+(AH/13.6)
= 24.76+|'1.7h3.61. 24.89 ln, H!
T.=460+t-
= 460+54
= 51tl R
Vrartoo KrxVt
. 0.04706 x 88
= 4,14 rc{ (Eq, a-!
vd.d)= lqxYxvmxPm
T.
= 17.64 x 0.997 x 45.538 x 24.89
514
= ?a.77 d*l
B-= v*td)
(Eq. a-3)
Vxltul + VmGtd)
= 4.14
4.14 + 38.77
= 0.096 (x/lool
B- r*ur = lo{a'lu{r+c))
(8q.44)
P't'ut
= 10 8r0r.r.trrsEl(.r r l rsd[
618.55
= 58.69
Varleble Valua )Qllnlilon Utrh of Maaruramant
Pu,24.76 etric Presure an. Hg
AH 7.7 ,ressure Oiff arential across Orifi ce ln. HzO
P-24.49 \bsolut€ Pressur€ at Gas Meter in.Ht
54 Temperature at Gas Meter .F
T.s14 \bslute Temperature at Gas Meter .R
K1 0.04706 :onversion Factor ft3/mL
88.0 /olume of Water Condensed t
4.14 /olume of Water condensed scf
l(.17.64 :onstant 'R/in.Ht
o.9970 vleter Calibration Factor Unitless
45.538 /olume of Stack Gas Collected dcf
38.77 ;amole Gas Volume dscf
B*0.o95 ;tack Gas Moisture Content vohN
t,105 itack Temperature .F
tr 41.1 itack Temperature 'c
P.-5.50 ;tack Static Pressur€in. H2O
P.t.ut 24.36 lbsolute Stack Pressure in- He
P 618.56 \bsolute Stack Pressure mm Hg
A 8.10765 :onstant mm Ht
B 1750.286 :onstant mm Hc
c 235 :onstant "c
0.095 hturated Stack Gas Moistur€ Content *lLco
GP043AS-036892-RT- 1 789
= 0.0!ts (x/10O1
Page 101 of 195
Cllcnt
Source
Date
Run 3
P.ciflcorp
Hunter 3
ttl2ol2024
I @ Low Load
variable valuG )cfinition Unlt of Measurement
%cor 9.5 :oncentration of Carbon Dioxide Dry Volume Percent (%vd)
%ot 9 :oncentration of OxySen Dry Volume Percent (%vd)
Md 29.88 )ry Molecular Weight of the Stack Gas lbllb-mole
B*,0.095 ;tack Gas Moisture Content % H2O / 100
M,28.75 \ctual Molecular Wei8ht of the Stack Gas lb/lb-mole
24.76 larometric Pressure in. Hg
P 5.50 itack Static Pressure in. H2O
P,24.16 \bsolute Stack Pressure in. Hs
trt 106 ;tack Temperature at Traverse Point i .F
T 566 \bsolute Stack Temperature at Traverse Point i .R
Kp 8S.49 lonversion Factor (ft/sec) x v(((lbllb-moleXin.Hs))/(('RXin.Hro)))
APr 0.16 )ifferential Pressure of Stack Gas at Traverse Point i in. HzO
cp 0.838 )itot Tube Calibration Coefficient Dimensionless
€vlt 1 vleasured Yaw Angle of Flow Velocity at Traverse Point i deSrees
Rlo 1.8 I Scribe Line Offset of Probe degrees
9vnt 0.8 :orrected Yaw Angle at Traverse Point i degrees
25.760 ;tack Gas Axial Velcity at Traverse Point i ft/sec
29.447 \veraSe Stack Gas Axial Velocity Across All Traverse Points ft/sec
s1s.389 :ross-sectional Area of the Stack ft2
T'ra 528 itandard Absolute Temperature .R
T 106.0 \vera8e Stack T€mperature Across All Traverse Points .F
T 566.0 \verage Absolute Stack Temperature Across All Traverse Points .R
P,r 29.92 itandard Absolute Pressure in, Hg
WAF 0.99 ,Vall Etfects Factor from EPA Method 2H (1.0 if not used)Dimensionless
o.,47,O74,53L \verace Wet-8asis Volumetric stack Flow Rate Corrected to Standard Conditions wscf/hr
a"-37,t77,723 \veraSe Dry-Basis Volumetric Stack Flow Rate Corrected to Standard Conditions dscf/hr
GP043AS-036892-RT- 1789 Page 102 of 195
PaclfiCoe: Hunt.r 3
EPA Method 2G Samplc Calculatlons
Run t1 e Lfl [oad, s.mpla Polnt 1 (1u20l2o24]
Md = (0.44 x 96CO2) + (0.32 x %OJ + 0.28(100-%CO2-%O2)
= (0.'14 x 9.5) + (0.32 x 9) + 0.28(10G9.5-9)
= 29.881b/lEmolc
M.= Mox(l-B.J + (18.0x 8*)
= 29.88 x (1 - 0.09s) + (18.0 x 0.095)
= 28.7s lb/lb-mole (Eq.2c-21
P.= Pb,+(P/13.5)
" 24.76 + (-s.s/13.6)
= 24.36 in. Ht
Td:450+tr
: 460 +106
=556R
(Eq.2G-3)
(Eq.2G-s)
V*n =lqxCpx
85-49 x O-84 x
x (cose6)
x (cos 0.8)
= 25.750|Vs
ad: 3500 x (v.(-d) x (A) x
= 3600 x (29.447) x (s15.39) x
= l1,O7tl,531scf/hr
Qd=q.'x(1-Bs)
. 41,074,531 x (1 -0.0949)
= l7,l77,l,2ldsctlhr
(Eq.2G-6)
(Tnd x Pi)
[Tsh"dxPdd] XWAF
(528 x 24.36)(566x29.92) x0.99
(Eq.2G-e)
(Aplr x T,lp
(P, x M.)
(0.16 x 5661
GP043AS-036892-RT- 1 789 Page 103 of 195
PftmCorp
Hunter Unlt 3
ttl2012024.
Run tl $mplc C.lel.tlffi
EPA M.thod 3A: DetGmlnrtlon of Orytan .nd C.rbon Oloxlda Conc.ntntlon3 In Emlsslons trom St.tlonrry Sourcls
llnstrumcnt l An.lyrcr Prcccdurcl
(aO CfR P.rt 50, AppGndk A-21
CF. (c.r - co) x cm.
(c,-q)
= (8.4 - 0) x 8.944
(e.1 - 0)
= 8.3Xw (Eq.7E-sb)
V.d.bL VrlI )cflnltlm
cM 8.4 \verate Unadjusted Gas Concentration %w
q 0.0 \verage Pre/Post Zero Gas Response %w
c-.8.9 :oncentratlon of Upscale Callbration Gas
cm 9.:vera8e Pre/Post Upscale Gas Repons€.t$w
cr.8.3 Nerage Gas Concentration Adjusted for Bias %w
GP043AS-036892-RT- 1 789 Page 104 of 195
Pecmcorp
Hunter Unh 3
tllz0l202a
Run lfl Sample c.lculatlons
EPA Mctlrod 5C: Octrmln.tlon of Sulfui Dloxld. Emlsslons ftom St tlonary Sourccs
(lnatrumcnt l Anaiyrer PmGduitl
(/ut CFR Part 60, Appcndh A4l
c--Co) x C*
(c. - c{}
(21.37s - (-0.1)) x 55.02
(6s.2s - (4.1))
= 21.4 ppmw
= 3.55E{5 lb/scf
Erym= (c-)(FJ (100)
(cO2t6w)
(3.ssE-05) (1800) (100)
(8.3)
= 0.077|b/mmBtu
tryr= (c.l (q*6)
= (3.ssE{6) (41,07a,s31}
= r4s.9 lb/hr
(Eq.19-7)
VarlaUc vrlu.,.ffnltl6
C.o 2t_4 Vera8e Unadiusted Gas Concentration ppmw
q {.1 verate Pre/Post zero Gas Resoonse ppmw
c-65.0 :oncentration of Upscale Calibration Gas ppm
c.6s.3 \veraSe Pre/Post Upscale Gas Reponse ppmw
c*2L.4 \verate Gas Concentratlon Adiusted for Bias ppmw
MW 64.06 vlolecular Welqht lb/lb-mole
385.3 385.3 /olume of One Pound of ldeal Gas at Standard Conditlons scfllb-mole
F,18m tactor from EPA Method 19 scf/mmBtu
c*3.55E-O5 ,ollutant Concentration, Wet Basis pound/wet standard cubic foot
CO296w 8.3 :Ol Concentration wet volume percenl
E57..au o.o77 :mission Rate pounds p.r million British thermal units
a*d 41.074.531 :xhaust tlow Rate (From EPA Method 2F)wet standard cubic feet per hour
Eu^,145.9 :mission Rate pounds Per hour
GP043AS-036892-RT- 1 789 Page 105 of 195
PicMCorp
Hunter Unlt 3
ttl20l2024
Run ,l Sample C.lcul.tlons
EPA Method 7E: Datemln.tlon of t{ltro3ln Oxldrs Emlsrlons from St.tlonary Soures
(lnstrumental Analyzor Procedurel
(40 CFR Part 60, AppGndix A{}
(C.r-ColxC.,
(c, - co)
= (88.2212s - (-0.25)) x 151.4
(1so.s - (-0.2s))
= 88.9 ppmw (Eq. 7E-sb)
= 1.06E-0s lblscf
ED/nhau=(c*) (F") (10o)
(COz%w)
(1.06E{s} (1800) (100}
(8.3)
= 0.231|b/mmBtu
Eryr= (C") (O*"n)
= (1.068-0s) (4r,074,s3r)
= t135,8 lblhr
(Eq.19-7)
V.rleblc Valu!).flnltlon Unlt of Mcasurcmant
88.2 \veraSe Unadjusted Gas Concentration ppmw
q -0.3 Werage Pre/Post Zero Gas Response ppmw
C."151.4 loncentration of Upscale Calibration Gas ppm
c-150-5 \verage Pre/Post Ups@le Gas Reponse ppmvw
c..,88.9 \veraSe Gas Concentratlon Adjusted for Bias ppmvw
MW 46.01 ilolecular Weirht lb/lb-mole
385.3 385.3 /olume ofOne Pound of ldeal Gas at Standard Conditions scfllb-mole
t 1800 Factor from EPA Method 19 scf/mmBtu
c*1.06E{5 ,ollutant Concentration, Wet Basis pounds p€r standaid cubic (oot
COa 96w 8.3 :Or Concentration wet volume percent
Erb/hnBro 0.231 imirsion Rate pounds per million British thermal units
A*s 47,074,511 :xhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
Eon,43s.8 :mission Rate pounds per hour
GP043AS-036892-RT- 1789 Page 106 of 195
l
PaclffCorp
Huntar Unlt 3
t,.l2ol2024
Run tl s.mplc c.lcul.tlons
EPA Mcthod 10: D.tcmln.tlon of Carbon Monoilde Emlsslons from Stetlonery SourG
(lnnrumGrn.l Analyrcr Prccdurcl
(tlo cFR Part 60, AppGndL A{l
Cr.= (C- - Q) x C*
(c'-q)
= 12.952 - t-1)l x 150.5
(1s1.7 - (-1))
= 3.9ppmw (Eq. 7E-Sb)
C*=(c*)(Mw)
(101 (38s.3)
= 2.t3E-O7 lb/scf
Etl.,ro'(c.) (Fc) (100)
(COr96w)
12.83E471 118001(1ml
(8.3)
= 0.006lb/mm8tu
e:,n= (c.) (A"ml
= (2.83E-07) (41,074,531)
= 11.6 lb/hr
(Eq.1e-7)
vrrl.bla V.lus )Gflnltlon Unlt of Mersnm6t
Qq 3.0 \veraSe Unadjusted Gas Concentration ppmw
q -1.0 \verate Pre/Post zero Gas Response ppmw
c*150.5 :oncentration of Upscale Calibration Gas ppm
c-151.7 \verage PrelPost Upscale Gas Reponse ppmw
,.9 UeEEe Gas Concentratlon Adiusted for Bias ppmw
MW 28.O1 lbllb-mole
385.3 38S.3 /olume of one Pound of ldeal Gas at Standard Conditions scfllb.mole
F,1800 Fador from EPA Method 19 scr/mmBtu
c"2.838-07 ,ollutant Concentration, Wet Basis pounds p€r standard cubic f@t
cO2%w 8.3 :O, Concentration wet volume percent
Erumm&!0.006 :mission Rate pounds per million British thermalunits
Q*m 4t,o74,53r :xhaust Flow Rate (from EPA Method 2F)wet standard cubic feet per hour
Ern,11.6 Rate pounds per hour
GP043AS-036892 -RT- 1 789 Page 107 of 195
P.cmCorp
Hunter Unlt 3
ttl20l2o2r
Rclatlw Accuracy TGst Audlt S.mple Calculatlons
No, (lb/mmBtu)
Run,d1
I
2
3
4
5
6
7
8
9
10
11
t2
0.231 0.238
0.219 0.223
0.210 0.215
0.211 0.215
0.209 0.213
0.210 0.214
0.209 0.214
0.2(B 0.274
0.210 0.2t4
-0.007 0.00005
-0.004 0.00002
-0.005 0.00003
-0.004 0.00002
-0.004 0.00002-o.o(x o.o(m2
-0.00s 0.00003{.005 0.00003-0.004 0.00002
Av.rat. 0.213 0.218sum nla alaSumr nla nle
-o.005
{r.042
0.qr18
0.0q,o2
0.00020
nla
= 0.001
CC=(h.ors) sd
Vn
(2.306) (0.001)
= 0.0O1
M=J3J!9!-- 11661RM
= 0.005 + 0.001 tloot0.213
= 2.5%
rdi 0.00020 ium of the squared Differences
IIdJ'0.@18 iouare of the Summed Differences
n 9 {umber of Test Runs
sd 0.001 itandard Deviation of Differences
to.ors 2.306 l'-value from Ps2, Table 2-1
cc o.ool 1.596 confidence coefficient
dt o.m5 \bsolute Averare Difference
lcc 0.001 \bsolute Confl dence Coeff icient
RM 0.213 Werate RM value
RA 2.6%lelatlve Accuracy
GP043AS-036892 -RT- 1 789 Page 108 of 195
Appendix B
Facility Process Data
Appendix 8.1
Unit 3
Appendix 8.1.1
High-Load Flow RATA
Average Data - High Flow Run 1
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:00 Through 1111912024 12:O5
Source
11119124 24.573 M,433,490.7 I,437.0 1 r3.19
11119t?4 24.574 8.8 I 64.463,607.0 1 13.14 447
11119t?4 24.575 64,669,143.8 1,442.2 113.21
11119124 12:03 24.574 12.1 64,554,581.9 1 r3.32
64.172.767.1 't,431.3 '113.25 445
'11119124 12:05 64,1 10,596.4 1,430.'l 11532
Average
Minimum
Maximum
Summation
Geometric M6an
lncludod Data Points
Total number of Data
P^i^rG
24.574
24.573
24.575
147.444
12.2
12.1
'12.3
48.9
64,400,697.8
64,1 10,596.4
64,669,143.8
386.404.186.9
1,436.4
1,430.1
1,442.2
8.618.1
113.24
113.'14
I 13.32
679.43
446
445
449
2.677
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: tl,lL9l24 12'22
GP043AS-036892- RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNtT3
BARPRESS
/INHA\
co2
/onT\
FLOWSCFH
/c^EHl
STKFLOW
/rQ^trtrt
STKTEMP
/ntraE\
UNttLOAD
Page 112 of 195
Average Data - High Flow Run 2
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:07 Through 1111912024 12:12
'11119124 12:07 24.573 64.022.599.3 1,427.3 112.98
11t19n4 24.574 12.3 63,774,814.7 1 13.07
11119124 12:09 24.575 64.034.232.6 1,424.2 1 13.29
11119124 12:10 il.291.251.2 '1,4u.2 113.38
11119124 12:11 24.577 't2.3 64,567,471.1 1,440.8 1 13.60
11119124 12:12 24.577 12.3 64,642,381.7 1,.143.1
Avorag€
Minimum
Maximum
Summation
Geom€tric Mean
lncluded Oata Points
Total numbor of Daia
P^i^tc
24.575
24.573
24.577
147.452
12.3
12.3
12.3
73.8
u,222,125.1
63,774,814.7
64,U2,3a1.7
385,332,750.6
1,432.6
1,422.0
1,443.1
8,595.6
'113.36
112.98
113.85
680.17
448
446
449
2.685
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: LtlL9l24 L2:23
cP043AS-036892-RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
IINIIGT
co2
/D'lTI
FLOWSCFH
rSCFH)
STKFLOW
(KSCFM)
STKTEMP
TDtrGFI
UNTTLOAD
Page 113 of 195
Source
11119124 12:'14 24.577
Average Data - High Flow Run 3
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:14 Through 1111912024 12:19
12.3 u.373.236.4 1.437.4 t'13.97 446
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(rNHG)
co2
(Pcr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNlTLOAD
(tfw)
11119124 12:15 24.576 12.3 il,597,274.5 1.441.4 1 I 3.73
11119124 12:16 24.576 12.3 64,574,06.2.7 't,441.2 113.70 445
11119124 12:17 12.2 64,260,776.9 1.434.0 113.62 445
11119124 12:'18 24.575 12.2 64,169,578.8 1,431.9 113.56 445
't1t'19124 12:',19 24.576 12.2 u.45/..743.2 113.54 446
Averago
Minimum
Maximum
Summation
Geomelrlc Mean
lncluded Data Points
Total number of Data
P^i^lc
24.576
24.575
24.577
147.456
12.3
12.2
12.3
73.5
1,437.4
r,431 .9
1,441.8
8.624.5
1 13.69
1 13.54
1 13.97
682.12
/146
445
446
2.673
u,404,945.4
64,169,578.8
u,597,274.5
386.429.672.5
C = Calibration
S = Substituted
* = Suspect
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: t7lt9/24 t2:23
GP043AS-036892-RT- 1789 Page 114 of 195
Average Data - High Flow Run 4
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:28 Through 1111912024 12:33
Source
'11119124 12:28 24.569 12.3 u,561,282.2 1,439.7 113.03 446
11119124 12:29 24.571 't2.3 u.475.487.3 1.438.8 113.48
11119124 12:30 24.569 12.3 64, 1 88,328.0 1,433.4 113.81 449
11119124 12:31 24.568 771 64.365,392.0 1,437.9 1 14.06
11119124 12:32 24.569 u,672,723.E 113.97 449
11119124 12:33 24.572 12.2 64,584,621.8 1,442.'.1 113_83
Average
Minimum
Maxirum
Summation
Geomeiric Mean
lncludod Data Points
Total numbor of Data
9^i^tc
24.570
?4.*8
24.572
147.418
12.3
12.2
't2.3
49.1
64,474,639.2
64,188,328.0
64,672,723.8
386.847.83s.1
't,439.4
1.433.4
1,444.4
8,636.s
't 13.70
113.03
1'14.06
682.18
448
446
449
2,688
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: lL/L9/24 12:49
GP043AS-036892-RT- 1 789
C = Calibratlon
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UN'T3
BARPRESS
(INHG)
co2
(Pcr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(tvlVV)
Page 115 of 195
Average Data - High Flow Run 5
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:35 Through 1111912024 12:40
11119124 12:35 24.574 64,645,984.7 1,442.6 1 13.54
11119124 12:36 24.574 64.558.809.6 1.440.3 113.40 447
11119124 12:37 u,455,247.8 1,437 .7 113.26
11t'19124 64.184.735.0 r,431 .6 113.20 447
1'1119121 12:39 24.57?64,281,01 7.3 1,433.8 113.25
11119124 24.573 64.459.378.8 1,437.9 113.32
Av€rage
Minimum
Maximum
Summation
Geomstric Mean
lncluded Data Points
Total numb€r of Data
hi6t.
24.573
24.572
24.574
147.437
12.2
12.2
12.2
73.2
64,430,862.2
64,rM,735.0
64,il5,984.7
386,585,173.2
't,437.3
1 ,431.6
1,442.6
8,623.9
113.33
113.20
1 13.54
679.97
u7
447
448
2.6U
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 7t/79/24 12:50
GP043AS-036892-RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(rNHG)
co2
(Pcr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNII LUAU
(lvfw)
Page 116 of 195
Average Data - High Flow Run 6
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period : 1 1 I 1 I I 2024 1 2:42 T hr ough 1 I I 1 9 I 2024 1 2:47
Source
'11119124 12:42 24.57'l 12.2 64,331,063.0 '113.40
11119124 12:43 24.570 12.3 64.614,647.3 1 ,441.8 113.43
11119124 12:U 24.570 12.3 64,863,182.3 1,447.5 447
11119124 12:45 24.570 04,689,855.0 1,444.2 '113.68
11119124 12:46 24.570 12.3 04,819.391.4 1.447.9 '114.00
1'll1Sl24 12:47 24.570 12.2 65,245,482.4 1,457.8 111.17
Avsrage
Minimum
Maximum
Summation
Geometric MBan
lncludod Data Points
Tolal number of Data
O^ihrc
24.570
24.570
24.571
147.42'.1
12.3
12.2
12.3
73.6
64,760,603.6
64.331.063.0
65,245,482.4
388,563,621.4
1,445.8
1,435.4
1,457.8
8,674.6
1 13.69
1'13.40
114.17
682.17
447
446
449
2,681
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: lL/79124 t2:50
GP043AS-036892-RT- 1 789
C = Calibratlon
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UN]T3
BARPRESS
(rNHG)
v9z
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNlTLOAD
(tvfw)
Page 117 of 195
Average Data - High Flow Run 7
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1111912024 12:49 Through 1111912024 12:54
Source
11119t24 12:49 24.569 12.2 65,079,382.0 t,455.5 114_69
11119124 l2:50 24-5?2 12.2 64,952,687.3 1.453.5 't15.08 449
11119124 1215'l 24.571 12.2 64,744,098.s 1,448.3 't 14.85 448
11115124 24.572 't2.2 64,U7,441.7 1,445.2 114.52
1'lt't9t24 12:53 24.574 12.2 64,U1,759.7 't,448.E 114.27 ua
11119124 12:54 24.573 12.2 64.846.785.7 1,448.2 1 13.96
Average
Minimum
Maximm
Summation
Geometric Mean
lncludod Data Points
fotal number of Data
hi.t<
24.572
24.569
24.574
'147.431
't2.2
12.2
12.2
73.2
64,852,025.6
u,u7,441.7
65,079,382.0
389,1 12,153.9
1,449.9
1,445.2
1,455.5
8.699.5
1 14.56
1 13.96
I 15.08
687.37
448
446
449
2,686
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generate d: lL/ L9 / 24 f3:.Lt
GP043AS-036892-RT- 1789
C = Callbration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(rNHG)
co2
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNII L(,AU
(lvfw)
Page 118 of 195
Average Data - High Flow Run 8
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202412:56 Through 1111912024 13:01
Source
11119124 12:56
-fnga
- 12'.5?-
24.572 12.2 64.,147.019.0 1,438.8 113.74 447
24.570 12.2 u,221,939.4 1.433.6 113.62 447
11119124 12:58 24.572 '12.2 il,274,175.3 1,433.9 1 13.34 448
11119124 12:59 24.572 12.3 M.33t.130.5 1.435.5 113.48 449
11115124 13:00 24.569 12.3 64,296,523.3 1,435.4 113.70 ,149
111'19124 13:01 24.569 9.0 I 64,1 85,551.5 1.432.6 113.53 450
Average
Minimum
Maximum
Summation
Gsom€tric Moan
lncluded Data Points
Total number of Data
9^i6t.
24.571
24.569
24.572
't47.424
12.2
12.2
12.3
61.2
u,29?,723.2
64,1 85,551.5
64,447,019.0
385,756,339.0
1,435.0
1,432.6
1,438.8
8,609.8
1 13.57
1 13.34
113.74
68'1.41
448
447
450
2.689
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Contro!
Report Generated: tll19/24 73:!1
GP043AS-036892-RT- 1789
C = Calibration
S = Substituted
r = Suspect
Time Online Criteria: 1 minute(s)
UN]T3
BARPRESS
rINHG}
c02
(PCTI
FLOWSCFH
ISCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(tYtVV)
Page 119 of 195
Source
11119t24 13:03 24.570
Average Data - High Flow Run 9
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202413:03 Through 1111912024 13:08
64,s82,953.9 't.440.1 1 13.03
11119124 13:04 24.570 12.3 64.431.141.5 1,437.2 1'13.20
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(NHG)
voz
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UN]TLOAD
(tfW)
-11,Jg24 13..05 ---' 2+5?O 64,O12,528.2 1,428.4 1 13.43
11119124 '13:06 24.570 12.3 63,807,1 06.3 1,424.3 't 13.65
't1t19t24 '13:07 24.571 63,738,'146.3 1.423.9 1 14.10
't1t't9t24 13:08 24.571 63,460,752.2 1,4',18.7 114.52
Average
Minimum
Maimum
Summation
Geomelrlc Mean
lncluded Data Points
Total number of Oata
P^i^lc
24.570
24.570
24.571
147.422
12.3
12.2
12.4
73.9
1,428.8
1,418.7
1,440.1
8,572.6
't'13.65
1t3.03
114.52
681.93
449
448
450
2,692
64,005,504.7
63,460,752.2
64,582,953.9
384.033.028.4
C = Calibration
S = Substituted
* = Suspect
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 7L/19/24 13:Ll
GP043AS-036892-RT- 1789 Page 120 of 195
Appendix B.1.2
Mid-Load Flow RATA
Average Data - Mid FIow Run 1
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202414:11 Through 1111912024 14:16
Source
11119124 14'.11 1 1.3 rC 49,663,962.2 t,107.0 't12.71 302
1'1119124 '14112 24.566 49,581,600.8 'l, 104.8 112.53
11115124 14:13 24.566 0.0 tc 49.527.846.9 1,103.5 112.49 300
11119124 14:14 0.0 lc 49,686,148.9 1.106.9 294
11119124 14:15 24.568 0.0 rc 49,495,297.6 1,102.7 112.46
111'19124 14:16 00 tc 49,329,970.8 1,100.1 113.02 293
Arerage
Minimum
Maximum
Summation
Gsom€tric M6an
lncluded Deta Points
Total numb€r of Data
g^i^lG
24.567
24.566
24.568
147.402
0.0
0.0
0.0
0.0
49,ill,471.2
49,329,970.8
49,686,1 48.9
297,2U,827.?
'1,104.2
1, r00.'l
1,107.0
6,625.0
1t2.60
112.41
113.O2
675.62
298
293
302
1.788
F = Unit Offllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated !7/79124 L4:37
GP043AS-036892-RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
,INHGI
co2
rPCTI
FLOWSCFH
/scFHt
STKFLOW
.KSCFM)
STKTEMP
{DEGFI
UNTTLOAD
(]vlvv)
Page 122 of 195
Source
'11119124 14:18 24.567 0.0 tc
Average Data - Mid Flow Run 2
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202414:18 Through 1111912024 14:23
50,028.062.6 r.1 15.7 1 13.03 296
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG}
co2
IPCTI
FLOWSCFH
lscFHl
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(tvfw)
1'1119124 14:19 24.566 00 tc 50,276,358.1 1,121.3 113.01
11119124 14:20 24.566 0.0 lc 50,143,754.5 1,118.2 112.95 298
111'19124 14:21 24.5U 0.0 lc 1 ,107.849,670,890.8 113.00 298
11119124 14:22 24.563 00lc 49.318.416.9 1,099.9 112.92 300
11119124 1.4:23 24.565 00 rc 49,293,882.8 1,099.1 112.83 30't
Average
Minimum
Maximum
Summation
Goornotric Mean
lncluded Data Points
Total number of Data
9^ihrc
24.565
24.563
24.fi7
147.391
0.0
0.0
0.0
0.0
49,788,560.9
49,293,882.8
50,276,358.1
298,731,365.7
C = Calibration
S = Substltuted
* = Suspect
1,1 10.3
1,099.1
1,12't.3
6,662.0
112.96
112.83
113.03
677.74
298
296
301
1,790
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: LLlL9l24 t4:3L
GP043AS-0 36892-RT- 1 789 Page 123 of 195
Source
Average Data - Mid Flow Run 3
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period:'l 1 l'l 91 2024 1 4 :25 Through 1'l I 1 91 2024 1 4:30
0.0 rc1',1119t24
ffgt24
49.607_373.8 1.'105.0 1 12.35 302
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG)
co2
(PCT)
rL(JWSUrn
(SCFH)
5 I I1.FL(JW
(KSCFM)
stntEMt-
(DEGF)
UNTTLOAD
(lvfw)
14126 24.570 0.3 rc |,094.749,184,282.6 1 I 1.96 301
11t19124 24.574 21lC 49,30 1,089.4 1.095.7 111.?3 30'l
1'1119124 14:28 24.576 103Ic 49,439,393.0 1,097.3 1 10.52
l1l't9124 10.7 tc 49,612,517.7 1.099.2 r09.49 301
'11119124 14:30 24.576 108 rC 49,472,476.4 1,095.6 109.26
Average
Minimum
Maximum
Summaiion
Geomotric Mean
lncludod Data Points
Total numbor of Data
P^i^1.
24.573
24.566
24.576
147.438
0.0
0.0
0.0
0.0
110.80
109.26
112.35
664.81
301
300
302
1,806
49,436,188.8
49jU,282.6
49,612,517.7
296,617,132.9
C = Gallbration
S = Substituted
t = Suspect
1,097.9
1,094.7
1,105.0
6,587.5
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: !t/L9/24 14:32
GP043AS-036892-RT- 1789 Page 124 of 195
Source
11119124 '14:58
Average Data - Mid Flow Run 4
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202414:58 Through 1111912024 15:03
10.6 lc 49,807,208.1 1,106.9 111.37
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
/ tN 1.ln \
wz
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
,reaEMt
STKTEMP
1ntrr:E\
UNTTLOAD
rMwt
11119124 14:59 24.583 10.6 C 50.012.351.5 1,108.8 110.05 298
1'.1119124 15:00 10.6 50,375,944.9 1,'t 16.6 109.92 298
11t19124 l5:01 24.583 6.9 r 49,963,572.3 1,108.4 110.40 297
11119t24 15102 24.83 49,577,807.3 1,099.1 109_98
11t19t24 15:03 24.583 50,183,001.1 1,r 10.6 109.02 299
Averago
Minimum
Maximum
Summation
Geometric Mean
lncludod Data Points
Total numbor of Data
O^i-rc
24.583
24.582
24.583
147.497
10.6
10.6
10.7
31.9
'!,108.4
1,099.1
'I,116.6
6.650.4
110.12
109.02
11',1.37
660.74
298
297
299
t.786
49,986,047.5
49,577 ,807.3
50,375,944.9
299,9't9,885.2
C = Calibration
S = Substituted
* = Suspect
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: lU!9/24 L5:77
GP043AS-036892-RT-1789 Page 125 of 195
Average Data - Mid Flow Run 5
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202415:05 Through 1111912024 15:10
Source
11119124 15:05 24.5U 10.7 50,791,735.5 t.'t27.4 1 10.76 302
11t19t24 15:06 24.586 'to.7 5',t,227,953.3 1,'138.8 1 11.60 302
11119124 24.585 10.7 51.093.945.0 1.136.2 111.82 30'l
11119t24 15:08 24.585 'to.7 50,534,308.3 1.124.3 1 12.09
11t19t24 24.585 10.7 fi.820.477.8 1,131.1 't12.31 299
11119124 15:10 10.7 51,1 39,765.8 1.138.5 't12.46 298
Avsrago
Minimum
Matmum
Summation
Geometric Msan
lncludod Data Points
Total numbor of Data
P^i^tc
24.585
24.5U
24.s86
147.511
10.7
10.7
10.7
64.2
50,934,697.6
50,534,308.3
51,227,953.3
305,608, I 85.7
1,132.7
1,124.3
't,'t 38.8
6,796.3
111.U
110.76
112.46
671.O4
300
298
302
1,80't
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: fl/L9124 !5:!8
GP043AS-036892-RT- 1 789
C = Calibratlon
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
IINHG)
co2
(PCT)
FLOWSCFH
(SCFH'I
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(lvtw)
Page 126 of 195
Average Data - Mid Flow Run 6
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202415:12 Through 1111912024 15:17
Sorrce
11t19124 15:12 10.6 51,123,542.7 1,138.3 112.49 298
11t19124 15:13 24.585 51.481.0r8.4 1.146.0 112.38 299
1'1t19t24 15'.'.14 24.584 10.5 51,468,4't 9.7 1,145.0 '112.O1 297
11119124 15:15 24.585 51.450.737.7 I,143.6 111.52 297
11119124 15:16 24.585 10.5 51,562,296.7 't,144.2 r 10.59 298
11119124 15:17 10.5 51,378,076.4 1,140.1 1 10.58
A\erage
Minimum
Maximum
Summation
Geom€tric Mean
lncluded Data Poinis
Total numbsr of Data
9^i^1.
24.585
24.5U
24.585
147.507
10.5
10.5
10.6
63.2
51,410,681.9
51,123,542.7
5r,562,296.7
308.464.091.6
1,142.9
1,1 38.3
'1,146.0
6,857.2
1 1 1.60
1 10.58
112.49
669.57
294
297
299
1,788
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 71.1 t9 / 24 L5 t79
GP043AS-036892-RT- 1 789
C = Callbration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG)
co2
(Pcr)
FLOWSCFH
(SCFH)
5 t Kl-L(JW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(lt/M/)
Page L27 of L95
Average Data - Mid Flow Run 7
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202415:19 Through 1111912024 15:24
So:rce
11119124 15:19 s1,630,810.3 1,143.6 299
'11119124 15:20 24.586 10.5 51.426.269.6 1,'t 39.4 't09.72 298
11119124 24.586 10.4 51.725.1 30.8 t,148.0 110.72 297
11t19124 15:22 24.586 52,1 57,073.8 '1,158.7 111.29
11t19124 15:23 24.588 10.4 52.500.884.5 1,166.5 1t'1.39 296
11t19124 'l.5:24 52,7s8,348.3 1,172.4 111.49 296
Awrage
Minimum
Maximum
Summation
Georn€tric Moan
lncludod Data Points
Total numb€r of Oata
9^i^rc
24.587
24.s86
24.588
147.520
10.4
10.4
10.5
62.6
52,033,086.2
5l ,426,269.6
52,758,348.3
31 2,1 98,51 7.3
'1,'t54.8
I,139.4
't,172.4
6,928.6
110.69
109.54
1 1 1.49
664_15
297
295
2gs
't,781
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: lU19l24 15:39
GP043AS-036892-RT- 1 789
C = Callbration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG)
CUZ
(PCT)
FLOWSCFH
(SCFH)
5I KTLUW
(KSCFM)
5tntEMt
(DEGF)
UNITLOAD
(t"lw)
Page 128 of 195
Average Data - Mid Flow Run 8
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202415:26 Through 1111912024 15:31
Source
11119124 15:26 24.589 53,1 26,928.1 1.181.4 11 1 .90
11119124 '15:21 52,91 9,531.0 '1.'t77.5 112.25 294
11119124 t5:28 24.589 '10.5 52,498,622.9 1,168.4 't12.38 297
11119124 15:29' 11nsrr 1i'.so -
10.4
--10A
52.393.877.6 1.166.3 112.5',1 219$
24.590 52,7'18,166.8 1.173.7 112.56 297
11119124 15:31 64 t 52.703.291.9 1,172.8 1't2.35 297
Average
Minimum
Maximum
Summation
Geomotric Msan
lncluded Data Points
Total numb€r of Datag^i^t.
24.s90
24.589
24.591
147.537
10.4
10.4
10.5
52.2
52,726,736.4
52,393,877.6
s3,126,928.1
31 6.360.41 8.3
1,173.4
1,166.3
1,181.4
7.0/,0.1
1 12.33
't 1 1.90
1 12.56
673.95
297
296
295
1,7U
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: LtlL9/24 15:39
GP043AS-036892-RT- 1789
C = Callbration
S = Substituted
| = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG)
co2
(PCT)
FLOWSCFH(scFH)
STKFLOW
IKSCFMI
STKTEMP
{DFGFI
UNITLOAD
TMW)
Page 129 of 195
Average Data - Mid Flow Run 9
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111191202415:33 Through 1111912024 15:38
Source
11119124 15:33 10.3
10,4
5 t,962,999.3 111.97
11119124 15:34
- 'r*"2a t'.as
24.59'l 52,285,556.2 1,'t62.3 1 1 1.76
10.4 52.357.81 6.3
1'1119124 15:36 24.591 10.3 52,125,270.3 111.37 301
1'1119124 15:37 10.4 52.01 0,1 25.1
11119124 '15:38 24.592 51,889,274.5 11?.01
Average
Minimum
Maximum
Summation
Geometric Mean
lncludod Data Poinis
Total number of Daia
9^i6tG
24.59',|
24.59 1
24.592
147.547
't0.4
10.3
10.4
62.2
52,1 05,1 73.6
51,889,274.s
52,357,816.3
312,631,041.7
t, t 58.1
1.154.0
1,163.0
6,948.7
1 1 1.67
111.?2
112.01
670_Ol
301
299
302
1.803
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generatedt tLhg/24 15:40
GP043AS-036892-RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(INHG)
co2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UN]TLOAD
(tfW)
Page 130 of 195
Appendix B.1.3
Low-Load Flow RATA
Average Data - Low Flow Run 1
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1112012024 07:43 Through 1112012024 08:20
Sorrcn
11120124 07:43 24_794 7.8 40.043.038.3 887.3 114.76
11120124 07'.44 24.797 7.9 40,046,459.9 113.99 'I E3
11120124 07:45 24.797 7.9 39,951,801.1 882.5 112.96
11120124 07:46 24.797 39,841,540.9 I 12.15 186
111201?4 07:47 24.757 8.2 39,738,396.4 876.0 I t 1.8't
11120124 07:48 24.798 39.702.861.3 874.3 111.21 187
11120124 07:49 ?4.798 8.3 39,086,r60.8 472.6 I 10.36 186
11120124 07:50 21_400 8.4 39,474,152.8 868.0 110.42
1'1120124 07:51 39,324,542.3 866.3 't 1'1.48 1U
1'v20124 07..52 24.801 8.4 39,520,448.9 871.5 112.06
11120124 07:53 24.801 8.4 39.662.240.9 874.7 112.11
11120124 07'.54 24.801 39,488,941.1 112.02 183
11120124 07:55 24.E01 8.4 39,562,948.2 872.3 r 12.00
11120124 07:56 24.A02 8.4 39,470,037.3 870.3 112.U
11120124 07:57 24.803 39,141 ,921.2 11 1 .97 1U
24.A04 8.5 39,182,689.9 863.4 11',t.72 183
11120124 07:59 24.803 8.5 39,445,'t00.9 868.4 1 1 1.'t6 184
11120124 08:00 24.8U 8.5 39,364,707.s 866.1 't 10.84 r83
11120124 08:0'l 8.5 39,321,948.1 865.1 110.82
11120124 0E:02 24.9U 8.5 39,454,650.0 1 10.99 183
11120124 08:03 24.806 8.5 39,288,6s6.8 804.7 't 11.10
11120124 08:04 24.806 39, r 54,703.7 86't.6 110.95 184
24.807 8.5 39.346.281.3 865_'t 110.50 1U
11120124 08:06 39,530,851.3 866.9 109.02 185
11120124 08:07 24.807 8.6 39,421,558.9 107.69 186
11120124 08:08 39.1 31.844.7 855.3 107.19
11120124 08:09 24.E11 8.6 39.157.653.2 855.7 185
11120124 08:10 8.6 39.374.064.8 860.4 107.15
11120124 08:11 24.A12 39,343,870.3 107.05 186
11120t24 08..12 24.813 39.163.198.8
24.A12 39,031,8@r.3 855.9 109.1 1 185
11120124 08;15 24.A13 38,782,295.7 850.1 108.93 186
11120124 08:'16 24.812 8.6 38,848,839.6 109.16
11120124 08:17 24.E',t1 38,888,534.3 852.4
11120124 08:18 24.411 38.803.875.9 849.8 108.34
11120124 08:19 24.812 38,804,157.1 849.2 107.96
24.813 I 107.29
M = Maintenance
T = Out Of Control
Report Generated: tLlZOl24 08:22
GP043AS-0 36892-RT- 1 789
C = Callbration
S = Substituted
t = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
tsAKT'KESIi
(INHG)
wz
(PCT)
rL(JW UUrrl
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(tfW)
11120124 08:13
8.6
u7.4
Page 132 of 195
't86
Average Data - Low Flow Run 1
Plant: HUNTER PLANT
lnterval: 1 Minute
TyPe: Block
Report Period: 1112012024 07:43 Through 1112012024 08:20
Time Online Criteria: 1 minute(s)
Average 24.405
Mininrum 24.797
MaxirYum 24.813
Summation 942.596
Geometric Moan
lncluded Data Points 38
Totel numb€r of Data 38
P^i^te
8.4 39,352,988.8
7.8 38,773,630.8
a.7 40,046,459.9
320.6 1.495.413.575.7
865.0
u7.4
887.3
32,870.2
110.31
107.12
114.76
4,191.82
185
180
187
7,021
38
38
38
38
38
38
38
38
38
38
F = Unlt Offllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated t1./2O124 08:22
GP043AS-036892-RT- 1 789
C = Callbration
S = Substituted
* = Suspect
Page 133 of 195
So:rce
Average Data - Low Flow Run 2
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1112012024 08:34 Through 1112012024 08:54
4.7 38,959,318.61112012408:34 24.816
Time Online Criteria: 1 minute(s)
UNlT3
tsAKt i{E!'S
(rNHG)
coz
(Pcr)
FLUW!iut-H
(scFH)
SI KFLUW
(KSCFM)
U I Ki EMt'
(DEGF)
UNII LL'AU
(tfW)
11120124 08:35 24.814 s.7 38,958,689.7 u8.7 105.42 185
11120t24 08:36 24.814 34.747,130.2 u4.7
1112U24 08:37 24.814 8.6 38,576,250.0 841.5 't06.r7 186
11120,124 08:38 24.a14 38,570,002.3 841.0 r86
11t20t24 08:39 24.816 8.7 38.621.769.7 841.8 105.77
11t20t24 24.418 8.7 38.676.958.8 U2.4 105.41 187
11t20t24 08:41 24.419 8.7 *,462,421.1 E37.2 105.08 186
11120124 08'.42 24.819 8.7 38.418.212.0 836.1 105.02 186
11t20124 24.8',19 4.7 38,281,389.8 833.0 104.89 186
11120124 08:44 24.819 8.7 38,038,643.7 186
'l'1120124 08:45 24.820 8.7 38,103,268.6 829.8 105.38 185
11120124 24.819 38,134,635.0 105.19 186
1'1120124 08:47 24.821 8.7 38,191,404.4
11120124 08:48 24.820 4.7 38,373,s70.8 832.5 103.24 186
11120124 08:49 38.218.622.8 827.5 102.09 186
11t20t24 08:50 24.820 8.7 38.136.399.0 825.2 101.81 186
11120121 08:51 38,203,407.1 826.7 101.81 185
11120t24 0E:52 24.421 8.E 38,038,953.6 823.0 101.72
11t20t24 24.823 8.8 38,027,519.6 822.7 101.74 1U
11120124 08:54 24.823 8.8 38,040,146.5 't8,/
Avsrago
Minimum
Maximum
Summation
Geometric Msan
lncluded Data Points
Total numbor of Data
P^lnt.
24.819
24.814
24.823
521.189
8.7
8.6
8.8
182.8
834.0
822.7
8/,8.7
17,514.4
104..27
101.72
106.r 7
2.189.60
186
'l8/.
187
3,898
38,370,414.9
38,027,519.6
38,9s9,31 8.6
805,778,713.3
C = Callbration
S = Substituted
+ = Suspect
21
21
21
21
21
21
21
21
2'l
21
21
21
F = Unlt Offllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: Lfl2O/24 O8:55
GP043AS-036892-RT- 1789 Page 134 of 195
Sorrce
11120124 09:08
Average Data - Low Flow Run 3
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1112012024 09:08 Through 1112012024 09:28
37,686,348.9 816.58.8
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
IINHGI
coz
(FCT)
FLOWSCFH
{SCFH)
STKFLOW
l](scFMl
STKTEMP
/ntraE\
UN]TLOAD
/M\
11120124 09:09 24.818 37,732,836.1 817.1 t02.18 185
11120124 09:10 8.8 37.762.948.5 817.1 101.69
11120124 09:11 24.817 816.68.9 37.767,689.1 101.31 184
11120124 09:12 8.8 37,763,272.5 816.5 10',1.29
24.820 37,645,929.1 813.9 't0't.33 184
11120124 09:14 8.9 37,640,960.9 813.7 10'1.22
815.3 101.44 184
11120124 09:16 37,590,714.6 813.6 '10't.94
102.2711120124 09:17
'11120124 09:18 24.820 8.9 37,681,609.8 816.3
11120124 09:19 24.819 1858.9 37,719,936.6 8't 7.3 102.51
11120121 09:20 24.820 8.9 37,689, r82.4 816.9 185
11120124 09:2'l 8.9 37,860,517.8 820.4 102.*184
11120124 09:22 24.820 8.9 37,848,583.7 8t 9_9 185
11120124 09:23 1858.9 37,658,2U.7 816.8 102.55
11120124 A9:24 24.820 8.9 37,666,386.3 8r6..1 102.73 185
11120124 09:25 8.9 37,U2,947.1 816.7 103.31 1U
11120124 09:26 24.8?1 37,474,111.6 8'13.7 103.77 184
11120t24 09:27 8.9 37.435.834.0 812.6
11120124 09:28 8.9 37.535.555.6 814.6 r03.45
Awragp
Mlnirrum
Maximum
Summation
G€om€trlc Mean
lncluded Data Points
Total number of Data
D^i^r.
24.820
24.817
24.821
521.215
8.9
8.8
8.9
186.5
37,668,646.2
37,435,834.0
37,860,517.8
791,U1,570.2
C = Calibration
S = Substltutedr = Suspect
815.9
812.1
820.4
17,134.0
102.34
'101.22
1$.n
2,149.13
184
184
186
3.474
21
21
21
21
21
21
21
?1
21
21
21
21
F = Unlt Offllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: LLl2Ol24 09:34
GP043AS-0 36892-RT- 1 789 Page 135 of 195
Source
Average Data - Low Flow Run 4
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1112012024 09:43 Through 111201202410:03
37,739,374.8 820.711t2012424.41?1858.9 10/.il
Time Online Criteria: 1 minute(s)
UN]T3
tIAKTKEi'5
(INHG)
vvt
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(tfW)
11120124 09:44 24.418 8.9 37.642.430.1 819.r 104.88
11t20124 09:45 37.ffi1.426.7 819.6 104.99 185
11120t24 09:46 24.819 8.9 37,778,159.2 821.7
11t20124 37,846,399.8 823.3 10{.74 184
11120124 8.909:48 24.818 37,849,167.9 1U
11120124 24.818 8.9 37,849,794.0 825.2 105.90 1U
11120124 24.818 1838.9 37.869.379.8 825.8 106.09
11t20124 1838.909:51 ?4.819 37,794,794.3
11120124 09:52 24.820 1858.9 37.766.508.4 820.5 '104.02
11t20t24 09:53 37,704,785.s 817.0 102.56 187
t1l20t?4 09:54 ?4.821 819.08.9 37.81 3.273.5 102.34
11t20t24 24_419 38.1 30.1 1 3.5 825.5 102.O7 't 85
11120124 09:56 24.818 1858.9 38.124,324.0 102.O2
11t20124 24.820 8.9 37.886.285.2 820.4 102.14
11t20124 09:58 24.819 37.620.379.0 816.1 103.19 1W
11t20t24 09:59 21.420 8.9 37,562,10s.5 817.7 105.20
11t20t24 8.9 37.s98.457.7 820.4 106.52 184
11120t24 8.8l0:01 24.521 37,61 1,313.0 106.47 1U
11t20t24 1858.8 37.491.76.7 817.9 106.35
11t201?4 8.8t0:03 24.515 37,337,306.9 gfi.7 '106.50 184
A\16rag6
Minimum
MainxJm
Summation
Geometric Mean
lncluded Oata Points
Total number of Data
O.ri^tc
24.819
24.817
24.82',1
521.203
8.9
8.8
8.9
186.6
820.9
814.7
825.8
17.238.8
104.60
102.02
106.52
2.196.63
185
183
187
3,876
37,746,550.7
37,337,306.9
38,130,1 13.5
792,677,565.5
C = Callbration
S = Substitutedt = Suspect
21
21
21
21
21
21
21
21
2'l
21
21
21
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 7Ll7O I 24 rO:O7
GP043AS-0 36892-RT- 1 789 Page 136 of 195
Average Data - Low Flow Run 5
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 111201202410;17 Through 1112012024 10:37
Source
1'll2ol24 10:17 24.821 8.9 37,573,294.3 103.0'l
11120124 10:18 8.9 38.12'1.157.'l 827.1 r03.29 1U
1'1120124 10:19 24.818 8.9 37,879,651.s 824.8 r05.30 185
11t20124 24.818 8.9 37.581.120.1 820.3 106.63
11120124 10:21 24.819 8.9 37,531,295.3 819.1 106.57 183
11t20124 21.420 8.9 37,641,668.7 821.8 106.84 1U
11120124 10:23 24.819 8.9 37,616,797.0 421.4 107.18 1U
11120t24 24.818 8.9 37,374,094.8 816.8 107.36 184
11120t24 10:25 24.818 8.9 37,496,1 1 3.5 107.48 1U
11t20t24 24.818 8.9 37,557,635.0 821.1 107.58
11120124 10:?7 21.820 8.9 37,469,'tE0.3 819.4 107.78 1E4
11120124 24.819 8.9 37,432,691.0 107.69
11120124 24.819 8.9 37,552,691.8 820.9 107.51 183
10:30 24.819 8.9 37,651,044.9 107.62
11120124 10:31 24.820 8.9 37.621,992.5 823.0 107.95 186
11120t24 10:32 24.821 8.9 37,5s0,059.0
11120124 10:33 8.9 s7.416,372.6 817.2 107.07 185
t'1t20124 10:3,4 24.822 8.9 37,316,3't 9.4 412.7 105.45
11120124 24"822 8.9 37,386,43r.5 812.3 10/..1?1U
11120124 '10:36 8.9 37,402,020.6 412.2 103.81 184
11120124 10:37 37,439,864.8 813.2 104.00 184
Avorago
Minimum
Maxifium
Summation
Geometrlc Moan
lncluded Data Points
Total numbor of Data
D^i^ta
24.820
24.818
24.823
521.218
8.9
8.9
8.9
186.9
37,567 ,214.1
37,316,319.4
38,121,157.1
788,91 1,495.7
819.4
812.2
827.1
17,207.4
106.30
103.01
108.02
2,232.3',1
184
183
186
3,870
21
21
21
21
21
21
21
21
21
21
21
2'l
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: tL/20/24 Lo:so
GP043AS-036892-RT- 1 789
G = Calibration
S = Substltuted
* = Suspect
Time Online Criteria: 1 minute(s)
UN]T3
BARPRESS
(INHG)
ca2
(PCT)
FLOWSCFH(scFH)STKFLOW
TKSCFM]
STKTEMP
IDFGF}
UNlTLOADlt A/t
Page 137 of 195
Average Data - Low Flow Run 6
Plant: HUNTER PLANT
lnterval: 't Minute
Type: Block
Report Period : 1 1 120 12024'l 0:52 Through 1 I I 20 I 2024 1 1 :1 2
Time Online Criteria: 'l minute(s)
Source
11120124 10:52 24.821 8.9 37.704.095.5 824.3 t07.60 185
11120124 10:53 24.8?0 8.9 37,665,593.6 823.0 107.25 1U
11l2ol24 10:54 24.419 8.9 37.566.77?.8 821.0 107.u 185
11120124 10:55 24.819 8.9 37,657 ,463.2 a21-1 185
11120124 10:56 8.9 37.745.332.2 420.7 104.54
11120124 10:57 24.819 8.9 37,84'r,675.7 422.3 |U.14 184
11120124 10:58 21.819 8.9 37,918,548.9 424"7 104.66
11l2ol24 10:59 24.818 8.9 37.745.651.0 a?1.4 104.94
11120124 'l 1:00 24.819 8.9 37 ,723,971.6 421.O 105.01 184
11120124 1 1:0'l 24.819 8.9 37,8r9,528.5 a24.5
11120124 11102 24.A19 8.9 37 ,777,372.3 a25.4 1o7.25
11120124 'l 1:03 24.819 8.9 37,587,863.3 821.9 107.67 185
11120124 'l 1:04 8.9 37.553.019.8 s21.6 107.93
11120124 1 1:05 24_815 37,ffi,111.2 822.2 108.20 183
24.815 8.9 37,/155,093.0 r83
1',1120124 11..07 21.814 8.9 37,321,349.9 817.4 r08.47
11120124 1 1:08 24.815 8.9 37,399,800.8 108.95 185
11120124 'l 1:Og 8.9 37,614,318.3 823.9 185
11120124 11:10 24.815 37,570,960.3 822.2 108.02 1U
11120124 11:11 24.813 8.8 37,376,374.4 8t7.6 '107.74 185
11120124 11'.12 37,398,325.6 817.8 107 .57
Averago
Minimum
Maximum
Summation
Goornetric Maan
lncluded Oata Points
Total numb€r of Data
9^i6ta
24.8'.17
21.812
24.82'l
521.161
8.9
8.8
8.9
186.7
37,619,201.0
37,321,349.9
37,9r8,548.9
790,003.22'1.9
821.6
817.4
825.4
17,253.8
106.97
10/..14
108.95
2,246.27
1U
183
185
3.874
2',1
21
2',1
21
21
?1
21
2'l
21
21
21
21
F = Unlt Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generatedt |L/2O124 Lt:zL
GP043AS-036892-RT- 1 789
C = Callbration
S = Substltuted
* = Suspect
UNtI3
BARPRESS
(rNHG)
UQ2
(Pcr)
r-LuwsuFrl
(scFH)
tit Kt-LUw
(KSCFM)
STKTEMP
(DEGF)
UNTTLOAD
(turw)
Page 138 of 195
Average Data - Low Flow Run 7
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1112012024 1 1:26 Through 1'112012024 11:46
Source
11120t24 11'.26 8.9 37,r141,689.3 820.8 108.89 't 85
11120124 11:27 24.805 8.9 37,6U,722.3
11120124 11:?8 37.506.385.3 823.2 r09.52 184
11120124 11:29 21.807 8.8 37,299,995.0 818.9
11120124 1 1:30 8.9 37,252,443.0 818.2 109.93 184
11120124 1 1:31 24.807 8.9 37,113,637.4 816.2 1 10.63 186
11120124 11'.32 24.807 8.9 37.1 99,261.4 818.2 t 10.73 184
11120124 I 1:33 24.806 8.9 37,359,302.6 821_4 110.49
11t20t21 1',t:9 24.806 8.9 37.388.891.1 822.3 r r0.67 185
11120124 'l 1:35 24.805 37,339,379.9 821.1 1 10.58
1'll2ol24 1 1:36 8.9 37.U2.200.6 820.8 110.29 186
11t20124 11..37 8.9 37,322,958.3 E19.6 186
11120124 1 1:38 24.803 8.9 37,273,356.5 816.7 108.44 185
11120124 1 1:39 8.9 37,267,385.9 E14.4 106.95 185
11120124 1 1:40 24.803 8.9 37,304,516.9 813.7
11120124 11:41 24.803 8.9 37,300,499.4 813.8 r06.01 184
11120124 11:42 24.801 8.9 37,355,268.9 816.2 106.85 184
11120124 1'l:43 24.80'l 8.9 37,384,028.2 81 7.3 107.18 1U
11120124 11:44 8.9 37,485,687.6 820.5 107.80
11120124 1 1:45 24.800 8.9 37,482,551.5 8U.3
11120124 1 'l:46 24.799 E.9 37,422,994.O 821.7 109.57 185
Av€rag€
Minimum
Maximum
Summation
Goomelric Mean
lncluded Data Points
Total numbor of Oata
P^i^rc
24.AU
24.799
24.810
520.892
8.9
8.8
8.9
186.6
37,357,478.8
37,1't 3,637.4
37,66/.,722.3
784,507,055.1
819.2
813.7
826.0
17,203.3
108.95
105.88
1 10.73
2,288.01
185
183
186
3,875
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Contro!
Report G€nerated: 7L/2O/24 tL:55
GP043AS-0 36892-RT- 1 789
C = Calibration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UN]T3
BARPRESS
/rNHal
co2
/qnTl
FLOWSCFH
/q(:FHl
STKFLOW
(KSCFM)
STKTEMP
(DEGFI
UNITLOAD
(lvIW)
Page 139 of 195
Average Data - Low FIow Run 8
Plant: HUNTER PLANT
lnterual: 1 Minute
Type: Block
Report Period: 111201202412:01 Through 1112012024 12:21
Source
11120124 '12:01 24.7 8.9 37.567.003.2 820.1 106.21 185
11120t24 12..02 24.793 8.9 37.455.345.7 417.7 106.10 185
11t20t24 12:03 24.793 8.9 37,310,608.6 106.62 185
11120124 12:04 21.793 8.9 37.1 02.533.1 81 1.E 107.46
11120124 12:05 24.794 8.9 37,r97,767.8 815.7 108.75 185
1'll2ol24 12:06 24.793 8.9 37.317.946.7 819.3 109.34
11120t24 12..07 24.7 8.9 37.373.576.3 820.1 109.07 '184
11120124 12:08 24,793 8.9 37,279,U2.3 185
11120124 12:09 24.792 8.9 37,274,253.0 819.6 I 10.19
11120124 12:10 24.792 8.S 37,303,1 1 9.4 82't.8 't10.1 1 1U
't1120124 12'.11 24.791 8.9 37,339,502.6 820.5 r09.81
11120124 12:12 8.9 37,160,415.7 817.1 t 10.14 185
11120124 12113 24.789 8.9 36,958,241.8 813.1 110.48 1U
11120124 '12:14 24.792 8.9 36.976.145.5 a2.a 110.03
11120124 12:15 24.789 37.072.361.8 815.3 110.21 183
11120124 12.'16 24.7A9 8.8 37,14?,777.7 a17.2 110.49
11120124 12:17 37 ,062,947.7 814.9 I 10.16
11t20t24 24.790 8.8 36,742,518.4 109.95 r84
11120124 12:19 24.789 8.8 36.690.955.5 806.4 r09.90
11120124 12:20 24.788 36,803,372.4 808.3 109.46 185
11120t24 24.788 8.9 36.872.731.0 808.9 186
Average
Minimum
Maximum
Summation
Geometric Msan
lncluded Data Points
Total number of Data
%ihta
24.791
24.788
?4.796
520.617
8.9
8.8
8.9
'186.3
37,146,817.4
36,690,955.5
37,567,003.2
780,083,166.2
8r5.3
806.4
821.8
't7j22.2
109.19
106.16
110.49
2.292.94
184
183
186
3,873
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: 77120/24 t2:27
GP043AS-036892-RT- 1 789
G = Callbration
S = Substitutedi = Suspect
Time Online Criteria: 1 minute(s)
UNlT3
BARPRESS
IINHGT
c02
(PCTI
FLOWSCFH
ISCFHt
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(tvtw)
Page 140 of 195
Average Data - Low Flow Run 9
Plant: HUNTER PLANT
lnterval: 1 Minute
Type: Block
Report Period: 1 1 I 20 12024 1 2: 35 Through 1 1 I 2012024 12:55
Source
11120124 12:35 24.785 36,913,592.9 8t1.8 1 10.1 5 185
11120124 12:36 24.786 8.8 36,870,085.8 810.1 109.64 1U
11t20124 12137 24.786 37,097,991.1 814.5 109.2r 't84
111?0124 12:38 24.785 8.9 37,174,00s.7 816.7 109.58
11120124 12:39 24.785 8.9 3{t.948.447.8 812.2 109.89 r85
11120124 24.765 8.9 36,759,283.3 808.0 'r09.87
11120124 12:41 24.785 8.9 36.933.539.4 810.5 108_98 r83
11120124 '12:42 24.783 8.9 37,265,371.6 816.2 107.8't
11120t24 12:43 24.7U 8.9 37.368.767.0 818.0 '107.52 t82
11120124 24.7U 8.9 37,275,U2.4 816.8
11t20t24 12:45 24.7U 8.9 37.056.827.6 812.6 108.50 184
1',120124 12..46 24.783 8.9 36,902,934.E
11120124 '12:47 21.783 8.9 36.944.842.5 812.6 110.17 i86
lll20l24 12:48 24.783 8_0 36,927,706.9 812.8 I 10.58
11t20124 24.782 8.9 36.906.164.9 812.8 1r0.89 185
11120124 12:50 24.7U 8.9 37.201.917.6
11120124 24.783 8.9 37.440.351.3 825.5 1 r 1.58 r85
l1l?0124 12:52 24.783 37.471.822.3 826.5 11',t.75 18s
11t20t24 24.743 8.8 37,503,622.1 827.1
11t20t24 12:54 24.742 8.8 37.424.4*.4 824.6 1't 1_16 186
11t20t24 12:55 24.742 8.8 37.448.510.2 824.8 110.911 185
Avorage
Minimum
Maximum
Summation
Goomotric Mean
lncluded Data Points
Total numbor of Data
P^i6tc
24.7U
24.782
24.786
520.460
8.9
8.8
8.9
186.3
37,135,053.6
36,759,283.3
37,503,622.1
779,836,125.6
816.4
808.0
827.1
17,144.3
109.93
107.52
'111.75
2,308.45
185
182
186
3.875
21
21
2'.1
2'l
21
21
21
21
2',1
21
21
21
F = Unlt Offllne
E = Exceedance
M = Maintenance
T = Out Of Control
Report Generated: LL/20/24 L3:OL
GP043AS-036892-RT- 1 789
C = Callbration
S = Substituted
* = Suspect
Time Online Criteria: 1 minute(s)
UNIT3
BARPRESS
(rNHG)
wz
(PCT)
FLOWSCFH
(SCFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UN]TLOAD
(tfw)
Page 141 of 195
Appendix 8.L.4
Low-Load Gas RATAs
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Appendix C
Quality Assurance/Quality Control
Appendix C.1
Units and Abbreviations
GP043AS-035892 -RT- 1 789 Page 154 of 195
6ri\ l;t?,N,T+gP.I
UNITS AND ABBREVIATIONS
@X% 02 conected to X% orygen (conected 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 H2O
0 total sampling time, minutespg microgrampa density of acetone, mg/ml
p* 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,fti
A" 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
Cr,s average unadjusted gas concentration, ppmv
Co,, 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
cm or m3 cubic meters
Cun actual concentration of the upscale calibration gas, ppmv
Co average of initial and final system bias check responses from low-level calibration gas, ppmv
Cp pitot tube coefficient
Cs 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 feet
dcm dry cubic meters
Dn diameter of nozzle, inches
D" diameter of stack, inches
dscf dry standard cubic feetdscfm 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
ft2 square feetg gramgal gallonsgr grains (7000 grains per pound)gr/dscf grains per dry standard cubic feet
GP043AS-036892-RT- 1789 Page 155 of 195
6 lt?.N,T+gp.H
UNITS AND ABBREVIATIONS
I percent of isokinetic samplingin inch
k kilo or thousand (metric units, multiply by tO3)K kelvin (temperature)
K3 conversion factor 0.0154 gr/mg
t& conversion factor 0.00266S ((in. HgXft"))/((mlX"R))
kg kilogramKp pitot tube constant (85.49 fUsec)
kwscfh thousand wet standard cubic feet per hourI literslb/hr pounds per hourlb/MMBtu pounds per million Btulpm liters per minutem meter or milliM thousand (English units) or mega (million, metric units)m3 cubic metersma 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 hourmn total amount of particulate matter collected, mg
mol mole
mol. wt. or MW molecular weightM" 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 Hg
pS picogram
Ps stack static pressure, inches H2O
P, barometric pressure of dry gas meter, inches Hg
ppb 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 Hg
psi pounds per square inchpsia pounds per square inch absolutepsig pounds per square inch gauge
Psro standard absolute pressure, 29.92 inches Hg
Q" volumetric flow rate, actual conditions, acfm
Q. volumetric flow rate, standard conditions, scfm
Qsto volumetric flow rate, dry standard conditions, dscfm
R ideal gas constant 21.85 ((in. Hg) (ft3)y(('R) (lbmole))
GP043AS-036892-RT- 1789 Page 156 of 195
64\ l+?.N,T+gP.E
UNITS AND ABBREVIATIONS
SBnnar post-run system bias check, % of span
SBr pre-run system bias check, % of span
scf standard cubic feetsclh standard cubic feet Per hour
scfm standard cubic feet per minute
scm standard cubic metersscmh standard cubic meters per hoursec second
sf, sq. ft., or ft2 square feet
std standardt metric ton (1000 kg)
T o.gzs t-value
T" 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
Ts absolute average stack gas meter temperature, oR (+459.67 for English)
Tsto absolute temperature at standard conditions
v8
V'"
v.
Valstd)
vm
vn
vs
Vrc(stc1
V*(sto)
Vrcg(sto)
W
wa
Wr.p
!Vse
volt
volume of acetone blank, ml
volume of acetone used in wash, ml
total volume H2O collected in impingers and silica gel, grams
volume of gas sampled through dry gas meter, ftJ
volume of gas measured by the dry gas meter, corected to standard conditions, dscf
stack gas volume sampled, acf
volume collected at stack conditions through nozzle, ac'f
average stack gas velocity, feet per second
volume of water vapor condensed, conected to standard conditions, scf
volume of water vapor in gas sampled from impingers, scf
volume of water vapor in gas sampled from silica gel, scf
watt
weight of residue in acetone wash, mg
total weight of impingers, grams
total weight of silica gel, grams
dry gas meter calibration factor, dimensionless
Page 157 of 195GP043AS-036892-RT- 1789
MONTROSEAtR quAttTY SERVtCES
AAS
ACDP
ACE
AD
ADL
AETB
AS
ASTM
BACT
BDL
BHP
BIF
BLS
CC
CD
CE
CEM
CEMS
CERMS
CET
CFR
CGA
CHNOS
CNCG
CO
coc
COMS
CPM
CPMS
CT
CTM
CTO
CVAAS
D"
DE
Dioxins
DLL
DNCG
ECD
EIT
ELCD
EMPC
EPA
EPRI
ES
ESP
EU
FCCU
FGD
FI
FIA
FID
FPD
FPM
FTIR
FTPB
FTRB
Furans
GC
ACRONYMS
atomic absorption spectroscopy
air contaminant discharge permit
analyzer calibration error, percent of span
absolute difference
above detection limit
Air Emissions Testing Body
applicable standard (emission limit)
American Society For Testing And Materials
best achievable control technology
below detection limit
brake horsepower
boiler and industrial furnace
black liquor solids
confldence coefficient
calibration drift
calibration error
continuous emissions monitor
continuous emissions monitoring system
continuous emissions rate monitoring system
calibration error test
Code of Federal Regulations
cylinder gas audit
elemental analysis for determination of C, H, N, O, and S content in fuels
concentrated non-condensable gas
catalytic oxidizer
chain of custody
continuous opacity monitoring system
condensible particulate matter
continuous parameter monitoring system
combustion turbine
conditional test method
catalytic thermal oxidizer
cold vapor atomic absorption spectroscopy
equivalent diameter
destruction efficiency
polychlorinated dibenzo-p-dioxins (pcdd's)
detection level limited
dilute non-condensable gas
electron capture detector
Engineer ln Training
electoconductivity detector (hall detector)
estimated maximum possible concentralion
US Environmental Protection Agency
Electric Power Research lnstitute
emission standard (applicable limit)
electrostatic precipitator
emission unit
fluid catalytic cracking unit
fl ue gas desulfurization
flame ionization
flame ionization analyzer
flame ionization detector
flame photometric detector
fi lterable particulate matter
Fourier-transform infrared spectroscopy
field train proof blank
field train recovery blank
polych lorinated dibenzofurans (pcdf s)
gas chromatography
GP043AS-036892-RT- 1 789 Page 158 of 195
64\ l,l?N,I+gLE
ACRONYMS
GC/MS gas chromatography/mass spectroscopyGFAAS graphite furnace atomic absorption spectroscopy
GFC gas filter conelationGHG greenhouse gas
HAP hazardous air pollutant
HC hydrocarbonsHHV higher heating valueHPLC high performance liquid chromatographyHRGC/HRMS high-resolution gas chromatography/high-resolution mass spectroscopy
HRSG heat recovery steam generator
lC ion chromatographyICAP inductively-coupled argon plasmography
ICPCR ion chromatography with a post-column reactorICP-MS inductively coupled plasma-mass spectroscopylR infrared radiationISO lnternational Standards Organization
kW kilowattsLFG landfill gasLHV lower heating value
LPG liquified petroleum gas
MACT maximum achievable control technologyMDI methylene diphyenyl diisocyanateMDL method detection limitMNOC maximum normal operating conditionsMRL method reporting limitMS mass spectrometryNA not applicable or not availableNCASI National Council For Air And Steam lmprovementNCG non-condensable gases
ND not detectedNDIR non-dispersive infraredNESHAP National Emissions Standards For Hazardous Air PollutantsNG natural gasNIOSH National lnstitute For Occupational Safety And HealthNIST National lnstitute Of Standards And TechnologyNMC non-methane cutterNMOC non-methane organic compoundsNMVOC non-methane volatile organic compoundsNPD nitrogen phosphorus detectorNSPS New Source Performance StandardsOSHA Occupational Safety And Health AdministrationPAH polycyclic aromatic hydrocarbonsPCB polychlorinated biphenyl compoundsPCWP plywood and composite wood products
PE Professional EngineerPFAS per- and polyfluoroalkyl substances (PFAS)Pl photoionizationPID photoionization detectorPM particulate matter
PM,o particulate matter less than 10 microns in aerodynamic diameter
PMz.s particulate matter less than 2.5 microns in aerodynamic diameter
POM polycyclic organic matterPS performance specificationPSD particle size distributionPSEL plant site emission limitsPST performance specification testPTE permanent total enclosurePTM performance test method
GP043AS-036892-RT- 1 789 Page 159 of 195
6 l+?.N,I+gp.E
OfuQC
QI
QSTI
RA
RAA
RACT
RATA
RCTO
RICE
RM
RTO
SAM
SCD
SCR
SD
Semi-VOST
SRM
TAP
TBD
TCA
TCD
TGNENMOC
TGNMOC
TGOC
THC
TIC
TO
TO
TPM
TSP
TTE
ULSD
UV
VE
VOC
VOST
WC
WWTP
ACRONYMS
quality assurance and quality control
Qualified lndividual
Qualified Source Testing lndividual
relative accuracy
relative accuracy audit
reasonably available control technology
relative accuracy test audit
rotary concentrator thermal oxidizer
stationary reciprocating internal combustion engine
reference method
regenerative thermal oxidizer
sulfuric acid mist
sulfur chemiluminescent detector
selective catalytic reduction system
standard deviation
semivolatile organic compounds sample train
standard reference material
toxic air pollutant
to be determined
thermal conductivity analyzer
thermal conductivity detector
total gaseous non-ethane non-methane organic compounds
total gaseous non-methane organic compounds
total gaseous organic compounds
total hydrocarbons
tentatively identified compound
thermal oxidizer
toxic organic (as in EPA Method TO-15)
total particulate matter
total suspended particulate matter
temporary total enclosure
ultra-low sulfur diesel
ultraviolet radiation range
visible emissions
volatile organic compounds
volatile organic sample train
water column
waste water treatment plant
GP043AS-036892-RT- 1 789 Page 160 of 195
6'1i\ flgN,I+P.p.E
CHEMICAL NOMENCLATURE
Ag silverAs arsenic
Ba barium
Be beryllium
C carbonCd cadmium
Se
SO,
Sos
SO,
TCDD
TCDF
TGOC
THC
TI
TRS
Zn
selenium
sulfur dioxide
sulfur trioxide
sulfur oxides
tetrachlorodibenzodioxi n
tetrachlorodibenzofuran
total gaseous organic concentration
total hydrocarbons
thallium
total reduced sulfur compounds
zinc
cadmium sulfide
CH2O formaldehyde
CH3CHO acetaldehyde
CH3OH methanol
CHr methane
C2H4O ethylene ofde
CzHe ethane
CaHIO acrolein
CaH6O propionaldehyde
CsHa propane
C6H5OH phenol
Clz
ct02
co
Co
Coz
Cr
Cu
EtO
chlorine
chlorine dioxide
carbon monoxide
cobalt
carbon dioxide
chromium
copper
ethylene oxideEIOH ethyl alcohol (ethanol)
H2 hydrogen
HrO
HzOz hydrogen peroxide
HrS hydrogen sulfide
H2SO4 sulfuric acid
HCI hydrogen chloride
Hg mercuryIPA isopropyl alcoholMDI methylene diphyenyl diisocyanate
MeCl2 methylene chloride
MEK methyl ethyl ketoneMeOH methanolMn manganese
N2
NHa
nitrogon
ammonia
nickel
nitric oxide
nitrogen dioxide
nitrogen oxides
orygen
Ni
NO
Noz
NO,
O2
P phosphorusPb leadPCDD polychlorinated dibenzo-pdioxinsPCDF polychlorinated dibenzofurans
antimony
GP043AS-036892-RT- 1 789 Page 161 of 195
Appendix C.2
Manual Test Method QAI QC Data
Quality Source Sanpling $stems & Accessories
Wind Tunnel Facility:
Probe Type:
Probe lD:
Standard Pitot lD:
Cp(std):
Barometric Press.(in Hg):
Slde:
0.798
0.795
0.801
CalDate: 12-|tar-21
Personnel: DH
60
60
60
1.117
1.116
1.116
Temp ("F):
R.ro ("):
0.837
0.835
0.839
67.0
- 1.8
0.000
0.002
0.002
cp=cp$a)W %Dlff 4.2Yo
% DilI
708 E. Club Blvd-, Durham, North Carolina 27704
GP043AS-036892 -RT- 1 789
Pitot Calibration for Method 2G
Environmental Supply Co., lnc.
S-Tube
s2c0t17
001
0.99
29.66
'Deviation = l{Cp(s) - AyGCp(s)}l {must be < 0.01}
Standard deviation of the deviations must be less than 0.02 for both sides.
= 9fu:s-l-)- CP (avs -nisa) *.100CP loug to-1
*O*"r"n"" shall not exceed +/-30/6.
0.838
919-95G9688 FAX: [phone]
Page 163 of 195
90
90
90
1.812
1.810
1.806
2.522
2.514
2.5',17
0.839
0.840
0.838
0.000
0.001
0.001
AVERAGE 0.839
Std devlatlon 0.001
www.environsupply.com
Quolly Sourte Sanpltng S\sums &Accessoria
Pitot Calibration for Method 2G
Wind Tunnel Facilig:
Probe Type:
Probe lD:
Standard Pitot lD:
Cp(std):
Barometric Press.(in Hg):
Environmental Supply Co., lnc.
S-Tube
s2G0135
001
0.99
29.56
CalDate:
Personnel:
Temp ('F):
R.ro ('):
l9-Mar-24
DH
89.7
- 0.1
A€IDE
Co=Coloarff %Drff o.1%
'Deviation - l{Cp(3) - AyGCp(g)}l {must bo < 0.0j}
StaMard dcviauon of thc dcvhtlons must b6 loss then 0.02 for both gidea.
%Ditr - CP (*s,*" - CP (ow-not', * 100
CP G"s-to*1
%Difierencs shell not exceed +/-3%.
708 E. Club Blvd", Durharn, North Carolina 277O4
GP043AS-036892-RT- 1 789
919-95G9688 EAX: 919-682-0333
Page 164 of 195
90
90
1.797
1.797
2.697
2.6%
2.691
0.808
0.808
0.809
{.001
0.000
0.001
-AVERAGE 0.808
Std devlatlon 0.001
www.eirvironsupply.com
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GP043AS-036892-RT- 1789 Page 179 of 195
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Lll2Ol24 L2:3t:11
Lll2Ol24 L2:3L:27
LLl2Ol24 t2:3L:37
Lrl2Ol24 l2:3L:41
Lrl2Olz4 l2:3L:5r
Lll2Ol24 12:32:OL
lll2Ol24 12:32;17
t].l2Ol24 L2:32:21
lLl2Ol24 L2:32:31
lll2Ol24 12:32:41
co2 so2 ilOx co
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.o
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
7.2
3.5
7.L
8.8
9.1
9.1
9.1
9.1
9.1
9.1
9.1
62.9 -0.1 -6.2
63.3 4.2 -5.5
63.9 -{1.4 4.7
64.0 -0.3 4.5
64.4 -0.3 4.7
64.2 -0.4 -4.2
64.7 -0.5 -3.7
64.3 -0.4 -3.6
64.5 -0.3 -4.1
64.7 -0.3 -4.1
64.6 -0.3 -4.7
64.6 -0.2 -4.9
64.9 -0.4 -4.9
64.5 -0.3 .4.4
65.0 -0.5 -4.0
65.3 -0.2 -4.4
65.5 -O.3 -3.9
61.4 37.L 3.7
50.8 119.0 26.5
35.5 1tt8.9 63.1
21.S 749.2 101.3
12.8 749.4 128.0
8.4 149.5 140.8
5.6 149.8 145.8
4.1 149.8 147.2
2.8 149.9 148.2
2.0 150.1 14E.5
7.7 149.t t48'7
t.7 149.6 Itt8.8
1.1 149.5 1tl8.5
1.1 749.7 148.1
0.8 L49.7 147.4
0.9 149.6 148.3
0.8 L49.7 144.4
0.9 149.9 148.4
o.7 106.0 744.7
0.7 31.9 L27.1
0.5 2.O 94.7
0.4 0.8 54.8
0.1 0.0 27.9
0.1 0.3 3.4
0.0 0.1 -4.1
0.1 0.1 -6.4
0.0 0.0 -r.?
-{t.2 0.0 -7.3
-o.2 -0.1 -'r.l
GP043AS-036892 -RT- 1 789 Page 180 of 195
Tlme
lLl20l24 12159tll
l]./29124 12:59:27
17l20l24 12:59:37
l1./20124 t2:59:41
lLl2Ol24 12:59:57
7712O/24 l3tOO:Ol
ttl20l24 73:OO:11
7l/2O124 71:N:2L
7l/2O124 73:OO:3t
lll20l24 l3:OO:At
7ll2O/24 l3:OO:51
Lll2Ol24 l3:Ol:Ol
Lt/20/24 l3:Ot:11
17120/24l3:OL27
ttl2ol24 lSto|tl
17l2ol24 13:OL:4r
lll20l24 l3:01:3t
lll2o/24 73t02t0l
lLl2Ol24 l3:O2:tl
fi/2O/24 73:02:27
ll/20/24 73:02:3L
7l/2O124 131O2:4t
11120/2a B:o2:sr
7,.l20/24 13:Ol:Ol
lrl2ol24 13:03:L!
lll2Ol24 73:03:27
7l/2O/24 71:01:31
7ll2ol24 l3:O3:47
77120/24 13:O7:51
17l2Ol24l3:M:01
lLl2gl24 l3t04trl
lll20l24l3:M:21
lLl20l24 13:04:31
lL/2O124 73t04:4L
lLl20l24 13:O4:5L
17/2O124 71:O5:OL
lrl2o/24 73:05:lL
l1/2O/24 L3:O5:2L
ll/20124 73:05:3L
ll/21/24 L3tO5:41
7tl2Ol24 l3:O5:51
7l/2O124 L3:O6:01
7l/20124 1.3:O6:tl
7t/2o/24 t3:O6:27
7l/20124 13:06:37
7l/2O124 13:06:47
lll2Ol24 l3:O6;5L
lU2Ol24l3:O7:Ol
71/20124 t3:O7:lL
77120124 13:07:27
7LlZOl24 t3:O7:31
1Ll2Ol24 rt:O7:41
NOr co
9.1
9.1
9.1
9.1
9.1
9.1
9.2
9.2
9.2
9.2
9.2
8.2
5.1
2.2
0.5
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.4 -0.2 -7.5
0.3 -0.2 -7.4
0.1 {r.3 -6.9
0.0 {.5 -5.5
{t.2 -0.3 {.5-0.2 -o.5 -6.5
o.2 -o.5 -6.5
-0.3 -o.4 -6.7
4.2 -0.3 -6.7
0.0 {.3 -6.8
-o.2 -0.1 -7.1
-0.1 33.8 -5.1
-o.2 90.6 6.5o.2 L24.O 33.6-0.1 141.9 72.20.1 t49.4 109.1o.2 t49.4 133.1
0.3 L49.4 t44.4o.2 t49.4 147.4
0.3 149.9 147.0
0.4 L49.4 146.8
0.4 t49.6 146.8
0.3 149.8 148.3
o.2 149.8 119.7
o.2 149.7 149.5
0.4 149.7 1t8.2
0.6 149.5 t{7.5
0.6 t49.4 148.0
0.5 149.2 747.9
0.5 149.1 747.3
0.4 149.1 146.9
0.6 149.3 L47.1
0.5 149.6 L46.2
3.4 10s.2 139.0
13.1 31.0 177.9
28.O 1.4 83.1
41.6 0.4 44.9
50.9 0.4 16.655.0 0.1 1.4
58.8 -0.2 -4.0
60.7 0.0 -4.9
61.8 0.2 -4.8
63.1 0.1 -4.8
63.6 -0.1 -5.6
53.9 -O.2 -5.6
64.3 0.0 -5.2
54.1 0.0 {.5
il.3 0.0 -3.7
6t1.5 -0.3 -3.3
54.8 -0.2 -3.9
64.9 4.2 -4.6
6rt,9 -O.l -4.5
GP043AS-036892 -RT- 1 789 Page 181 of 195
PROJ-036892
PaclflCorp
Hunter Unlt 3
tu20l2o2{
EPA Method 7E 516.2.2
NOr to NO Convcrtcr Eff,clency Test
NO, ppm
ttl20l2413:09:21
tU2Ol2413:09:31
ttl20l2413:09:41
Ll/2O12413:09r51
1U2O12413:10:01
Ltl2ol2413:10:11
ltl20l2413:10:21
ttl20l2413:10:31
lll20l2413:10:41
LI.l20l2413:10;51
l-tl2Ol24 13:11:01
Ltl2ol2413:11:11
43.9
44.4
44.9
45.0
45.1
45.1
45.4
45.5
45.6
45.8
45.9
46.1
NOr r.re*
torve*
Conveiler Effrclency
Llmlt
/16.1
t[8.4
95,2%
>90|t6
GP043AS-036892-RT- 1 789 Page 182 of 195
Appendix C.4
Calibration Gas Certificates
AiIgas.
an Ar LiqukJo cornpany
Airgas Specialty Gases
Airgas USA LLC
52S North Industrial toop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
E03N180E15A0015
E80097288
124 -Tooele (SAP)- UT
872024
co2,02,BALN
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
JulO2,2O32
153-403084726-1
1s0.0 cF
2015 PS|G
590
Jul 02,2024
Certilication performed in accordanco with 'EPA Trac6ability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" documont EPA
600/R-12531, using th6 assay proceduros listed. Analytical Methodology does not requir€ conection for anaMical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence levol of 95%. Th6re are no signilicant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. Tho r€port shall not b€ reproduced except in full without approval of the laboratory. Do
Not Use This below 100 osio. i.e.0.7
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036892-RT- 1 789
Page 1 of 'l
Page 184 of 195
ANALYTICAL RESI.JLTS
Actual ProtocolConcentration Method
CARBON DIOXIDE
OXYGEN
NITROGEN
9.000 %
10.50 %
Balance
8.944 o/o
1O.51 o/"
+l- 0.7o/o NIST Traceable
+l- O.3o/o NIST Traceable
G1
G1
07to212024
0710212024
CALIBRATION STANDARDS
Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM
NTRM
7 .489 O/O CARBON DIOXIDE/NITROGEN
1 4.93 O/O OXYGEN/NITROGEN
0.6%
0.2%
1 306041 1
1 10606M
cc413537
cc338173
ANALYTICAL EQIIIPMENT
Analytical Principle
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
Airgas.
an Air Liquide company
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:
153-402530253-1
158.0 CF
2015 PSIG
590
5ep02,2022
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)' document EPA
600/R-12/53'l , using the assay procedures listed. Analytical Methodology does not require corroction for anatytical interference. This rylinder has a total analytical
uncortainty as stated below with a confidence level of 957o. There are no significant impurities which affect the use of this calibration mbdure. All concentrations are on a
mole/mole basis unless otheMise noted. The results relate only to the itBms tosted. The report shall not bo roproduced except in full without approval of the laboratory. Do
Nol Use This below 100 psig, i.€. 0.7 m€gapascals
Triad Data Available Upon Request
Sianatrrre on flla
Approved for Release
GP043AS-036892-RT- 1789
Page 1 of 1
Page 185 of 195
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
E03Nt61E1540287
cc701902
124 - Tooele (SAP)- UT
872022
co2,02,BALN
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Sep 02. 2030
ANALYTICAL RESI.'LTS
Actual ProtocolConcentration Method
CARBON DIOXIDE
OXYGEN
NITROGEN
18.00 %
21 .00 0/o
Balance
17.85 Yo
21.0'.1 o/o
G1
G1
+l- 0.7o/o NIST Traceable
+l- 0.5o/o NIST Traceable
09t0a2022
09t0212022
CALIBRATION STANDARDS
Lot lD Cylinder No Concentration Uncertainty Expiration Date
0.6%
0.4Yo
NTRM
NTRM
1 3060802
09061434
cc415397
cc282492
24.04 O/O CARBON DIOXIDE/NITROGEN
22.53 Yo OXYGEN/NITROGEN
ANALYTICAL EQUIPMENT
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
Ai]gas.
an Air Liquide cornpany
Airgas Specialty Gases
Airgas USA LtC
525 North Industrial loop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Products EPA PROTOCOL STANDARI)
Part Number: E02N199E15A1827
Cylinder Number: E80142305Laboratory: 124 - Tooele (SAP)- UT
PGVP Number: 872024
Gas Code: SO2,BALN
Reference Number: 153-403015444-1
Cylinder Volume: 144.0 CF
Cylinder Pressure: 2015 PSIG
Valve Outlet: 660
Certification Date: Apr 16,2024
Expiration Date: Apr 16.2032
Certilication performed in accordance wilh 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)' docum€nt EPA
600/R-1 2/531 , using the assay procedures listed. Analylical Methodology does not roquire conection for anaMical inlerferenc€. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95o/o. There are no significant impurities which affect the use of this calibration mixture. All concrntrations are on a
mole/mole basis unless otheMiso noted. The results relate only to the items tested. The report shall not be reproduc€d exc€pt in full without approval of the laboratory. Do
Not Use This b6low 100 psio, i.6.0.7
Triad Data Available Upon Request
Sionature on file
Approved for Release
GP043AS-036892-RT- 1789
Page I of 1
186 of 195
ANALYTICAL RESI,JLTS
Actual Protocol Total Relative
SULFUR DIOXIDE 63.00 PPM 65.02 PPM Gl +l- 1 .4o/o NIST Traceable 0410912024, 0411612024
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot lD Gylinder No Concentration
NTRM 16010208 KALOO3185 97.69 PPM SULFUR DIOXIDE/NITROGEN 0.8%Nov 01, 2027
ANALYTICAL EQUIPMENT
Analytical Principle
Nicolet iS50 AUP2010228 SO2 MSO2 FTIR 4o103.2024
Page
AiIgas.
an Air Lkluide company
Ai"gas Specialty Gases
Airgas USA LLC
525 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:
153-402452434-1
144.0 CF
2015 PS|G
660
Jun 03,2022
Expiration Date: Jun 03,2030
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" documont EPA
600/R-1 2/531 , using the assay procedures listed. Analytical Methodology does not require correction for analytical inlerference. This cylinder has a total analytical
uncertainty as stated below with a confldence level of 95o/o. There are no signiflcant impurities which affect the use of this calibralion mixture. All concentrations are on a
mole/mole basis unless otherwise noted. Th€ resuhs relate only to the items lested. Tho report shall nol be reproduced except in full without approval of the laboratory. Do
Not Uso This below 100 psig, i.e. 0.7 megapascals
Triad Data Available Upon Request
Sianatrrra on flle
Approved for Release
GP043AS-036892-RT-1 789
Page 't of 1
187 of 195
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
E02Nr99E15A1966
cc97223
124 -Tooele (SAP) - UT
872022
SO2,BALN
ANALYTICAL R"ESULTS
Actual Protocol Total Relative
SULFUR D|OX|DE '145.0 PPM 146.9 PPM Gl +l-0.7o/o NIST Traceable 0512712022,0610312022
NITROGEN BAIANCE
CALIBRATION STANDARDS
Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM 19060735 EBO1'I3181 246.6 PPM SULFUR DIOXIDE/NITROGEN O,4O/O Mar 09, 2026
ANALYTICAL EQUIPMENT
Nicolet iS50 AUP2010228 SO2 MSO2 FTIR Mav 18,2022
Page
Airgas.
an Air Liquide company
Airgas Specialty Gases
Airgas USA Lt C
525 North Industrial l,oop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product:
E03Nr99E15A0353
ALMO54747
124 - Tooele (SAP) - UT
872024
CO,NO,NOX,BALN
EPA PROTOCOL STANDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Aor 10. 2032
1 53-40301 0556-1
144.0 CF
2015 PS|G
660
Apr 10,2024
Expiration Date:
Certification performed in accordance with 'EPA Traceabilily Protocol for Assay and Certification of Gaseous Calibration Standards (May 20121" document EPA
600/R-1 2/531 , using the assay procedures listed. Analytical Methodology does not require correction for anatytical interference. This cylinder 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
mole/mole basis unless othenilise noted. The results relate only to the items lested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This bolow 100 Dsiq. i.e. 0.7
Triad Data Available Upon Request
Sionaiure on flle
Approved for Release
GP043AS-036892-RT- 1 789
Page 1 of 1
188 of 195
ANALYTICAL RE,SI.]LTS
Actual Protoco! Total Relative
NOX '150.0 PPM 151 .4 PPM Gl +l- 0.7o/o NIST Traceable 0410312024, 0411012024
CARBON MONOXIDE 150.0 PPM 150.5 PPM Gl +l- O.5o/o NIST Traceable O4lO3l2O24
NITRIC OXIDE 150.0 PPM 151.4 PPM G1 +l-0.7o/o NIST Traceable 0410312024,0411012024
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM 11010109
PRM 12414GMIS 2023042521
PRM 12409
GM|S 15340',t2021103
KA1003092
4PE1514048
cc7u372
D91 3660
ND73012
97.31 PPM CARBON MONOXIDSNITROGEN
.IOO.19 PPM NITRIC OXIDE/NITROGEN
98.40 PPM NITRIC OXIDE/NITROGEN
15.01 PPM NITROGEN DIOXIDE/AIR
4.956 PPM NITROGEN DIOXIDE/NITROGEN
0.40/o
0.3Yo
0.40/
1.5o/o
1.60/o
May 25,2028
Feb 28,2025
Apr 25,2031
Feb'17,2023
Jun '15, 2025
The SRM, NTRM, PRM, or RGM noted abov€ is only in reference to the GMIS used in the assay and not part of the
ANALYTICAL EQTIIPMENT
Analytical Principle
Apr 02,2024
Mar 13,2024
Mar 13,2024
Nicolet iS50 AUP2010228 CO LCO
Nicolet iS50 AUP2O'1O228 NO LNO
Nicolet iS50 AUP2010228 NO2
FTIR
FTIR
Page
Aituas.
an Air Uqukje company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Inop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
E03Nt99E15A0456
cc323381
124 -Tooele (SAP) - UT
872022
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153-402396220-1
144.0 CF
2015 PS|G
660
Apr 04,2022
Expiration Date: Apr 04, 2030
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certlfication of Gaseous Calibration Standards (May 20121' document EPA
600/R-1 2/531 , 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 affect the use of this calibration mixture. All @ncentrations are on a
Triad Data Available Upon Request
Sianefurre an fila
Approved for Release
GP043AS-036892-RT-1 789
Page 1 of 1
Page 189 of 195
mole/mole basis unless olherwise noted.
ANALYTICAL RESIJLTS
Actual Protocol Total Relative
NOX 330.0 PPM 331.9 PPM Gl +l- 1.2o/o NIST Traceable 0312812022,0410412022
CARBON MONOXIDE 330.0 PPM 328.3 PPM G'l +l-0.5% NIST Traceable 0312812022
NtTRtC OXTDE 330.0 PPM 331.4 PPM G1 +l- 1j% NIST Traceable 0312812022,0410412022
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot !D Gylinder No Concentration
NTRM 14060359
PRM 12395
NTRM 20060321GM|S 1534002020104
The SRM, PRM or RGM notod above is
CC4Y477 2'2.'PPMCARBONMONOXIDE/NITROGEN
D887660 9.91 PPM NITROGEN DIOXIDE/AIR
EBO113037 250.3 PPM NITRIC OXIDE/NITROGEN
EBO13OO55 4.81 PPM NITROGEN DIOXIDE/NITROGEN
in referenco to the GMIS used in the assay and not part of the analysi
0.3%
2.iYo
0.8%
2.0o/o
Feb 1 3, 2026
Feb 02,2022
Oct 19,2026
Apr 30,2024
ANALYTICAL EQUIPMENT
Analytica! Principle
Nicolet iS50 AUP2010228 CO MCO
Nicolet iS50 AUP20'10228 NO MNO
Nicolet iS50 AUP2010228 NO2
FTIR
FTIR
FTIR NO2
Mar 02,2022
Mar 09,2022
Mar 10.2022
Airgas.
an Air Uquid€ company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
CERTIFICATE OFANALYSrc
Grade of Product: EPA PROTOCOL STANDARI)
Part Number: E02A199E15W002't
Cylinder Number: CC502363Laboratory: 124 - Tooele (SAP) - UT
PGVP Number: 872023
Gas Code: NO2,BALA
Reference Number: 153-4027077 56-1
Cylinder Volume: 146.0 CF
Cylinder Pressure: 2015 PSIG
Valve Outlet: 660
Certification Date: Apr 10,2023
Expiration Date: Apr 10. 2026
Certilication 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 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
mole/mole basis unless otherwise notod. The results relate only to the items tested. The report shall not b€ reproduced except in full without approval of the laboratory. Do
Not Us6 This bolow 100 osio, i.e. 0.7
Triad Data Available Upon Request
Sianrhrra an fila
Approved for Release
GP043AS-036892-RT- 1789
Page I of 1
195
ANALYTICAL RESULTS
Actual Protoco! Total Relative
NITROGEN DIOXIDE 50.00 PPM 48.42 PPM Gl +l- 2.Oo/o NIST Traceable 0410312023, 041'1012023
AIR Balance
CALIBRATION STANDARDS
Type Lot !D Gylinder No Concentration Uncertainty Expiration Date
GM|S 12357 CC511358 59.32 PPM NTTROGEN D|OXTDE/NTTROGEN 1.40/o Dec'17,2024
ANALYTICAL EQUPMENT
Analytical Principle Last Multipoint Calibration
MKS FT|R NO2 018143349 FTIR 4o106.2023
Page 190 of
Appendix C.5
Accred itation I nformation / Ceft ifications
tnol
o
Ncrl
OJc'lto
CLa
E](J
)r{
&
E]a
Htr{
F]
pc
&lr{
rqac&
FlZc
E
oo=oo
ooo
6o-c
-)N
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