DAQ-2024-004373

1

DAQC-1364-23
Site ID 10238 (B5)

MEMORANDUM

TO: CEM FILE – PACIFICORP HUNTINGTON PLANT

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Rob Leishman, Environmental Scientist

DATE: December 21, 2023

SUBJECT: Source: Huntington Power Plant Units 1 and 2
Contact: Russ Wilson – 435-687-4331
Location: Huntington Canyon, Emery County, UT
Test Contractor: Air Hygiene, Inc.
FRS ID#: UT00000049001501001
Permit/AO#: Title V operating permit #1501001005, dated January 22, 2020
Subject: Review of RA/PST Report dated May 3, 2023

On May 8, 2023, Utah Division of Air Quality (DAQ) received a Relative Accuracy/Performance
Specification Test (RA/PST) report for the Pacificorp Huntington Plant Units 1 and 2 in Huntington,
Utah. Testing was performed on April 12-14, 2023, 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. 1
NSPS RATA - Test Date - 4/13-14/2023
Primary
Channel Manufacturer Serial
No. Units CEM
Value
RM
Value
Relative
Accuracy Status
SO2 Thermo Fisher
43iQ-ACAN 131 ppm 20.356 22.243 11.1% Passed
lbs/MMBtu 0.057 0.061 9.8% Passed
CO2 Thermo Fisher
410iQ-ACN 133 % 10.750 10.920 3.0% Passed
NOx Thermo Fisher
42iQ-ACANN 132 ppm 100.578 100.346 2.1% Passed
lbs/MMBtu 0.203 0.198 4.0% Passed
CO Thermo Fisher 48iQ-CAN ppm 139.356 142.767 4.6% Passed
lbs/MMBtu 0.169 0.171 3.9% Passed
Volumetric Flow Rate wscfh 77065486 78916900 3.2% Passed
Stack Test Deviation Report
There were no deviations observed during testing.
Calibration gases were in date and met performance specifications.

1 8 2
2

Unit No. 1
Acid Rain Tests - Test Date - 4/13-14/2023
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status Testing
Frequency
SO2 Thermo Fisher
43iQ-ACAN 131 ppm 20.355 22.243 19.00% Passed Annual
NOx Thermo Fisher
42iQ-ACANN 132 lbs/MM
Btu 0.203 0.198 4.30% Passed Annual
CO2 Thermo Fisher
410iQ-ACN 133 % 10.756 10.920 2.99% Passed
Equation - Di (Rmi – CEMi)
Rmi = 0.1976
CEMi = 0.2031
Di = 0.0055 Passed

Unit No. 2
NSPS RATA - Test Date - 4/14/2023
Primary
Channel Manufacturer Serial No. Units CEM
Value
RM
Value
Relative
Accuracy Status
SO2 Thermo Fisher
43iQ-CAN 231 ppm 26.644 26.014 2.8% Passed
lbs/MMBtu 0.074 0.074 1.4% Passed
CO2 Thermo Fisher
410iQ-CAN 234 % 10.730 10.490 2.9% Passed
NOx Thermo Fisher
42iQ-ACANN 232 ppm 113.889 109.612 4.4% Passed
lbs/MMBtu 0.228 0.225 2.2% Passed
CO Thermo Fisher
48iQ-CAN ppm 124.867 128.989 5.7% Passed
lbs/MMBtu 0.149 0.160 9.7% Passed
Volumetric Flow Rate wscfh 81119625 82886440 2.8% Passed
Stack Test Deviation Report
There were no deviations observed during testing.
Calibration gases were in date and met performance specifications.

Unit No. 2
Acid Rain Tests - Test Date - 4/14/2023
Primary
Channel Manufacturer Serial
No. Units CEM
Value
RM
Value
Relative
Accuracy Status Testing
Frequency
SO2 Thermo Fisher
43iQ-CAN 231 ppm 26.644 26.014 4.00% Passed Annual
NOx Thermo Fisher
42iQ-ACANN 232 lbs/MMBtu 0.228 0.225 2.10% Passed Annual
CO2 Thermo Fisher
410iQ-CAN 234 % 10.733 10.495 2.93% Passed
Equation - Di (Rmi – CEMi)
Rmi = 0.2246
CEMi = 0.2283
Di = 0.0037 Passed

3

DEVIATIONS: No deviations were noted in this report.

CONCLUSION: Pacificorp operates the continuous emissions monitors (CEMs) on the
Huntington Unit 1 and Unit 2 stacks to measure CO2, NOX, SO2, and CO
emissions. The CEMs were audited by the DAQ and found to meet
quality assurance requirements found in 40 CFR Part 60, Appendix B,
Performance Specification 1, and R307-170, Continuous Emission
Monitoring System Program. Quarterly cylinder gas audits and an annual
relative accuracy test audit were conducted in accordance with the
procedures outlined in UAC R307-170.

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

HPV: No.

ATTACHMENTS: RATA Review Spreadsheets.
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name PacifiCorp Huntington
Company Contact:Richard Neilson
Contact Phone No.435-687-4334
Stack Designation:Unit No. 1
Test & Review Dates
Test Date:4/13-14/2023
Review Date: 12/19/2023
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.1200 0.2600 0.3400 0.061 0.198 0.171
lbs./hr. 595.0 1290.0 1686.0 259.58 841.915 726.260
ppm
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
323.28 570.013 0.9783 1.82 0.824 23.38 -4.5 23.049118

Contractor Information
Contact:Andrew Bruning
Contracting Company: Montrose Air Quality Services
Address: 990 W 43rd Avenue, Denver, CO 80211
Phone No.: 303-810-2168
Project No.:
1800

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
Lignite
Natural
Propane
Butane
10100
COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Wet CEM
Correct For O2
CO2 Interference w/CO
Yes
Yes
Yes
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Company PacifiCorp Huntington
Point Source Unit No. 1
Test Date 4/13-14/2023
Start
Time
End
Time Run
CO
lb/hr
CO
lb/mmbtu
CO2
%
CO
ppm
NOx
lb/hr
NOx
lb/MMBtu
NOx
PPM
SO2
lb/hr
SO2
lb/MMBtu
SO2
PPM
Unit Load
MW
Heat Input
MMBtu/hr
Stack
Flow
WSCF
6:12 6:33 1 844.5 0.183 10.6 148.9 1033.7 0.225 111.3 269.8 0.059 20.9 493 4594.6 77741892
7:06 7:27 2 1017.4 0.223 10.8 185.1 909.9 0.196 99.8 266.5 0.058 21 493 4596.5 76338519
7:49 8:10 3 712.9 0.156 10.9 129.6 903.7 0.196 90.1 261.7 0.057 20.6 493 4610 76362986
8:26 8:47 4 1456.6 0.31 10.9 258.9 879.4 0.19 96.6 257.9 0.058 20.4 496 4625.4 76266939
9:02 9:23 5 1046.6 0.228 10.9 190.1 896.7 0.194 96.4 236.7 0.052 18.8 495 4623.4 76284511
9:59 10:20 6 1000 0.223 10.8 183.7 924.1 0.2 100.3 247.2 0.054 19.3 492 4614 77208758
11:15 11:36 7 340.3 0.079 10.6 63.6 941.9 0.205 102.2 244.7 0.054 19.1 485 4534.7 77212255
11:50 12:11 8 303.7 0.07 10.6 56.8 961.2 0.211 103.6 256.1 0.058 19.9 487 4551.5 77569671
6:12 6:33 9 214.3 0.046 10.7 37.5 965 0.211 104.9 303.1 0.065 23.2 492 4662.2 78603841
10
11
12
13
14
15
16
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.12 595.00
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/13-14/2023 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/13-14/2023 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 6:12 6:33 Y 23.1 20.9 2.15 Y 0.0626 0.059 0.004 272.28 269.8 1 6:12 6:33 Y 11.0 10.6 0.42
2 7:06 7:27 Y 23.8 21 2.80 Y 0.0665 0.058 0.008 277.81 266.5 2 7:06 7:27 Y 10.7 10.8 -0.09
3 7:49 8:10 Y 22.1 20.6 1.45 Y 0.0619 0.057 0.005 255.06 261.7 3 7:49 8:10 Y 10.6 10.9 -0.25
4 8:26 8:47 Y 22.6 20.4 2.20 Y 0.0608 0.058 0.003 256.43 257.9 4 8:26 8:47 Y 11.1 10.9 0.21
5 9:02 9:23 Y 21.0 18.8 2.21 Y 0.0561 0.052 0.004 247.21 236.7 5 9:02 9:23 Y 11.2 10.9 0.30
6 9:59 10:20 Y 21.5 19.3 2.17 Y 0.0585 0.054 0.004 250.02 247.2 6 9:59 10:20 Y 11.0 10.8 0.18
7 11:15 11:36 Y 20.3 19.1 1.19 Y 0.0559 0.054 0.002 236.47 244.7 7 11:15 11:36 Y 10.9 10.6 0.26
8 11:50 12:11 Y 22.4 19.9 2.51 Y 0.0624 0.058 0.004 262.92 256.1 8 11:50 12:11 Y 10.7 10.6 0.14
9 6:12 6:33 Y 23.5 23.2 0.31 Y 0.0639 0.065 -0.001 278.03 303.1 9 6:12 6:33 Y 11.0 10.7 0.31
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 22.2 20.36 1.89 0.061 0.057 0.004 Average = 10.920 10.750 0.164
Sd Standard Deviation = 0.77 Sd Standard Deviation = 0.002 Sd Standard Deviation = Sd Standard Deviation = 0.21
Confidence Coefficient = 0.59 Confidence Coefficient = 0.002 Confidence Coefficient = Confidence Coefficient = 0.162
RA - Relative Accuracy =11.10%RA 9.80%RA RA - Relative Accuracy =2.98%
n = 9 9 0 n = 9 or RA of 1%0.17%
t0.975 = 2.306 2.306 t0.975 = 2.306
E.L. Relative Accuracy = 51%
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
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Thermo Fisher 43iQ-ACAN 131
133Thermo Fisher 410iQ-ACN
Ac
t
i
v
a
t
e

R
u
n
?
PassedPassedPassed
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 1
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.26 1290.00
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/13-14/2023 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 6:12 6:33 Y 108.6 111.3 -2.7 Y 0.212 0.225 -0.013 922.07 1033.7 1 6:12 6:33 7.5
2 7:06 7:27 Y 97.8 99.8 -2.0 Y 0.196 0.196 0.000 820.56 909.9 2 7:06 7:27 7.5
3 7:49 8:10 Y 95.7 90.1 5.6 Y 0.193 0.196 -0.003 795.94 903.7 3 7:49 8:10 7.5
4 8:26 8:47 Y 95.2 96.6 -1.4 Y 0.184 0.19 -0.006 776.07 879.4 4 8:26 8:47 7.5
5 9:02 9:23 Y 97.2 96.4 0.8 Y 0.187 0.194 -0.007 822.08 896.7 5 9:02 9:23 7.5
6 9:59 10:20 Y 99.5 100.3 -0.8 Y 0.195 0.2 -0.005 832.89 924.1 6 9:59 10:20 7.5
7 11:15 11:36 Y 102.3 102.2 0.1 Y 0.203 0.205 -0.002 856.85 941.9 7 11:15 11:36 7.5
8 11:50 12:11 Y 103.0 103.6 -0.6 Y 0.206 0.211 -0.005 868.45 961.2 8 11:50 12:11 7.5
9 6:12 6:33 Y 103.8 104.9 -1.1 Y 0.203 0.211 -0.008 882.33 965 9 6:12 6:33 7.5
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 100.3 100.6 0.232 0.20 0.203 0.005 Average =
Sd Standard Deviation = 2.44 Sd Standard Deviation = 0.004 Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = 1.874 Confidence Coefficient = 0.003 Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy =2.10%Relative Accuracy =4.00%Relative Accuracy = RA - Relative Accuracy =
n = 9 9 0 n = 0 or RA of 1%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 =
E.L. Relative Accuracy = EMRA 76% 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
132Thermo Fisher 42iQ-ACANN
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
PassedPassed
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 1
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.340 1686.00
Date CO Dry CO Dry CO
4/13-14/2023 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 6:12 6:33 Y 142.72 148.9 6.18 Y 0.170 0.183 0.013 737.69 844.5
2 7:06 7:27 Y 191.65 185.1 -6.55 Y 0.234 0.223 -0.011 978.75 1017.4
3 7:49 8:10 Y 135.76 129.6 -6.16 Y 0.167 0.156 -0.011 687.10 712.9
4 8:26 8:47 Y 263.04 258.9 -4.14 Y 0.310 0.31 0.000 1305.77 1456.6
5 9:02 9:23 Y 196.93 190.1 -6.83 Y 0.230 0.228 -0.002 1013.56 1046.6
6 9:59 10:20 Y 189.05 183.7 -5.35 Y 0.225 0.223 -0.002 963.27 1000
7 11:15 11:36 Y 65.17 63.6 -1.57 Y 0.079 0.079 0.000 332.21 340.3
8 11:50 12:11 Y 58.91 56.8 -2.11 Y 0.072 0.07 -0.002 302.42 303.7
9 6:12 6:33 Y 41.67 37.5 -4.17 Y 0.050 0.046 -0.004 215.58 214.3
10
11
12
13
14
15
16
Average = 142.77 139.36 3.41 0.171 0.169 0.002
Sd Standard Deviation = 4.05 0.007
Confidence Coefficient = 3.111 0.005
RA - Relative Accuracy =4.60% 3.90%
n = 9 9 0
t0.975 = 2.306 2.306
E.L. Relative Accuracy = 50%
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Passed Passed
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Thermo Fisher 48iQ-CAN
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Dry Volumetric Flow
dscfh
Run Date Start Time End Time RM CEM Diff
1 4/13-14/2023 6:12 6:33 71,090,345.04
2 4/13-14/2023 7:06 7:27 70,239,499.78
3 4/13-14/2023 7:49 8:10 69,609,113.04
4 4/13-14/2023 8:26 8:47 68,274,902.55
5 4/13-14/2023 9:02 9:23 70,785,477.53
6 4/13-14/2023 9:59 10:20 70,078,317.93
7 4/13-14/2023 11:15 11:36 70,112,106.38
8 4/13-14/2023 11:50 12:11 70,605,428.92
9 4/13-14/2023 6:12 6:33 71,148,179.43
10 4/13-14/2023
11 4/13-14/2023
12 4/13-14/2023
13 4/13-14/2023
14 4/13-14/2023
15 4/13-14/2023
16 4/13-14/2023
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Dry Volumetric Flow
dscfm
Run Date Start Time End Time RM CEM Diff
1 4/13-14/2023 6:12 6:33 1,184,839.08
2 4/13-14/2023 7:06 7:27 1,170,658.33
3 4/13-14/2023 7:49 8:10 1,160,151.88
4 4/13-14/2023 8:26 8:47 1,137,915.04
5 4/13-14/2023 9:02 9:23 1,179,757.96
6 4/13-14/2023 9:59 10:20 1,167,971.97
7 4/13-14/2023 11:15 11:36 1,168,535.11
8 4/13-14/2023 11:50 12:11 1,176,757.15
9 4/13-14/2023 6:12 6:33 1,185,802.99
10 4/13-14/2023
11 4/13-14/2023
12 4/13-14/2023
13 4/13-14/2023
14 4/13-14/2023
15 4/13-14/2023
16 4/13-14/2023
Average =
Standard Deviation
PacifiCorp Huntington
Unit No. 1
En
t
e
r

Us
e
En
t
e
r

Us
e
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Actual Volumetric Flow
acfm
Run Date Start Time End Time RM CEM Diff
1 4/13-14/2023 6:12 6:33 1,868,833.22
2 4/13-14/2023 7:06 7:27 1,842,498.62
3 4/13-14/2023 7:49 8:10 1,835,863.67
4 4/13-14/2023 8:26 8:47 1,787,606.37
5 4/13-14/2023 9:02 9:23 1,850,741.01
6 4/13-14/2023 9:59 10:20 1,833,538.02
7 4/13-14/2023 11:15 11:36 1,847,115.73
8 4/13-14/2023 11:50 12:11 1,858,094.18
9 4/13-14/2023 6:12 6:33 1,859,393.81
10 4/13-14/2023
11 4/13-14/2023
12 4/13-14/2023
13 4/13-14/2023
14 4/13-14/2023
15 4/13-14/2023
16 4/13-14/2023
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
WET VOLUMETRIC FLOW
wscfh
Run Date Start Time End Time RM CEM Diff
1 4/13-14/2023 6:12 6:33 Y 80,057,126.52 77741892 2,315,234.52
2 4/13-14/2023 7:06 7:27 Y 78,984,461.09 76338519 2,645,942.09
3 4/13-14/2023 7:49 8:10 Y 78,562,035.56 76362986 2,199,049.56
4 4/13-14/2023 8:26 8:47 Y 76,456,743.74 76266939 189,804.74
5 4/13-14/2023 9:02 9:23 Y 79,268,177.82 76284511 2,983,666.82
6 4/13-14/2023 9:59 10:20 Y 78,476,274.52 77208758 1,267,516.52
7 4/13-14/2023 11:15 11:36 Y 79,071,274.05 77212255 1,859,019.05
8 4/13-14/2023 11:50 12:11 Y 79,569,153.33 77569671 1,999,482.33
9 4/13-14/2023 6:12 6:33 Y 79,806,854.93 78603841 1,203,013.93
10 4/13-14/2023
11 4/13-14/2023
12 4/13-14/2023
13 4/13-14/2023
En
t
e
r

Us
e
En
t
e
r

Us
e
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
14 4/13-14/2023
15 4/13-14/2023
16 4/13-14/2023
Average = 78,916,900.17 77,065,485.78 1,851,414.39
Standard Deviation 850,995
Confidence Coefficient = 654131
RA - Relative Accuracy =1 3.2%
n = 9
t0.975 =2.306
Wet Volumetric Flow
wscfm
Run Date Start Time End Time RM CEM Diff
1 4/13-14/2023 6:12 6:33 1,334,285.44
2 4/13-14/2023 7:06 7:27 1,316,407.68
3 4/13-14/2023 7:49 8:10 1,309,367.26
4 4/13-14/2023 8:26 8:47 1,274,279.06
5 4/13-14/2023 9:02 9:23 1,321,136.30
6 4/13-14/2023 9:59 10:20 1,307,937.91
7 4/13-14/2023 11:15 11:36 1,317,854.57
8 4/13-14/2023 11:50 12:11 1,326,152.56
9 4/13-14/2023 6:12 6:33 1,330,114.25
10 4/13-14/2023
11 4/13-14/2023
12 4/13-14/2023
13 4/13-14/2023
14 4/13-14/2023
15 4/13-14/2023
16 4/13-14/2023
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
En
t
e
r

Us
e
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 1
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023
Start Time 6:12 7:06 7:49 8:26 9:02 9:59 11:15 11:50 6:12
Stop Time 6:33 7:27 8:10 8:47 9:23 10:20 11:36 12:11 6:33
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28 323.28
As ft^2 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01 570.01
Cp (Pitot Tube Coefficient)0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82
Yd Meter Y Factor (unit less)0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783 0.9783
Pbar Barometric Pressure ("Hg)23.38 23.38 23.38 23.38 23.38 23.38 23.38 23.38 23.38 23.38 23.38 23.38
Pq (Static Pressure)-4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50
Ps (Pressure of the Stack)23.05 23.05 23.05 23.05 23.05 23.05 23.05 23.05 23.05 23.05 23.05 23.05
Ts Stack Temp Avg. oF 109.70 109.30 110.30 110.60 109.80 110.20 110.10 109.90 108.60
Tm Meter Temperature oF 66.00 66.00 66.00 71.00 71.00 71.00 69.00 71.00 56.00
CO2 (carbon dioxide)11.02 10.71 10.65 11.11 11.20 10.98 10.86 10.74 11.01
O2 (oxygen)7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Md Molecular Weight Dry 30.06 30.01 30.00 30.08 30.09 30.06 30.04 30.02 30.06 #VALUE!#VALUE!
Ms Molecular Weight Wet 28.71 28.68 28.63 28.79 28.80 28.77 28.68 28.67 28.75 #VALUE!#VALUE!
N2 (nitrogen)81.48 81.79 81.85 81.39 81.30 81.52 81.64 81.76 81.49 #VALUE!#VALUE!
Vm Sample Volume (cf)99.65 99.65 99.65 75.55 75.55 75.55 50.80 26.20 29.04 0.00 0.00 0.00
Vm std Standard Volume (dscf)76.44 76.44 76.44 57.41 57.41 57.41 38.74 19.91 22.71
Vlc Moisture (g)215.40 215.40 215.40 142.40 142.40 142.40 134.00 62.10 60.60
Vwstd Moisture Volume (scf)10.14 10.14 10.14 6.70 6.70 6.70 6.31 2.92 2.85
Bws Moisture Content (%100)12.08%12.08%12.08%10.70%10.70%10.70%14.36%13.10%11.71%
S Bws (saturation moisture)11.20%11.07%11.40%11.49%11.23%11.36%11.33%11.27%10.85%
AvgSqrtDlp √∆P 0.849 0.837 0.831 0.837 0.843 0.831 0.843 0.849 0.849
Vs. Gas Velocity (ft./sec)54.64 54.64 54.64 54.64 54.64 54.64 54.64 54.64 54.64 54.64 54.64 54.64
Qa (stack actual flow rate) acfm 1,868,833 1,842,499 1,835,864 1,787,606 1,850,741 1,833,538 1,847,116 1,858,094 1,859,394
Qs (stack std. flow rate) dscfm 1,184,839 1,170,658 1,160,152 1,137,915 1,179,758 1,167,972 1,168,535 1,176,757 1,185,803 #VALUE!#VALUE!#VALUE!
Qsd (stack std. flow rate) dscfh 71,090,345 70,239,500 69,609,113 68,274,903 70,785,478 70,078,318 70,112,106 70,605,429 71,148,179
Qw (stack flow rate) wscfm 80,057,127 78,984,461 78,562,036 76,456,744 79,268,178 78,476,275 79,071,274 79,569,153 79,806,855
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 1
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023 4/13-14/2023
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 23.10 23.80 21.30 21.10 19.50 19.90 19.10 21.40 23.20
Dry Corrected 23.05 23.80 22.05 22.60 21.01 21.47 20.29 22.41 23.51
Wet Corrected
NOx Concentrations
Uncorrected 111.90 99.90 93.50 91.40 94.00 96.50 100.20 101.70 104.90
Dry Corrected 108.59 97.80 95.73 95.16 97.23 99.50 102.31 102.97 103.82
Wet Corrected
CO Concentrations
Uncorrected 149.60 197.40 133.50 253.10 189.40 181.20 62.50 56.30 40.00
Dry Corrected 142.72 191.65 135.76 263.04 196.93 189.05 65.17 58.91 41.67
Wet Corrected
CO2 Concentrations
Uncorrected 11.30 11.20 10.90 11.00 11.00 10.80 10.80 10.80 11.20
Dry Corrected 11.02 10.71 10.65 11.11 11.20 10.98 10.86 10.74 11.01
Wet Corrected
O2 Concentrations
Uncorrected 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Dry Corrected 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50 7.50
Wet Corrected
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.061 0.198 0.171 Average % concentration
lbs./hr.259.58 841.91 726.26 CO2 O2
ppm or % 22.24 100.35 142.77 10.92 7.50
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 CO2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.26E-02 2.12E-01 1.70E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.830E-06 1.297E-05 1.038E-05
lbs./hr.272.28 922.07 737.69 11.02 7.50
ppm or %23.05 108.59 142.72 11.30 7.50
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.65E-02 1.96E-01 2.34E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.955E-06 1.168E-05 1.393E-05
lbs./hr.277.81 820.56 978.75 10.71 7.50
ppm or %23.80 97.80 191.65 11.30 7.50 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.19E-02 1.93E-01 1.67E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.664E-06 1.143E-05 9.871E-06
lbs./hr.255.06 795.94 687.10 10.65 7.50
ppm or %22.05 95.73 135.76 10.90 7.50 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.08E-02 1.84E-01 3.10E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.756E-06 1.137E-05 1.913E-05
lbs./hr.256.43 776.07 1305.77 11.11 7.50
ppm or %22.60 95.16 263.04 11.00 7.50 Raw Value
Run 5
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)5.61E-02 1.87E-01 2.30E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.492E-06 1.161E-05 1.432E-05
lbs./hr.247.21 822.0824 1013.56 11.20 7.50
ppm or %21.01 97.23 196.93 11.00 7.50 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 1
O2
CO2
Clear
lbs./MMBTU
Run 6
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)5.85E-02 1.95E-01 2.25E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.568E-06 1.189E-05 1.375E-05
lbs./hr.250.02 832.8882 963.27 10.98 7.50
ppm or %21.47 99.50 189.05 10.80 7.50 Raw Value
Run 7
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)5.59E-02 2.03E-01 7.85E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.373E-06 1.222E-05 4.738E-06
lbs./hr.236.47 856.85 332.21 10.86 7.50
ppm or %20.29 102.31 65.17 10.80 7.50 Raw Value
Run 8
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.24E-02 2.06E-01 7.18E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.724E-06 1.230E-05 4.283E-06
lbs./hr.262.92 868.45 302.42 10.74 7.50
ppm or %22.41 102.97 58.91 10.80 7.50 Raw Value
Run 9
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.39E-02 2.03E-01 4.95E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.908E-06 1.240E-05 3.030E-06
lbs./hr.278.03 882.33 215.58 11.01 7.50
ppm or %23.51 103.82 41.67 11.20 7.50 Raw Value
Run 10
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
Run 11
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Huntington Unit 1 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-13-2023)
Calibration Error Test
Test Date 4/13-14/2023 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 4/13-14/2023 CO2
CS - Cal. Span 17.94
Units %
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
Mid-level 8.93 9.20 0.27 1.505% Passed Cal.
High-level 17.94 17.90 0.04 0.223% 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 49.78%
100% of Cal. Span High-level 100.00%
Test Date 4/13-14/2023 SO2
CS - Cal. Span 61.94
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 0.161% Passed Cal.
Mid-level 26.51 26.30 0.21 0.339% Passed Cal.
High-level 61.94 62.00 0.06 0.097% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 42.80%
100% of Cal. Span High-level 100.00%
Test Date 4/13-14/2023 NOx
CS - Cal. Span 332.30
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.10 0.10 0.030% Passed Cal.
Mid-level 153.80 156.70 2.90 0.873% Passed Cal.
High-level 332.30 335.80 3.50 1.053% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 46.28%
100% of Cal. Span High-level 100.00%
Test Date 4/13-14/2023 CO
1686 CS - Cal. Span 333.80
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.70 0.70 0.210% Passed Cal.
Mid-level 150.90 154.30 3.40 1.019% Passed Cal.
High-level 333.80 335.60 1.80 0.539% 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 45.21%
100% of Cal. Span High-level 100.00%
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name PacifiCorp Huntington
Company Contact:Richard Neilson
Contact Phone No.435-687-4334
Stack Designation:Unit No. 2
Test & Review Dates
Test Date:4/14/2023
Review Date: 12/20/2023
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.1200 0.2600 0.074 0.225
lbs./hr.
ppm
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
322.68 567.899 0.9995 1.721 0.824 23.45 -4.5 23.119118
Contractor Information
Contact:Andrew Bruning
Contracting Company: Montrose Air Quality Services
Address: 990 W 43rd Avenue, Denver, CO 80211
Phone No.: 303-810-2168
Project No.:
1800

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
Lignite
Natural
Propane
Butane
10100
COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Wet CEM
Correct For O2
CO2 Interference w/CO
Yes
Yes
Yes
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Company PacifiCorp Huntington
Point Source Unit No. 2
Test Date 4/14/23
Start
Time
End
Time Run
CO
lb/hr
CO
lb/mmbtu
CO2
%
CO
ppm
NOx
lb/hr
NOx
lb/MMBtu
NOx
PPM
SO2
lb/hr
SO2
lb/MMBtu
SO2
PPM
Unit Load
MW
Heat Input
MMBtu/hr
Stack
Flow
WSCF
9:08 9:29 1 299.3 0.052 10.6 50 1133.3 0.235 115.2 516.3 0.107 37.5 451 4832 82390103
10:00 10:21 2 173.6 0.036 10.5 29 1147.6 0.239 116.9 433.6 0.09 31.8 480 4808.3 82204033
10:36 10:57 3 203.9 0.042 10.6 34.3 1154.4 0.238 117.9 432.1 0.083 29.5 483 4840.7 81980084
11:12 11:33 4 650.2 0.133 11 111.8 1031.3 0.212 107.9 334.9 0.069 25.2 486 4873.4 80058021
11:48 12:09 5 1071.6 0.22 10.9 183.1 1059.6 0.218 110.2 320.4 0.066 24 484 4863.5 80562616
12:22 12:43 6 621.7 0.17 10.8 150.4 1072.7 0.222 111.7 290.6 0.06 21.8 479 4825 80384575
12:59 13:20 7 1341 0.279 10.8 229.9 1091.7 0.227 113.8 313.5 0.065 23.5 479 4808.6 80358745
13:32 13:53 8 866.1 0.184 10.7 150.4 1127 0.233 116.3 298.2 0.062 22.1 480 4830 81144153
14:07 14:28 9 1088.4 0.226 10.7 184.9 1113.3 0.231 115.1 328.3 0.068 24.4 478 4810.4 80994293
10
11
12
13
14
15
16
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.12
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
4/14/2023 RM CEMS Diff RM CEMS Diff RM CEMS Diff 4/14/2023 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 9:08 9:29 Y 37.0 37.5 -0.51 Y 0.1062 0.107 -0.001 452.87 516.3 1 9:08 9:29 Y 10.4 10.6 -0.18
2 10:00 10:21 Y 31.1 31.8 -0.66 Y 0.0901 0.09 0.000 388.06 433.6 2 10:00 10:21 Y 10.3 10.5 -0.16
3 10:36 10:57 Y 28.8 29.5 -0.73 Y 0.0824 0.083 -0.001 362.66 432.1 3 10:36 10:57 Y 10.4 10.6 -0.16
4 11:12 11:33 Y 24.8 25.2 -0.36 Y 0.0700 0.069 0.001 301.73 334.9 4 11:12 11:33 Y 10.6 11 -0.38
5 11:48 12:09 Y 23.4 24 -0.64 Y 0.0664 0.066 0.000 286.10 320.4 5 11:48 12:09 Y 10.5 10.9 -0.38
6 12:22 12:43 Y 21.2 21.8 -0.62 Y 0.0599 0.06 0.000 259.76 290.6 6 12:22 12:43 Y 10.6 10.8 -0.22
7 12:59 13:20 Y 22.8 23.5 -0.74 Y 0.0646 0.065 0.000 278.25 313.5 7 12:59 13:20 Y 10.5 10.8 -0.26
8 13:32 13:53 Y 21.3 22.1 -0.79 Y 0.0605 0.062 -0.002 261.16 298.2 8 13:32 13:53 Y 10.5 10.7 -0.16
9 14:07 14:28 Y 23.8 24.4 -0.62 Y 0.0681 0.068 0.000 291.28 328.3 9 14:07 14:28 Y 10.4 10.7 -0.26
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 26.0 26.64 0.63 0.074 0.074 0.000 Average = 10.490 10.730 0.238
Sd Standard Deviation = 0.13 Sd Standard Deviation = 0.001 Sd Standard Deviation = Sd Standard Deviation = 0.09
Confidence Coefficient = 0.10 Confidence Coefficient = 0.001 Confidence Coefficient = Confidence Coefficient = 0.068
RA - Relative Accuracy =2.80%RA 1.40%RA RA - Relative Accuracy =2.91%
n = 9 9 0 n = 9 or RA of 1%0.24%
t0.975 = 2.306 2.306 t0.975 = 2.306
E.L. Relative Accuracy = 62%
a For steam generators;b Average of three samples;9
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
13.2 Relative accuracy Performance Specification. The RA of the CEMSS must be not greater than 20 percent when RM is used in the denominator of Eq. 2-6
(average emissions during test are greater than 50 percent of the emission standard)or 10 percent when the applicable emission standard is used in the
denominator of Eq. 2-6 (average emissions during test are less than 50 percent of the emission standard).
Up dated January 17, 2006
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
13.2 CEMS Relative Accuracy Perfromance Specification.
The RA of the CEMS must be no grater than 20 percent of the mean value of the reference method (RM) data. 1 percent O2 or CO2.
The results are also acceptable if the absolute value of the difference between the mean RM value and the mean CEMS value is less than or equal to 1.0 percent O2 (or CO2).
Up dated September 14, 2016
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
PassedPassedPassed
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Thermo Fisher 43iQ-CAN 231
234Thermo Fisher 410iQ-CAN
Ac
t
i
v
a
t
e

R
u
n
?
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 2
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:0.26
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
4/14/2023 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 9:08 9:29 Y 112.1 115.2 -3.1 Y 0.231 0.235 -0.004 986.22 1133.3 1 9:08 9:29 6.5
2 10:00 10:21 Y 112.3 116.9 -4.6 Y 0.233 0.239 -0.006 1005.78 1147.6 2 10:00 10:21 6.5
3 10:36 10:57 Y 114.6 117.9 -3.3 Y 0.236 0.238 -0.002 1038.38 1154.4 3 10:36 10:57 6.5
4 11:12 11:33 Y 104.1 107.9 -3.8 Y 0.211 0.212 -0.001 908.96 1031.3 4 11:12 11:33 6.5
5 11:48 12:09 Y 106.0 110.2 -4.2 Y 0.217 0.218 -0.001 933.35 1059.6 5 11:48 12:09 6.5
6 12:22 12:43 Y 106.9 111.7 -4.8 Y 0.217 0.222 -0.005 942.48 1072.7 6 12:22 12:43 6.5
7 12:59 13:20 Y 109.1 113.8 -4.7 Y 0.223 0.227 -0.004 959.02 1091.7 7 12:59 13:20 6.5
8 13:32 13:53 Y 111.2 116.3 -5.1 Y 0.227 0.233 -0.006 979.55 1127 8 13:32 13:53 6.5
9 14:07 14:28 Y 110.1 115.1 -5.0 Y 0.227 0.231 -0.004 969.84 1113.3 9 14:07 14:28 6.5
10 10
11 11
12 12
13 13
14 14
15 15
16 16
Average = 109.6 113.9 4.277 0.23 0.228 0.004 Average =
Sd Standard Deviation = 0.73 Sd Standard Deviation = 0.002 Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = 0.562 Confidence Coefficient = 0.001 Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy =4.40%Relative Accuracy =2.20%Relative Accuracy = RA - Relative Accuracy =
n = 9 9 0 n = 0 or RA of 1%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 =
E.L. Relative Accuracy = EMRA 86% 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
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
PassedPassed
232Thermo Fisher 42iQ-ACANN
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Division of Air Quality
Relative Accuracy Test Audit of
PacifiCorp Huntington
Unit No. 2
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Date CO Dry CO Dry CO
4/14/2023 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 9:08 9:29 Y 59.89 50 -9.89 Y 0.075 0.052 -0.023 320.73 299.3
2 10:00 10:21 Y 34.35 29 -5.35 Y 0.043 0.036 -0.007 187.24 173.6
3 10:36 10:57 Y 38.35 34.3 -4.05 Y 0.048 0.042 -0.006 211.51 203.9
4 11:12 11:33 Y 114.87 111.8 -3.07 Y 0.142 0.133 -0.009 610.45 650.2
5 11:48 12:09 Y 183.93 183.1 -0.83 Y 0.229 0.22 -0.009 985.46 1071.6
6 12:22 12:43 Y 145.64 150.4 4.76 Y 0.180 0.17 -0.010 781.46 621.7
7 12:59 13:20 Y 236.06 229.9 -6.16 Y 0.293 0.279 -0.014 1262.70 1341
8 13:32 13:53 Y 155.95 150.4 -5.55 Y 0.194 0.184 -0.010 836.33 866.1
9 14:07 14:28 Y 191.86 184.9 -6.96 Y 0.240 0.226 -0.014 1028.35 1088.4
10
11
12
13
14
15
16
Average = 128.99 124.87 4.12 0.160 0.149 0.011
Sd Standard Deviation = 4.18 0.005
Confidence Coefficient = 3.214 0.005
RA - Relative Accuracy =5.70% 9.70%
n = 9 9 0
t0.975 = 2.306 2.306
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Passed Passed
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Thermo Fisher 48iQ-CAN
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Dry Volumetric Flow
dscfh
Run Date Start Time End Time RM CEM Diff
1 4/14/23 9:08 9:29 73,660,232.54
2 4/14/23 10:00 10:21 74,979,863.98
3 4/14/23 10:36 10:57 75,854,276.27
4 4/14/23 11:12 11:33 73,087,496.88
5 4/14/23 11:48 12:09 73,688,655.65
6 4/14/23 12:22 12:43 73,799,857.15
7 4/14/23 12:59 13:20 73,568,562.02
8 4/14/23 13:32 13:53 73,758,276.29
9 4/14/23 14:07 14:28 73,717,437.21
10 4/14/23
11 4/14/23
12 4/14/23
13 4/14/23
14 4/14/23
15 4/14/23
16 4/14/23
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Dry Volumetric Flow
dscfm
Run Date Start Time End Time RM CEM Diff
1 4/14/23 9:08 9:29 1,227,670.54
2 4/14/23 10:00 10:21 1,249,664.40
3 4/14/23 10:36 10:57 1,264,237.94
4 4/14/23 11:12 11:33 1,218,124.95
5 4/14/23 11:48 12:09 1,228,144.26
6 4/14/23 12:22 12:43 1,229,997.62
7 4/14/23 12:59 13:20 1,226,142.70
8 4/14/23 13:32 13:53 1,229,304.60
9 4/14/23 14:07 14:28 1,228,623.95
10 4/14/23
11 4/14/23
12 4/14/23
13 4/14/23
14 4/14/23
15 4/14/23
16 4/14/23
Average =
Standard Deviation
En
t
e
r

Us
e
En
t
e
r

Us
e
PacifiCorp Huntington
Unit No. 2
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
Actual Volumetric Flow
acfm
Run Date Start Time End Time RM CEM Diff
1 4/14/23 9:08 9:29 1,914,478.39
2 4/14/23 10:00 10:21 1,934,718.31
3 4/14/23 10:36 10:57 1,965,350.79
4 4/14/23 11:12 11:33 1,904,596.95
5 4/14/23 11:48 12:09 1,919,248.74
6 4/14/23 12:22 12:43 1,922,145.03
7 4/14/23 12:59 13:20 1,914,103.58
8 4/14/23 13:32 13:53 1,922,076.88
9 4/14/23 14:07 14:28 1,919,998.37
10 4/14/23
11 4/14/23
12 4/14/23
13 4/14/23
14 4/14/23
15 4/14/23
16 4/14/23
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
WET VOLUMETRIC FLOW
wscfh
Run Date Start Time End Time RM CEM Diff
1 4/14/23 9:08 9:29 Y 82,478,711.65 82390103 88,608.65
2 4/14/23 10:00 10:21 Y 83,556,555.72 82204033 1,352,522.72
3 4/14/23 10:36 10:57 Y 84,759,877.14 81980084 2,779,793.14
4 4/14/23 11:12 11:33 Y 81,980,862.86 80058021 1,922,841.86
5 4/14/23 11:48 12:09 Y 82,626,058.95 80562616 2,063,442.95
6 4/14/23 12:22 12:43 Y 82,750,747.64 80384575 2,366,172.64
7 4/14/23 12:59 13:20 Y 82,433,548.43 80358745 2,074,803.43
8 4/14/23 13:32 13:53 Y 82,733,263.44 81144153 1,589,110.44
9 4/14/23 14:07 14:28 Y 82,658,331.31 80994293 1,664,038.31
10 4/14/23
11 4/14/23
12 4/14/23
13 4/14/23
En
t
e
r

Us
e
En
t
e
r

Us
e
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
14 4/14/23
15 4/14/23
16 4/14/23
Average = 82,886,439.68 81,119,624.78 1,766,814.90
Standard Deviation 760,156
Confidence Coefficient = 584307
RA - Relative Accuracy =1 2.8%
n = 9
t0.975 =2.306
Wet Volumetric Flow
wscfm
Run Date Start Time End Time RM CEM Diff
1 4/14/23 9:08 9:29 1,374,645.19
2 4/14/23 10:00 10:21 1,392,609.26
3 4/14/23 10:36 10:57 1,412,664.62
4 4/14/23 11:12 11:33 1,366,347.71
5 4/14/23 11:48 12:09 1,377,100.98
6 4/14/23 12:22 12:43 1,379,179.13
7 4/14/23 12:59 13:20 1,373,892.47
8 4/14/23 13:32 13:53 1,378,887.72
9 4/14/23 14:07 14:28 1,377,638.86
10 4/14/23
11 4/14/23
12 4/14/23
13 4/14/23
14 4/14/23
15 4/14/23
16 4/14/23
Average =
Standard Deviation
Confidence Coefficient =
RA - Relative Accuracy =
n = 0
t0.975 =
En
t
e
r

Us
e
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 2
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023
Start Time 9:08 10:00 10:36 11:12 11:48 12:22 12:59 13:32 14:07
Stop Time 9:29 10:21 10:57 11:33 12:09 12:43 13:20 13:53 14:28
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68 322.68
As ft^2 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90 567.90
Cp (Pitot Tube Coefficient)0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82 0.82
Yd Meter Y Factor (unit less)0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995 0.9995
Pbar Barometric Pressure ("Hg)23.45 23.45 23.45 23.45 23.45 23.45 23.45 23.45 23.45 23.45 23.45 23.45
Pq (Static Pressure)-4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50 -4.50
Ps (Pressure of the Stack)23.12 23.12 23.12 23.12 23.12 23.12 23.12 23.12 23.12 23.12 23.12 23.12
Ts Stack Temp Avg. oF 108.20 106.80 107.60 108.70 108.60 108.60 108.40 108.70 108.60
Tm Meter Temperature oF 63.00 63.00 63.00 69.00 69.00 69.00 70.00 70.00 70.00
CO2 (carbon dioxide)10.42 10.35 10.44 10.62 10.52 10.58 10.54 10.54 10.44
O2 (oxygen)6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50
Md Molecular Weight Dry 29.93 29.92 29.93 29.96 29.94 29.95 29.95 29.95 29.93 #VALUE!#VALUE!
Ms Molecular Weight Wet 28.65 28.70 28.68 28.66 28.65 28.66 28.66 28.65 28.64 #VALUE!#VALUE!
N2 (nitrogen)83.08 83.16 83.06 82.88 82.98 82.92 82.96 82.96 83.06 #VALUE!#VALUE!
Vm Sample Volume (cf)90.29 90.29 90.29 75.67 75.67 75.67 74.30 74.30 74.30 0.00 0.00 0.00
Vm std Standard Volume (dscf)71.38 71.38 71.38 59.14 59.14 59.14 57.96 57.96 57.96
Vlc Moisture (g)191.10 191.10 191.10 159.70 159.70 159.70 162.40 162.40 162.40
Vwstd Moisture Volume (scf)9.00 9.00 9.00 7.52 7.52 7.52 7.64 7.64 7.64
Bws Moisture Content (%100)11.61%11.61%11.61%11.58%11.58%11.58%11.94%11.94%11.94%
S Bws (saturation moisture)10.69%10.26%10.51%10.85%10.82%10.82%10.75%10.85%10.82%
AvgSqrtDlp √∆P 0.877 0.889 0.894 0.872 0.877 0.894 0.877 0.877 0.877
Vs. Gas Velocity (ft./sec)56.19 56.19 56.19 56.19 56.19 56.19 56.19 56.19 56.19 56.19 56.19 56.19
Qa (stack actual flow rate) acfm 1,914,478 1,934,718 1,965,351 1,904,597 1,919,249 1,922,145 1,914,104 1,922,077 1,919,998
Qs (stack std. flow rate) dscfm 1,227,671 1,249,664 1,264,238 1,218,125 1,228,144 1,229,998 1,226,143 1,229,305 1,228,624 #VALUE!#VALUE!#VALUE!
Qsd (stack std. flow rate) dscfh 73,660,233 74,979,864 75,854,276 73,087,497 73,688,656 73,799,857 73,568,562 73,758,276 73,717,437
Qw (stack flow rate) wscfm 82,478,712 83,556,556 84,759,877 81,980,863 82,626,059 82,750,748 82,433,548 82,733,263 82,658,331
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification PacifiCorp Huntington
Point Source Unit No. 2
Contact Phone No.Richard Neilson
Stack Designation:Unit No. 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023 4/14/2023
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 37.10 31.70 29.30 25.30 23.80 21.60 23.20 21.80 24.30
Dry Corrected 36.99 31.14 28.77 24.84 23.36 21.18 22.76 21.31 23.78
Wet Corrected
NOx Concentrations
Uncorrected 113.90 116.10 116.60 106.10 111.20 113.70 116.90 119.70 119.20
Dry Corrected 112.09 112.30 114.60 104.12 106.04 106.91 109.13 111.18 110.14
Wet Corrected
CO Concentrations
Uncorrected 59.40 32.70 37.00 116.30 188.40 147.80 239.80 157.80 194.80
Dry Corrected 59.89 34.35 38.35 114.87 183.93 145.63 236.06 155.95 191.86
Wet Corrected
CO2 Concentrations
Uncorrected 10.60 10.70 10.80 11.10 11.00 11.00 10.90 10.90 10.80
Dry Corrected 10.42 10.35 10.44 10.62 10.52 10.58 10.54 10.54 10.44
Wet Corrected
O2 Concentrations
Uncorrected 6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50
Dry Corrected 6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50 6.50
Wet Corrected
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.074 0.225 0.160 Average % concentration
lbs./hr.CO2 O2
ppm or % 26.01 109.61 128.99 10.49 6.50
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 CO2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)1.06E-01 2.31E-01 7.52E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.148E-06 1.339E-05 4.354E-06
lbs./hr.452.87 986.22 320.73 10.42 6.50
ppm or %36.99 112.09 59.89 10.60 6.50
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)9.01E-02 2.33E-01 4.35E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 5.176E-06 1.341E-05 2.497E-06
lbs./hr.388.06 1005.78 187.24 10.35 6.50
ppm or %31.14 112.30 34.35 10.60 6.50 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)8.24E-02 2.36E-01 4.81E-02 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.781E-06 1.369E-05 2.788E-06
lbs./hr.362.66 1038.38 211.51 10.44 6.50
ppm or %28.77 114.60 38.35 10.80 6.50 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)7.00E-02 2.11E-01 1.42E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 4.128E-06 1.244E-05 8.352E-06
lbs./hr.301.73 908.96 610.45 10.62 6.50
ppm or %24.84 104.12 114.87 11.10 6.50 Raw Value
Run 5
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.64E-02 2.17E-01 2.29E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.883E-06 1.267E-05 1.337E-05
lbs./hr.286.10 933.3542 985.46 10.52 6.50
ppm or %23.36 106.04 183.93 11.00 6.50 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
PacifiCorp Huntington
Unit No. 2
O2
CO2
Clear
lbs./MMBTU
Run 6
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)5.99E-02 2.17E-01 1.80E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.520E-06 1.277E-05 1.059E-05
lbs./hr.259.76 942.4849 781.46 10.58 6.50
ppm or %21.18 106.91 145.64 11.00 6.50 Raw Value
Run 7
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.46E-02 2.23E-01 2.93E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.782E-06 1.304E-05 1.716E-05
lbs./hr.278.25 959.02 1262.70 10.54 6.50
ppm or %22.76 109.13 236.06 10.90 6.50 Raw Value
Run 8
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.05E-02 2.27E-01 1.94E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.541E-06 1.328E-05 1.134E-05
lbs./hr.261.16 979.55 836.33 10.54 6.50
ppm or %21.31 111.18 155.95 10.90 6.50 Raw Value
Run 9
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)6.81E-02 2.27E-01 2.40E-01 E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.951E-06 1.316E-05 1.395E-05
lbs./hr.291.28 969.84 1028.35 10.44 6.50
ppm or %23.78 110.14 191.86 10.80 6.50 Raw Value
Run 10
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
Run 11
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Huntington Unit 2 High Flow RATA RM 1, 2G, 2H, 3A, 6C, 7E, 10 (Tested 4-12-2023)
Calibration Error Test
Test Date April 14, 2023 O2
CS - Cal. Span 20.00
Units %
Cylinder No. Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.00% Passed Cal.
Mid-level 10.00 10.00 0.00 0.00% Passed Cal.
High-level 20.00 20.00 0.00 0.00% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of CS - Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 50.00%
100% of Cal. Span High-level 100.00%
Test Date April 14, 2023 CO2
CS - Cal. Span 17.94
Units %
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.10 0.10 0.557% Passed Cal.
Mid-level 8.93 8.90 0.03 0.167% Passed Cal.
High-level 17.94 17.80 0.14 0.780% 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 49.78%
100% of Cal. Span High-level 100.00%
Test Date April 14, 2023 SO2
CS - Cal. Span 61.94
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 0.00 0.00 0.000% Passed Cal.
Mid-level 26.51 26.00 0.51 0.823% Passed Cal.
High-level 61.94 61.90 0.04 0.065% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 42.80%
100% of Cal. Span High-level 100.00%
Test Date April 14, 2023 NOx
CS - Cal. Span 332.30
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 -0.30 0.30 0.090% Passed Cal.
Mid-level 153.80 153.70 0.10 0.030% Passed Cal.
High-level 332.30 334.40 2.10 0.632% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 46.28%
100% of Cal. Span High-level 100.00%
Test Date April 14, 2023 CO
CS - Cal. Span 333.80
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 -1.60 1.60 0.479% Passed Cal.
Mid-level 150.90 151.40 0.50 0.150% Passed Cal.
High-level 333.80 334.00 0.20 0.060% 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 45.21%
100% of Cal. Span High-level 100.00%
xFtgr$PRPENERGY
Huntington Power Plant
6 miles west of Huntington, Utah on Hwy. 3l
P.O. Box 680
Huntington, Utah 84528
May 3,2023
Mr. Bryce Bird, Director
Utah Department of Environmental Quality
Division of Air Quality
195 North 1950 West
P. O. Box 144820
Salt Lake city, utah 84114-4820
Attn: Mr. Rob Leishman
RE: 2023 RATA Reports
U'TAH DEPARI'MENT OF
ENVIiiOhlId{:NTAL QUAUTY
[tLl * .] .,iJ
DIVISION OF AIR OUALITY
Dear Mr. Bird,
The Annual Source Emission Test Reports, or Relative Accuracy Test Audits (RATAs) of the Continuous
Emissions Monitoring Systems (CEMs) in service at the PacifiCorp Huntington Plant Units I and2have
been completed per the specifications found in 40 CFR Part 60 and 7 5 . The low-load, and high-load
Flow RATAs, along with the high-load Gas RATAs were conducted on April l2s - 14'fi,2023.
Enclosed are the RATA reports for the Huntington Plant Unit I and2 Flow and Gas CEMs.
I am authorized to make this submission on behalf of the owners and operators of the affected source or
affected units for which the submission is made. I certiff under penalty of the law that I have personally
examined, and am familiar with, the statements and information submitted in this document and its
attachments. Based on my inquiry of those individuals with primary responsibility for obtaining the
information, I certifu that the statements and information are to the best of my knowledge and belief true,
accurate, and complete. I am aware that there are significant penalties for submitting false statements and
information or omitting required statements and information, including the possibility of fine or
imprisonment.
Should you have any questions or concerns please contact Terry Guthrie, Hunter and Huntington Plant
Envi
Sincerel
(
Ll^-r---,
ren Huntsma
Managing Director - Hunter and Huntington Plants
Responsible Official
Enclosures: "Source Test Report for 2023 RATA Testing Unit I &Unitz"
cc:
Scarlet Jackson - NTO w/o enclosure
Youn Joo Kim - EPA Region VIII denclosure
Russ Willson - Huntington Plant denclosure
Tom Wiscomb - NTO w/o enclosure
Source Test Report tor 2023
Unitl&Unit2
PacifiCorp
RATA Testing
Huntington Power Plant
Huntington, Utah
Prepared For:
PacifiCorp
L407 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
Docu ment N u mber: G PO43AS-O 227 22-RT-1 298
Test Dates: April 12 - 14, 2023
Submittal Date: May L4,2023
U'f.i ;-i [)t.i--!\!r-; r,.:-i.j i iil]
ENlu l0Nhli:i\ tl\l- C{ir\UTy
Ni,ri i t..
DIVISIONI CF AIil
,l
ci.,At_iT',/
ah
lIEFrEiiEql
'fJi"o,H"?""
sAe
rl
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 ceftify
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.
April26,2023
Name:Title: Project Manager
I have reviewed, technically and editorially, details, calculations, results, conclusions, and
other appropriate written materials contained herein. I hereby certify that, to the best of my
knowledge, the presented material is authentic, accurate, and conforms to the requirements
of the Montrose Quality Management System and ASTM D7036-04.
April26,2023
Name:Matthew Parks QA/QC Specialist
G P043AS -02 27 22-RT - L298 Page 2 of 278
rl
Tahle of Contents
Section Paqe
1.0 Introduction... .......... 5
1.1 Summary of Test Program ........ 5
t.2 KeyPersonnel..... ......,..,.9
2.0 Plant and Sampling Location Descriptions..,..,.. .....,..........11
2.t Process Description, Operation, and Control Equipment............ ............11
2.2 Flue Gas Sampling Locations ............11
2.3 Operating Conditions and Process Data...... ....,...11
2.4 CEMS Description .........L2
3.0 Sampling and Analytical Procedures ...........13
3.1 Test Methods.... .......13
3.1.1 EPA Method 2c ... .....,........13
3,1.2 EPA Method 2H............ ......15
3.1.3 EPA Method 4........ ...,.........16
3.1.4 EPA Methods 34, 6C, 7E, and 10.......... ..............18
3.2 Process Test Methods.,,., ..............19
4.0 Test Discussion and Results........ .....2O
4.1 Field Test Deviations and Exceptions.... ............20
4.2 Presentation of Results........ .........20
5.0 Internal QA/QC Activities .........2L
5.1 QA/QC Audits .............21
5.2 QA/QC Discussion. ..........21
5.3 Quality Statement ...........21
List of Appendices
A Field Data and Calculations ... .........22
A.1 Sampling Locations.. .....23
A.2 RATA Results..... ......25
A.2.1 Unit 1 ....... .........26
A.2.2 Unit 2........ ...........33
A.3 Field Data .......40
A.3.1 Unit 1........ ..........4L
A.3.1.1 Low-Load Flow Data ......42
4.3.L.2 High-Load Flow Data .......60
A.3.1,3 Instrumental Test Method Data.. ........,.83
A.3,2 Unit 2........ ........,.91
A,3.2.1 Low-Load Flow Data .........92
a a ra - t
.a
a .r I r- a
G P043AS -02 27 22 - RT - t298 Page 3 ot 278
I
ro
A.3.2.2 High-Load Flow Data ,.............110
A.3.2.3Instrumental Test Method Data.... .........131
A.4 Example Calculations ........ .,...139
B Facility Process Data........ .....148
B.1 Unit 1 .........,149
B.1.1 Low-Load Flow RATA..... ,.,........150
B.1.2 High-Load Flow RATA ...........160
B.1.3 Gas MTAs.... ......L7L
B.2 Unit 2........ ......182
B.2.1 Low-Load Flow RATA.. .,..,183
8.2.2 High-Load Flow RATA ,.......193
B.2.3 Gas MTAs.. .......2O4
C Quality Assurance/Quality Control .......,....215
C.1 Units and Abbreviations,........... .....2L6
C.2 Manual Test Method QA/QC Data..... .......224
C.3 Instrumental Test Method QA/QC Data...... ...........231
C.3.1 Unit 1 ..,... ....232
C.3.2 Unit 2........ ......,...251
C.4 Calibration Gas Certificates.. ..........267
C.5 Accreditation Information/Certifications ..274
List of Tables
Table 1-1 Summary ofTest Program,..... .......5
Table 1-2 Summary of RATA Results - Huntington Unit 1.,...... .......7
Table 1-3 Summary of RATA Results - Huntington Unit 2........ ............. I
Table 1-4 Test Personnel and Observers......... ......10
Table 2-1 Sampling Locations...... .........11
Table 2-2 CEMS Information .,...........12
List of Figures
Figure 3-1 EPA Method 2G Sampling Train ....14
Figure 3-2 EPA Method 4 Sampling Train........ ..........t7
Figure 3-3 EPA Methods 3A, 6C, 7E, and 10 Sampling Train .........19
I
G P04 3AS-02 27 22 -Rr - L29 I Page 4 of 278
I rl
1.O Introduction
1.1 Summary of Test Program
PacifiCorp contracted Montrose Air Quality Services, LLC (Montrose) to perform a RATA test
program at Huntington Power Plant located in Huntington, Utah. The tests were conducted
in accordance with the requirements of UDEQ Operating Permit 1501001005 and (as
applicable) 40 CFR Parts 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 Units 1 and
2.
. 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 repoft, a list of Units and Abbreviations is included in Appendix C.1.
Throughout this report, chemical nomenclature, acronyms, and reporting units are not
defined. Please refer to the list for specific details.
:1..-.:'r r !'-.r' at !t ' r
411212023 Huntington
Unit 1
Low Volumetric Flow Rate RATA EPAMZG/H,3,4 9 >5
4lt3/2023 Huntington
Unit 2 Low Volumetric Flow Rate RATA EPA,M2G/H,3,4 9 >5
4lt3/2023 Huntington
Unit 1
High Volumetric Flow Rate RATA*EPAM2G/H,3,4 9 >5
High Oz, COz, SOz, NOx, CO MTAsx EPA M3A, 6C,7E, and 10 9 2t
4/L4/2023 Huntington
Unit 2
High Volumetric Flow Rate RATA EPAMZG/H,3,4 9 >5
High Oz, COz, SOz, NO*, CO MTAs EPA M3A, 6C,7E, and 10 9 2t
'The last run of the Unit 1 High Load RATAwas completed on April 14h.
GP043AS-0227 22-RT -L298 Page 5 of 278
o ro
r' r I Air rruA. ltlry r!Elitl,rlt:.[:!
This report presents the test results and supporting data, descriptions of the testing
procedures, descriptions of the facility and sampling locations, and a summary of the quality
assurance procedures used by Montrose. The average emission test results are summarized
and compared to their respective performance specifications in Tables 1-2 through 1-4.
Detailed results for lndlvidua! test runs and all supporting data can be found in the
appendlces.
The testing was conducted by the Montrose personnel listed in Table 1-5. The tests were
conducted according to the test plan (protocol) that was submitted to and approved by
UDEQ.
I
r1
ii
t'
I
i
tl
I
I
I
i
lir
I necirrcorp
Z02l ,RA;A Reparl i;rrrii,r!:t,r Prul r'- i
G P04 3AS -0227 22-RT - L298 Page 6 of 278
I ro
Table 1-2
Summary of RATA Results - Huntington Unit 1
April 12 - L4,2023
Part 6O
Sulfur Dioxide (SOz)
lblmmBtu PS-2 < 20.0olo of RM 9,60/o
lb/hr PS-6 < 20.0olo of RM t3.9o/o
Nitrogen Oxides (NO, as NOz)
ppmvw PS.2 < 20.0olo of RM 2.4o/o
tblhr PS-6 < 20.0olo of RM 2.2o/o
Carbon Monoxide (CO)
ppmvw PS-4A < 10olo of RM 5.5o/o
lblmmBtu PS-6 S 20.0olo of RM 4.Oolo
lb/hr PS-5 < 20.0olo of RM 9.7olo
Part 75
Volumetric Flow (Low Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM l.Oo/o
Volumetric Flow (High Load)
wscfh App. B Sect. 2.3.1.2 Annual: S 7.5olo of RM 3.Oolo
Carbon Dioxide (COz)
o/o volume wet App. B Sect. 2.3.1.2 Annual: S 7.5olo of RM 3.Lo/o
Sulfur Dioxide (SOz)
ppmvw App. B Sect. 2.3.1.2 Annual: d + 12.0ppm d = 1.8 ppm
Nitrogen Oxides (NO, as NOz)
lblmmBtu App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 4.4o/o
GP043AS-0227 22-RT - 7298 Page 7 oJ 278
ar
,t
Table 1-3
Summary of RATA Results - Huntington Unit 2
April 13 & 14, 2023
?
Part 6O
Sulfur Dioxide (SOz)
lblmmBtu PS-2 < 20.0olo of RM O.5olo
lblhr PS.6 S 20.0olo of RM L.Oolo
Nitrogen Oxides (NOx as NOz)
ppmvw PS-2 3 20.0olo of RM 4.4o/o
lblhr PS-5 < 20.0olo of RM 2.2o/o
Carbon Monoxide (CO)
ppmvw PS-44 < 10o/o of RM 5.4o/o
lblmmBtu PS.6 < 20.0olo of RM 7.9o/o
lb/hr PS-6 < 20.0olo of RM 7.8o/o
Part 75
Volumetric Flow (Low Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 2.7o/o
Volumetric Flow (High Load)
wscfh App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 3.Oo/o
Carbon Dioxide (COz)
o/o volume wet App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 3.Lo/o
Sulfur Dioxide (SOz)
ppmvw App. B Sect. 2.3.1.2 Annual: < 7.5olo of RM 2.9o/o
Nitrogen Oxides (NOx as NOz)
lblmmBtu App. B Sect. 2.3.1.2 Annual: S 7.5olo of RM 2.Oolo
' rl
I .r r r. a . r: .t... .
G P043AS -02 27 22-RT - L298 Page 8 of 278
I
I
i
1.2 Key Personnel
A list of proJect pafticipants is included below:
Facility Information
Source Location: PacifiCorp
Huntington Wyoming Plant
8 Miles West of Huntington on Hwy 31
ProJect Contact: Tom Wiscomb Russell Willson
Role: Sr. Environmental Advisor Senlor EnvironmentalAnalyst
Company: PacifiCorp PacifiCorp
Telephone: [phone] (435) 687-433t
Email: [e-mail] [e-mail]
Agency Information
Regulatory Agency: Utah Department of Air Quality
Agency Contact: Rob Leishman
Telephone: [phone]
Email: [e-mail]
Testing Company Informatlon
Testing Firm: Montrose Air Quality Servlces, LLC
Contact: Cralg Kormylo
T'itle: DistrictManager
Telephone: [phone]
Email: [e-mail]
FacifiCrrp
2 | 2 I RATA R e pr rt. l-l unliilgtirlr P lv."ie,' llau rtl
G P04 3AS -02 27 22-RT - 1298 Page 9 of 278
ra
Test personnel and observers are summarized in Table 1-4.
Table 1-4
Test Personnel and Observers
Craig Kormylo
Project Manager
Qualified Individual (QI)
Trailer operator
Sample train operator
Sample train operator
Calculations and report preparation
Test Coordinator
Plant Representative
GP043AS-0227 22-Rr -t298 Page 10 of 278
rl
2,O Plant and Sampling Location Descriptions
2,L Process Description, Operation, and Control
Equipment
The Huntington Plant comprises two pulverized coal-fired boilers. Huntington Unit #1 is
equipped with low-NO* burners and overfire air for nitrogen oxides (NO,) control, a flue gas
desulfurization (FGD) scrubber for sulfur dioxide (SOz) control and pulse-jet fabric filters for
particulate matter (PM) control. Huntington Unit #2 is equipped with low-No, burners and
overfire air for NOx control, an FGD scrubber for SOz control and pulse-jet fabric filters for
PM control.
2.2 Flue Gas Sampling Locations
Information regarding the sampling locations is presented in Table 2-1.
Table 2-1
Sampling Locations
Sample location(s) were verified in the field to conform to EPA Method 1.
See Appendix A.1 for more information.
2.3 Operating Conditions and Process Data
Emission tests were performed while the source/units and air pollution control devices were
operating at the conditions required by the relevant performance specifications. The units
were tested when operating within the load levels required by 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
.a
a : !t r t. a a a ta -
Page 11 of 278G P043AS-0227 22-RT - 1298
I rl
2.4 CEMS Description
Information regarding the monitoring systems is presented in Table 2-2.
Table 2-2
CEMS Information
Unit 1
Flow Teledyne Monitor Labs Model 150 136
COz Thermo Fisher Model 410|Q-ACN 133
SOz Thermo Fisher Model 43|Q-CAN 131
NOx Thermo Fisher Model 42iQ-ACANN L32
co Thermo Fisher Model 48|Q-CAN
Unit 2
Flow Teledyne Monitor Labs Model 150 236
COz Thermo Fisher Model 41OiQ-CAN 234
SOz Thermo Fisher Model 43|Q-CAN 231
NOx Thermo Fisher Model 42|Q-ACANN 232
co Thermo Fisher Model 48|Q-ACN
at
l.: rl I t-aa a a !l - !.
G P04 3AS -0 227 22 -RT - L298 Page L2 of 278
I rl
3.O Sampling and Analytical Procedures
3.1 Test Methods
The test methods for this test program have been presented in Table 1-1. Additional
information regarding specific applications or modifications to standard procedures is
presented below.
3.1.1 EPA Method 2G, Determination of Stack Gas Velocity and
Volumetric Flow Rate with Two-Dimensional Probes
EPA Method 2G is used to measure the velocity pressure and the yaw angle of the flow
velocity vector in a stack or duct using a 2-D probe. Alternatively, these measurements are
made by operating one of the three-dimensional (3-D) probes described in Method 2F,in
yaw determination-only mode. From these measurements and a determination of the stack
gas density, the average near-axial velocity of the stack gas is calculated. The near-axial
velocity accounts for the yaw, but not the pitch, component of flow. The average gas
volumetric flow rate in the stack or duct is then determined from the average near-axial
velocity.
Pertinent information regarding the performance of the method is presented below:
o Method Options:
o None
. Method Exceptions:
o None
. Target and/or Minimum Required Sample Duration: 5 minutes
The typical sampling system is detailed in Figure 3-1.
aa
| .r r !-ta . at..a - ..
G P043AS-0 227 22-Rr - L298 Page 13 of 278
)l
Figure 3-1
EPA Method 2G Sampling Train
GP043AS-0227 22-Kf - 1298 Page 14 of 278
I rl
3.1.2 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 Method2,2F, 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 MTA 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
I rr r .-ra a a .t - ..
G P043AS-0227 22-RT - L298 Page 15 of 278
i
l1i
i-l
l
I
I r
,r. t- ', 1: iiA lL i"j y- S ll?"V ii C E :i
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 serles of pre-weighed lmpingers containing methodology-
specific liquids and silica ge! immersed ln 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:
o Method Options:
o None
r Method Exceptions:
o None
The typical sampling system is detalled in Figure 3-2.
Pacif it-rrp
2l2J fi.1,TA t,eptr" I irni.nt.rn Fowr, La I
G P04 3AS -0 2 27 22-Rr - t29 I Page 16 of 278
I rl
Figure 3-2
EPA Method 4 Sampling Train
taa
I .^ r .-aa a O
G P04 3AS - 0 2 2 7 22 - RT - L29 I
SAT'PIE LINE
(stand.rd tp). VACUUM<r- LNE
BY-PASSVALVE
THERMOCOUPLESlt thtgdpd ) VACUUM
VALVE
[Nx.dpd)
MANOIIETER._-D
Page L7 of 278
o rl
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
(Instru menta I Analyzer Procedu res)
Concentrations of Oz, COz, SOz, NOx, and CO are measured simultaneously using EPA
Methods 3A, 6C, 7E, and 10, which are instrumental test methods. Conditioned gas is sent
to a series of analyzers to measure the gaseous emission concentrations. The performance
requirements of the method must be met to validate the data.
Pertinent information regarding the performance of the method is presented below:
o Sampling is performed using a dilution probe
o A nondispersive infrared analyzer is used to measure COz
o An ultraviolet absorption analyzer is used to measure SOz
o A chemiluminescent analyzer is used to measure NOx
o A gas filter correlation nondispersive infrared analyzer is used to measure
co
o NO and NOz are measured separately and summed to report NOx
emissions
o Gas stratification testing is performed across a grid of 12 points
determined using EPA Method 1 in accordance with 40 CFR Part 60,
Appendix B, PS2 58.1.3.2 and 40 CFR Part 75, Appendix A, 96.5.6.1.
Stratification testing is performed for two minutes per traverse point in
accordance with 40 CFR Part 75, Appendix A, $6.5,6.1(c). If diluent and
pollutant concentrations are within 5o/o of their mean concentrations,
subsequent gas RATA testing is performed at a single point in the stack as
allowed by 40 CFR Paft 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 meter and 2.0 meters from the stack wall,
as required by 40 CFR Part 60, Appendix B, PS2 58.1.3.2 and 40 CFR Part
75, Appendix A, $6.5.6.1(a).
The typical sampling system is detailed in Figure 3-3.
| .r r .- a . a .a - ..
G P04 3AS -0 2 27 22-Rr - t298 Page 18 of 278
I rl
Figure 3-3
EPA Methods 3A (OzlCOz), 6Cr 7E, and 1O Sampling Train
3.2 Process Test Methods
The test plan did not require that process samples be collected during this test program;
therefore, no process sample data are presented in this test report.
a
I. l I .- a t a rt . ..
Exieul
Sand. / C.lbr'bon Gag
F-----------+
I-{aYlli'
ior&ttiSwrxtlilcilriot
YA\f,S
sl
firx tLotrcoilrR0(
lr
.s*pu.m*rs,
iolffatatsKtx 7tilcorltil vaEs
HEATEO
SAUPLE
UNE
MASS FLOIVCONTROLLER/
CAUffi ATICfiI GAS MANIFOLD
G P04 3AS -0 227 22-RT - t298 Page 19 of 278
llr
l
1
4.O Test Discussion and Results
4.L Field Test Deviations and Exceptions
Unit 1 lost load after RATA Run #8 on Aprll 13th. The ninth run was completed on April 14th.
No further fleld deviations or exceptions from the test plan or test methods were identified
by the project manager during thls test program.
4.2 Presentation of Results
The average results are compared to the permit limits in Tables 1-2 and 1-3. Emissions are
reported in units conslstent with those in the appllcable performance specifications.
Additional informatlon ls included in the appendices as presented ln the Table of Contents.
l-iLlntin!t!n Prwer lLant
FacifiCrrp
2023 R.ATA Reprrt
G P043AS-02 27 22-RT - L298 Page 20 of 278
I rl
5.O Internal QA/QC Activities
5.1 QA/QC Audits
The meter boxes and sampling trains used during sampling performed within the
requirements of their respective methods. All post-test leak checks, minimum metered
volumes, and minimum sample durations met the applicable QA/QC criteria, except where
noted in Section 5,2.
EPA Method 3A, 6C, 7E, and 10 calibration audits were all within the measurement system
performance specifications for the calibration drift checks, system calibration bias checks,
and calibration error checks, except where noted in Section 5.2.
The NOz to NO converter efficiency check of the analyzer was conducted per the procedures
in EPA Method 7E, Section 8.2.4. The conversion efficiency met the criteria, except where
noted in Section 5.2.
5.2 QA/QC Discussion
All QA/QC criteria were met during this test program.
5.3 Quality Statement
Montrose is qualified to conduct this test program and has established a quality
management system that led to accreditation with ASTM Standard D7036-04 (Standard
Practice for Competence of Air Emission Testing Bodies). Montrose pafticipates in annual
functional assessments for conformance with D7036-04 which are conducted by the
American Association for Laboratory Accreditation (A2l-A). All testing performed by Montrose
is supervised on site by at least one Qualified Individual (QI) as defined in D7036-04
Section 8.3.2. Data quality objectives for estimating measurement uncertainty within the
documented limits in the test methods are met by using approved test protocols for each
project as defined in D7036-04 Sections 7.2.L and 12.10. Additional quality assurance
information is included in the report appendices. The content of this repoft is modeled after
the EPA Emission Measurement Center Guideline Document (GD-043).
' la
| .r r r- t a .a - .!
G P043AS -0 22 7 22-Rr - t298 Page 2l of 278
Appendix A
Field Data and Calculations
G P043AS-0227 22-Nl - 1298 Page 22 of 278
Appendix A.1
Sampling Locations
G P043AS-022 7 22-RT - L298 Page 23 of 278
PacifiCorp Huntington Power Plant Sampling Locations
Pollutant Stratification Test Points
Stack Cross Section (A-A)
oH
Stack Cross Section (A-A)
+++ + + +++
L21 4 1 3 21
Unlt
Diameter (D)
Upstream Distance (A)
Downstream Distance (B)
Sample Point Distances from Stack Wall
Traverse Point 1
Traverse Point 2
12
323.3' 322.7">220' >220',
>266', >266',
14.1" 14.1"47.3" 47.3"
Volumetric Flow Rate Sample Points
Upstream Distance (A) >220'
Downstream Distance (B)>266',
Sample Point Distances from Stack Wal!
Unlt
Diameter (D)
Traverse Point 1
Traverse Point 2
Traverse Point 3
Traverse Point 4
1
323.3"
10.4"
33.9"
62.7"
104.5"
2
322.7"
>220'
>266',
10.4"
33.8"
62.5"
104.3"
G P04 3AS -02 27 22 -RT - L298 Page 24 of 278
Appendix A.2
RATA Results
G P043AS -0227 22-RT - L298 Page 25 of 278
Appendix A.2.1
Unit 1
G P043AS-0227 22-RT -L298 Page 26 of 278
PaclflCorp
Huntln$on 1
Low Load Flow RAIA
4h2l20r?
Parameter:Exheust Gas Flow (wscfhl
Run #
1
2
3
4
5
6
7
8
9
10
LI
L2
StartTlme StopTlme UnftLoad
8:52 9:00 190
9:02 9:10 193
92LZ 9:20 191
9:26 9:34 f92
9:35 9:44 191
9146 9:54 192
9:56 10:04 f90
10:06 10:14 195
10:16 10t24 190
Difference Use?
-52,000 Yes
-439,000 Yes
-196,000 Yes
274,000 Yes
145,000 Yes
458,000 Yes
-269,000 Yes
-473,W Yes
777,ON Yes
No
No
No
WAF Applled?
RATA Reiults
Yes
Number of Runs: 9
T-value 2.305
Standard Deviation 42E,&O
Confidence Coefficient 325,454
Relative Accuracy (%RM) 0.98%
Bias Adiustment Factor 1.000
RA<10% (5eml-Annual)
RM
36,038,000
35,581,000
3s,55&000
36,199,000
36,002,000
35,412,000
35,409,000
3S,919,000
35,878,000
CEM
36,090,000
36,020,000
35,764,000
35,925,00O
35,856,0@
35,954,000
35,678,000
35 392,0@
35,101,000
AvGragc 35,889,555 t5,a64,444L92 25,LL,.
G P04 3AS - 0 2 27 22- Rr - t29 I Page 27 of 278
I
PecifiCorp
Huntindon 1
HiSh Load Flow RATA
0llr - 41L41202t
Paaameter:E$aust Gas Flow (wssftl
Run s
1
2
3
4
5
6
7
8
9
10
lt
t2
6il2 6:50
7:06 7:26
7:49 8:09
8:26 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 12:10
6:12 6:32
St rtTime Stopl'ime Unitload Oifference Usc?
2,129,000 Yes
2,427,000 Yes
1,891,000 Yes
2,140,000 Yes
2,575,000 Yes
826,000 Yes
Z,L7o,OOO Yes
1,980,000 Yes
1,134,000 Yes
No
No
No
wAF Applied?
RATA Results
Number of Runs: 9
T-value 2.306
Standard Deviatlon 576,598
Confidence coefficient 443,212
Relative Accuracy (%RM) 2.99%
Bias Adjustment Factor 1.025
RA<10% (Semi-Annual)
493
493
493
496
495
492
485
447
492
RM
79,87L,000
78,766,000
78,254,000
78,407,000
78,860,000
78,035,000
79,382,000
79,550,000
79,738,000
CEM
77,?42,000
76,339,000
76,363,000
76,267,OO0
76,28s,000
77,209,000
77,2r2,OO0
77,570,000
78,604,000
Average 492 74,9E/,774 77,065,667 L,9t9,LLt
GP043AS-0227 22-Rr - t298 Page 28 of 278
Job Code PROJ-022722
Pacificorp, Huntington Unit 1
Test Date: 4ll3 - 4h412O2,
Parameter:CO2 (%vw)
Run #
1
2
3
4
5
5
7
8
9
10
11
L2
13
L4
15
Load
493
493
493
496
49s
492
485
487
492
RM
10.9
rt.2
to.7
11.1
tL.2
11.0
10.8
10.8
11.0
CEM
10.6
10.8
10.9
10.9
10.9
10.8
10.5
10.6
10.7
Start nme End Time
6:L2 6:50
7:OG 7:26
7:49 8:09
8:25 8:45
9:O2 9:22
9:59 10:19
11:15 11:35
11:50 t2:to
6:L2 6:32
Difference Used?
0.3 x
0.4 x
-0.2 x
0.2 x
0.3 x
0.2 x
0.2 x
0.2 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: OZ I COz%
9
2.306
0.2
0.1
3.L%
nla
n/a
nla
0.3
Relative Accuracy Limit:
RA<7.5%or !0.7%
Average o.210.811.0492
Parameter:NOx (lblmmBtul
Run #
1
2
3
4
5
6
7
8
9
10
11
t2
13
t4
15
Load
493
493
493
496
495
492
48s
487
492
RM
0.2r4
o.L92
0.193
0.184
0.186
0.195
0.203
0.205
0.201
CEM
0.223
0.198
0.196
0.190
0.194
0.200
0.208
0.277
o.zL\
Start nme End Time
5:12 5:50
7:OG 7:26
7:49 8:09
8:26 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 12:10
6:t2 6:32
Dlfference Used?
-0.011 x
-0.006 x
-0.003 x
-0.005 x
-0.008 x
-0.005 x
-0.005 x
-0.005 x
-0.010 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
2.306
0.003
0.002
4.4%
nla
n/a
1.000
Relative Accuracy Limit:
RA<7.5% or 10.015 lblmmBtu
Average 492 0.197 o.20tl -0.007
Parameter:SO2 lppmvw)
Run fl
1
2
3
4
5
6
7
8
9
10
11
72
13
14
15
Load
493
493
493
496
495
492
485
487
492
RM
23.1
23.7
22.r
22.6
2L.O
21.5
20.3
22.4
23.0
CEM
20.9
2t.o
20.6
20.4
18.8
19.3
19.1
19.9
23.?
Start nme End Time
6:12 6:50
7:06 7:25
7:49 8:09
8:26 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 12:10
6:t2 6:32
Difference Used?
2.2
2.7
1.5
2.2
2.2
2.2
t.2
2.5
-o.2
RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coeff icient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: SO2 / NOx ppm
9
2.305
0.9
0.7
L7.4%
nla
nla
1.090
Relative Accuracy Limit:
RA<7.5% or *12.0ppm
Average 20,4
G P04 3AS-02 27 22 -RT - 1298
492 22.2 1.8
Page 29 of 278
lobCodePROI422722
Pacificorp, Huntington Unit 1
Tesr Date: 4ll3 - 4lL4l2O23
Parameter:NOx (ppmvwl
Run il
L
2
3
4
5
5
7
8
9
10
11
L2
13
T4
15
Load
493
493
493
496
495
492
485
487
492
RM
108.4
99.9
95.8
95.1
97.3
99.5
102.3
103.0
L02.4
CEM
111.3
99.8
99.1
96.5
98.4
100.3
LO2.2
103.8
104.9
Start Time End Tlme
6:L2 5:50
7:06 7:26
7:49 8:09
8:26 8:45
9:O2 9:22
9:59 10:19
11:15 11:35
11:50 L2:LO
6:12 6:32
Difference Used?
-2.9 x
0.1 x
-3.3 x
-1.5 x
-L,T X
-0.8 x
0.1 x
-0.8 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
20% RM or 10%EL
9
2.306
7.2
1.0
2.4%
nla
n/a
n/a
Average 492 1(n,4 101.8 -t,4
Parameter:SO2 (lblmmBtul
Run fi
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
[oad
493
493
493
495
495
492
485
487
492
RM
0.053
0.054
0.052
0.051
0.055
0.059
0.055
0.062
0.053
CEM
0.059
0.058
0.057
0.055
0.052
0.054
0.054
0.056
0.055
Start Time End Tlme
6:t2 5:50
7:06 7:25
7:49 8:09
8:26 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 12:10
6:L2 6:32
Difference Used?
0.004 x
0.006 x
0.005 x
0.005 x
0.004 x
0.005 x
0.002 x
0.006 x
-O.OO2 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS2: SO2 / NOx ppm
9
2.306
0.003
0.002
9.6%
n/a
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 492 0.061 0,057 0.004
G P043AS -02 27 22-RT - 7298 Page 30 of 278
Job Code PROI-022722
PacifiCorp, Huntington Unlt 1
Test Date: 4lL3 - 4lL4l2O2?
Parameter:Nox llb/hr)
Run #
1
2
3
4
5
6
7
8
9
10
11
L2
13
L4
15
Load
493
493
493
496
495
492
485
487
492
RM
1033.5
939.5
894.8
890.7
915.9
927.L
959.7
978.2
974.7
CEM
1033.7
909.9
903.7
879.4
896.7
924.t
94L.9
967.2
98s.0
Start Time End Time
6:L2 6:50
7:06 7:26
7:49 8:09
8:26 8:45
9:02 9:22
9:59 10:19
11:15 11:35
11:50 t2:L0
6:12 6:32
Difference Used?
-0.1 x
29.7 x
-8.9 x
11.3 x
79.2 x
3.0 x
27.8 x
L7.O x
-10.3 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
14.8
It.4
2.2%
nla
nla
nla
Relative Accuracy Limit:
ZO%RM or 7O%EL
Average 492 947.1 937.1 9.9
Parameter:SO2 (lb/hr)
Run #
7
2
3
4
5
6
7
8
9
10
11
72
13
t4
15
Load
493
493
493
496
495
492
485
487
492
RM
305.4
311.0
287.0
294.3
275.9
278.5
267.5
295.1
304.9
CEM
269.8
255.5
267.7
257.9
238.7
247.2
244.7
256.L
303.1
44.5
25.3
35.4
37.2
31.3
22.8
40.0
1.8
Start Tlme End Time
6:L2 5:50
7:06 7:26
7:49 8:09
8126 8:45
9:Q2 9:22
9:59 10:19
11:15 11:35
11:50 72:70
6:L2 6:32
Dlfference Used?
35.6 x
RATA Results
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Conf idence Coeff icient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS6: Mass Emissions
9
2.305
12.8
9.8
13.9%
n/a
nla
nla
Relative Accuracy Limit:
20% RM or 10%EL
Average 492 291.3 260.6 30.7
G P043AS -02 27 22-Rr - L29B Page 31 of 278
Job code PRot422722
Pacificorp, Huntington Unit 1
Test Date: 4ll3 - 4lt4l2o23
Parameter:CO (ppmvw)
Run #
1
2
3
4
5
5
7
8
9
10
11
L2
13
L4
15
Load
493
493
493
495
495
492
485
487
492
RM
143.9
L97.4
13s.8
253.1
195.9
189.0
67.4
61.3
39.0
CEM
148.9
185.1
129.6
258.9
190.1
183.7
53.5
55.8
37.5
Start Time End Time
6:t2 5:50
7:06 7:26
7:49 8:09
8:25 8:45
9:O2 9:22
9:59 10:19
11:15 11:35
11:50 12:10
6:t2 6:32
Difference Used?
-5.0 x
72.3 x
6,2 x
4.2 x
6.8 x
5.3 x
3.8 x
4.5 x
L.5 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS4A: CO ppm <200
Relative Accuracy Limit:
10% RM or 5%EL or I d | +Cc<sppm
9
2.306
4.6
3.5
5.5o/o
nla
nla
n/a
Average 492 143.8 139.4 4.4
Parameter:co (lblmmBtul
Run #
r
2
3
4
5
6
7
8
9
10
7r
12
13
L4
15
[oad
493
493
493
496
495
492
485
487
492
RM
o.t73
0.231
0.t67
0.309
0.230
o.726
0.082
0.074
o.047
CEM
0.183
0.223
0.156
0.310
0.728
0.223
0.079
0.070
0.046
Start Time End Time
6:L2 6:50
7:OG 7:25
7:49 8:09
8:25 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 LZ:IQ
6:L2 6:12
Difference Used?
-0.010 x
0.008 x
0.011 x
-0.001 x
0.002 x
0.003 x
0.003 x
0.004 x
0.001 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O PS6: Mass Emissions
9
2.306
0.006
0.00s
4.0%
n/a
nla
nla
Relative Accuracy Limit:
ZO%RM or IO%EL
Averat€492 o.L7t 0.169 o.002
Parameter:co (lblhr)
Run #
1
2
3
4
5
5
7
8
9
10
\t
t2
13
74
15
Load
493
493
493
496
49S
492
485
487
492
RM
835.5
1130.1
772.4
t499.5
LLZ8.7
7072.5
389.1
354.5
226.L
CEM
844.5
LOL7.4
712.9
1458.6
1046.5
1000.0
340.3
303.7
2L4.3
Start Time End Time
6:72 6:50
7:OG 7:26
7:49 8:09
8:26 8:46
9:02 9:22
9:59 10:19
11:15 11:35
11:50 12:70
6:LZ 6:32
Difference Used?
-8.9 x
LL2.7 x
59.5 x
40.9 x
82.1 x
72.5 x
48.8 x
50.8 x
11.8 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P5O PS5: Mass Emissions
9
2.305
36.3
27.9
9.7%
nla
n/a
^/a
Relative Accuracy Limit:
2O%RM or |O%EL
Average
G P043AS -0 22 7 22 -Nf - L298
492 423.2 770.9 52.2
Page 32 of 278
Appendix A.2.2
Unit 2
G P04 3AS -0227 22-RT - L298 Page 33 of 278
PacmCom
Huntlndon 2
tow Lord Flow RATA
4/,.tl202?
Parameter:Exhaust 6as Flow (wscf,tl wAFApplled? No
Run* StartTime StopTime Unitload RM CEM DlffGrence Use? MTARcaults
I L4i29 l4i?4 188 36,491,000 37,670,000 -1,179,000 Yes NumberofRuns: 9
2 14:37 14.43 189 36,634,000 37,759,000 -1,125,000 Yes T-value 2.306
3 14i45 14:51 188 36,492,000 37,496,000 -1,004,000 Yes Standard Deviation 459,354
4 15:15 l5i2l la7 37,f62,000 37,559,000 -397,000 Yes Confidence Coefficient 351090
5 15:23 15:29 188 37,069,000 37,097,000 -2&000 Yes RelativeAccuracy(%RM) ?.69'/$
6 15:31 15:37 186 36,722,000 37,328,000 -606,000 Yes gias Adjustment Factor 1.000
7 15:39 15:45 190 37,262,000 38,236,000 -974,000 Yes
8 15:47 15:53 189 37,569,000 37,535,000 34,000 Yes P75 Relative Accuracy Sttnd.rds
9 15:55 16:01 188 35,962,000 37,431,000 469,000 Yes RA<7.5% (Annual)
10 No RA<10% (Semi-Annual)
11 No
AYerete 188 t6,929,222 37,567,889 €38,557
No
G P043AS-0227 22-Rr -L298 Page 34 of 278
PacifiCorp
HuntinSton 2
HiSh Load Flow RATA
4lL4l202t
Perameter:Exhaust Gas Flow lwscftl WAF Applied? Yes
Run# StartTime StopTime UnitLoed RM CEM Difference Use? RATAResults
1 9:08 9:46 481 82,599,000 82,390,000 209,000 Yes Number of Runs:
2 10:00 10:20 480 83,768,000 82,204,000 1,564,000 Yes T-value
3 10:36 10:55 483 84,600,000 81,980,000 2,620,000 Yes Standard Deviation 719,963
4 ll:12 11:32 486 A2,204,000 80,058,000 2,L46,000 Yes Confidence Coefficient 553,411
5 11:48 12:08 484 82,736,000 80,563,000 2,173,000 Yes Relative Accuracy (%RM) 2.95%
6 12:22 72:42 479 82,875,000 80,382,000 2,493,000 Yes Bias Adjustment Factor 1.023
7 72i59 13:19 4?9 82,650,000 80,359,000 2,291,000 Yes
8 13:32 13:52 480 82,930,000 81,144,000 1,785,000 Yes P75 Relative Accuracy Standards
914:o714:2747882,835,ooo8o,994,ooo1,841,oooYesffi
10 No RA<10% (SemFAnnual)
11 No
AYerage 481 83,021,889 81,119,333 1,902,555
9
2.305
t2
G P04 3AS -0 227 22 -Rr - L298 Page 35 of 278
Job Code PRO1422722
PacifiCorp, Huntin8ton Unit 2
Test Date: 4ll4l23
Parameter:CO2 (%vw)
Run #
1
2
3
4
5
5
7
8
9
10
L7
t2
13
L4
15
Load
48t
480
483
485
484
479
479
480
474
RM
70.4
10.3
10.4
10.5
10.6
10.s
10.5
10.5
10.4
CEM
10.6
10.5
10.5
11.0
10.9
10.8
10.8
10.7
70.7
Start Time End Time
9:08 9:46
10:00 10:20
10:35 10:56
7L:12 LL:32
11:48 12:08
72:22 L2:42
72:59 13:19
73:32 13:52
74:07 14:27
Difference Used?
-o.7 x
-0.2 x
-0,2 x
-0.4 x
-0.3 x
-0.3 x
-0.3 x
-0.2 x
-0.3 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: 02 / CO2 %
9
2.306
0.1
0.1
3.1%
nla
nla
nla
Relative Accuracy Limit:
RA<7s% or !O.7oA
Average 10.5It81 LO,7 -0.3
Parameter:NOx (lblmmBtu)
Run S
1
2
3
4
5
6
7
8
9
10
11
12
13
T4
15
Load
481
480
483
486
484
479
479
480
474
RM
0.232
o.234
0.236
0.210
0.276
0.218
0.223
0.228
o.227
CEM
0.235
o,239
0.238
0.272
0.218
0.222
0.227
0.233
o.237
Start Time End Time
9:08 9:46
10:00 10:20
10:36 10:56
ll:72 t7:32
11:48 12:08
f2:22 L2:42
72:59 13:19
!3:32 13:52
14:07 14:27
Difference Used?
-0.003 x
-0.005 x
-0.002 x
-0.002 x
-0.002 x
-0.004 x
-0.004 x
-0.005 x
-0.004 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coeff icient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: NOx lb/mmBtu
9
2.306
0.001
0.001
2.0%
nla
nle
1.000
Relative Accuracy Limit:
RA<7.5% or 10.015 lb/mmBtu
Averate tl81 o.225 o,224 -0.003
Parameter:SO2 lppmvwl
Run #
1
2
3
4
5
6
7
8
9
10
11
t2
13
L4
15
Load
481
480
483
485
484
479
479
480
478
RM
37.0
31.1
28.8
24.8
23.3
7L.2
22.8
2t.3
23.8
CEM
37.8
31.8
29.5
25,2
24.0
2L.a
23.s
22.7
24_4
-0.8
-0.7
-o.7
-o,4
-o.7
-0.5
-o.7
-0.8
-0.5
9
2.306
0.1
0.1
2.9%
n/a
nla
1.000
Start Time End Time
9:08 9:46
10:00 10:20
10:36 10:56
7l:12 77:32
Ll:48 12:08
12:22 72:42
L2:59 13:19
73:32 73:52
l4:O7 14:27
Dlfference Used?RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P75, Annual: SO2 / NOx ppm
Relative Accuracy Limit:
RAs7.5% or t12.0ppm
Averate
G P04 3AS -0 2 27 22-P.T - 1298
4At 26.O 26.7 -o.7
Page 36 of 278
Job Code PROJ{22722
PacifiCorp, Huntington Unit 2
Test Date: 4lL4l23
Parameter: NOx (ppmvw)
Run #
1
2
3
4
5
5
7
8
9
10
11
t2
13
14
15
Load
481
480
483
485
484
479
479
480
478
RM
r72.1
1r2.3
114.6
104.1
106.1
105.9
109.1
lLL.7
110.1
CEM
Lts.2
115.9
LLl.9
107.9
110.2
LL7.7
113.8
115.3
115.1
Start Time End Time
9:08 9:45
10:00 10:20
10:36 10:56
IL:LZ tL:32
11:48 12:08
72:22 12:42
12:59 13:19
13:32 13:52
14:07 L4:27
Difference Used?
-3.1 x
-4.6 x
-3.3 x
-3.8 x
-4.7 x
-4.8 x
-4.7 x
-5.1 x
-5.0 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS2: SO2 / NOx ppm
9
2.306
0.7
0.5
4.4%
n/a
n/a
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 4,3109.6 113.9
Parameter:So2 (lb/mmBtul
Run #
1
2
3
4
5
5
7
8
9
10
11
t2
13
L4
15
Load
48t
480
483
486
484
479
479
480
478
RM
0.107
0.090
0.083
0.070
0.066
0.060
0.065
0.061
0.058
CEM
0.107
0.090
0.083
0.059
0.055
0.060
0.05s
0.062
0.068
Start Tlme End Tlme
9:08 9:45
10:00 10:20
10:36 10:56
L1:L2 t7:32
11:48 12:08
L2:22 L2t42
12:59 13:19
13:32 13:52
t4:07 L4t27
Difference Used?
0.000 x
0.000 x
0.000 x
0.001 x
0.000 x
0.000 x
0.000 x
-0.001 x
0.000 x
RATA Results
Number of Runs:
T-value
Standard Deviatlon
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS2: SO2 / NOx ppm
9
2.306
0.001
0.000
os%
nla
n/a
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Averate It81 o.o74 o.o74
G P043AS-0 22 7 22-RT - t298 Page 37 of 278
Job Code PROJ{22722
PaclfiCorp, Huntington Unit 2
Test Date: 4/14123
Parameter:NOx (lblhrl
Run fi
L
2
3
4
5
6
7
8
9
10
IL
L2
13
t4
15
Load
481
480
483
486
484
479
479
480
478
RM
1106.0
1123.3
1158.1
LO22.2
1048.0
1057.9
LO76.7
1101.3
1089.2
CEM
1133.3
1147.6
7L54.4
1031.8
1059.8
7072.7
1091.7
1L27.0
1113.3
Start Time End Time
9:08 9:46
10:00 10:20
10:35 10:56
Ll:!2 L7:32
11:48 12:08
12:22 12:42
12:59 13:19
13:32 13:52
14:07 14:27
Difference Used?
-27.3 x
-24,3 x
3.7 x
-9.5 x
-11.8 x
-14.8 x
-15.0 x
-25.7 x
-24.L x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O PS6: Mass Emissions
9
2.306
10.0
7.7
2.2%
nla
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Average 481 1087.0 1103.5 -16.5
Parameter:soz (lblhrl
Run #
L
2
3
4
5
5
7
8
9
10
11
t2
13
L4
15
[oad
481
480
483
486
484
479
479
480
478
RM
507.6
433.4
404.7
339.0
320.8
292.4
312.9
294.0
327.6
CEM
515.3
433.5
402.L
334.9
320.4
290.6
313.5
298.2
328.3
Start Time End Tlme
9:08 9:45
10:00 10:20
10:35 10:56
7L:L2 17:32
1L:48 12:08
12:22 L2:42
72:59 13:19
13:32 13:52
L4tO7 t4:27
Dlfference Used?
-8.7
-o.2
2.6
4.1
0.4
1.8
-0.6
-4.2
-0.7
RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P6O PS6: Mass Emissions
9
2.306
3.8
2.9
L.O%
nla
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Avera8e 481 359.2 359.8 -0.5
G P04 3AS - 0 22 7 22-Rr - L298 Page 38 of 278
Job Code PROJ-022722
PacifiCorp, Huntington Unit 2
Test Date: 4/14123
Parameter:CO lppmvwl
Run #
1
2
3
4
5
5
7
8
9
10
11
L2
13
L4
15
Load
481
480
483
485
484
479
479
480
474
RM
59.9
34.3
38.3
L74.9
183.9
14s.6
234.7
155.8
191.5
CEM
50.0
29.0
34.3
111.8
183.1
L40.4
229.9
150.4
184.9
Start Time End Time
9:08 9:45
10:00 10:20
10:36 10:56
!L:72 l!:32
11:48 12:08
72:22 t2:42
12:59 13:19
73:32 13:52
74:07 t4:27
Difference Used?
9.9 x
5.3 x
4.0 x
3.1 x
0.8 x
5.2 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS4A: CO ppm <200
Relative Accuracy Limit:
10% RM or 5%EL or I d | +CC<Sppm
4.8
5.4
6.6
x
x
x
9
2.306
2.s
1.9
5.4o/o
n/a
n/a
n/a
Average 481 128.8 123.8 5.0
Parameter:CO (lb/mmBtul
Run #
1
2
3
4
5
5
7
8
9
10
11
t2
13
14
15
Load
481
480
483
485
484
479
479
480
478
RM
0.076
0.044
0.048
0.141
o.224
0.181
0.292
o.L94
o.241
CEM
0.052
0.035
o.o42
0.133
0.220
0.170
0.279
0.184
0.226
Start Tlme End Tlme
9:08 9:46
10:00 10:20
10:36 10:55
7l:12 7!:32
11:48 12:08
t2:22 t2:42
12:59 13:19
13:32 13:52
14:07 L4:27
Difference Used?
0.014 x
0.008 x
0.005 x
0.008 x
0.008 x
0.011 x
0.013 x
0.010 x
0.015 x
RATA Results
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS5: Mass Emissions
9
2.306
0.003
0.002
7.9%
n/a
nla
n/a
Relative Accuracy Limit:
20% RM or 10%EL
Avera8e It81 0.151 0.150 0.010
Parameter:co (lb/hr)
Run f
1
2
3
4
5
5
7
8
9
10
rT
t2
13
L4
15
Load
481
480
483
486
484
479
479
480
478
RM
359.8
209.1
235.7
685.7
LLO6.2
877.1
L4tO.2
939.s
1153.4
CEM
299.3
173.6
203.9
650.2
1071.6
82r.7
1341.0
885.1
1088.4
60.s
35.5
31.8
36.5
34.6
55.4
69.2
s3.4
55.0
9
2.305
t4.6
L7.2
7.8%
n/a
n/a
nla
Start mme End Time
9:08 9:46
10:00 10:20
10:36 10:55
L7:72 7l:32
11:48 12:08
L2:22 t2:42
12:59 13:19
73132 !3:52
74:07 74:27
Difference Used?RATA Results
x
x
x
x
x
x
x
x
x
Number of Runs:
T-value
Standard Deviation
Confidence Coefficient
Relative Accuracy (%RM)
Emission Limit
Relative Accuracy (%EL)
Bias Adjustment Factor
P60, PS6: Mass Emissions
Relative Accuracy Limit:
20% RM or 10%EL
Average
G P04 3AS -02 27 22 -RT - t29 I
48t 775.3 726.2 49.1
Page 39 of 278
Appendix A.3
Field Data
G P043AS-0227 22 -Rr - t298 Page 40 of 278
Appendix A.3.1
Unit 1
G P04 3AS - 0 2 2 7 22 - RT - t29 8 Page 4L ot 278
Appendix A.3.1.1
Low-Load Flow Data
G P04 3AS -0 2 2 7 22- RT - L298 Page 42 of 278
Client Pacificorp
Unit lD Huntington I
Load low
EPAMethod3&4Data
AH
Tm
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H2O)
O, (/.vd)
CO2 (%vd)
Volume of Water Condensed (mL)
volume of Stack Gas Collected (dcf)
Meter Calibration Factor (unitless)
Pressure Differential Across Orifice ("HrO)
Temperature at Gas Meter ('F)
Calculations
Pn Absolute Pressure at Gas Meter ("Hg)
T. Absolute Temperature at Gas Meter ('R)
Vw(*d) Volume of Water Condensed (scf)
Vm(std) Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B*""t Saturated Moisture Content (y"/100)
Bw Measured Moisture Content (/"/100)
B*" Stack Gas Moisture Content (y./100)
23.62
-4,50
8.5
10.5
23.62 23.52
-4.50 -4.50
8.5 8.5
10.5 10.5
85.9 8s.9 8s.9
42.OL2 42.012 42.OtZ
0.9783 0.9783 0.9783
1.8 1.8 1.8
52 62 62
23.75 23,75 23.75
522 522 522
4.04 4.04 4.O4
32,99 32.99 32.99
41.6 41.8 47.9
0.102 0.103 0.104
0.109 0.109 0.109
0.102 0.103 0.104
lsaturated) {Saturated) (Saturated)
23.52 23.62 23.62
-4.50 -4.50 -4.50
8.5 8.5 8.5
10.5 10.5 10.5
23.52 23.62 23.62
-4.50 -4.50 -4.50
8.5 8.5 8.5
10.5 10.5 10.5
99.9 99.9
50.558 50.568
0.9783 0.9783
1.8 1.8
68 58
23.75 23.75
578 528
4.70 4.70
39.25 39.25
41.9 41.8
0.104 0.103
0.707 0.L07
0.104 0.103
{saturated) (saturated)
99.9 99.9 99.9
s0.568 s0.s68 s0.568
0.9783 0.9783 0.9783
1.8 1.8 1.8
58 68 58
99.9
50.558
0.9783
1.8
68
23.75 23.75 23.t5
528 528 528
4.70 4.70 4.70
39.26 39.25 39.26
42.2 42.1 42.1
0.105 0.105 0.105
0.L07 0.107 0.107
0.105 0.105 0.105
(Saturated) (S.turated) {Saturated)
23.75
528
4.70
39.25
41.9
0.104
0.107
0.104
(sarunted)
G P043AS - 02 27 22-RT - L298 Page 43 of 278
Low Load Run f1
Locatlonr Huiltintton 1
tosd (MW: 190
D*e: 41721202,
Start Timc: 8:52
EndTimc: 9:0O
Probe / Gas Data
Probe fl Re: 0 deSreet
ProbC f2 REo: 0 dGgrees
Piobe *1 Rsrc: -33 deSrees
Probe f2 Rsro: -12 detre.s
8*: 0.1018 %/100
Md: 30.02 lb/lb-mol.
M,: 28.E0 lbllb.mol.
Pb,r 23.62 ln Hg
P.: 4.50 ln HzO
P.: 23,29 ln Ht
9(COr: 10S 96
%q,___ 8s%
96CO: 0.0 %
Flow RATA Traverse Data
Polnt lD Probe lD
Corrrcted
St.cl T.mp Yaw An3I€ YawAngle P1-P2
(Fl (dcrl O-lderl (in H,0)
Unsdjusted Replacment Point U3cd rWAf
tulal Velclty Axial Veloclty tor Point5
v.(fv*cl v.(lved wAF? Usedc"
001 105 0 t.2 0.14 0.424 24.209
oo2 lo7 0 t.2 0.16 0.8240 2S.903
003 L07 2.2 0.16 0.8240 25.890
004 107 2.2 0.15 0.8240 25.068
00s 106 0 1.7 0.14 0.8240 24.209
offi 101 o 16 0 8ra0 ?5 859
007 107 0.16 0.8240 25.890
008 108 0 L.2 0.15 0.4240 25.103
oo9 106 4 7.3 o_ 13 0.8160 22.920
01.0 105 4 0.1 0.8160 23.042
011 t07 6.3 0.15 0.8160 24.693
o12 to7 0 3.3 0.15 0.8160 24.801
o13 107 o1 0 8160 )) 1)S
014 108 2 5.3 0.13 0.8160 23.049
015 LO7 5.3 o.t4 0.8150 23.898
016 107 4 o 15 0 8160 )t777
lv€rages 106.9 1.3 3.5 0.15 0.8200 2{./l55 nla ala
GP043AS-0227 22-RT - 1298 Page 44 of 278
Probc fl Re: 0 dcgrecs
Prolf, f2 Re: 0 degreas
Prcb€ fl &E: -33 degrecs
Probe fi2 R.ro: -1J dcgreas
B$r 0.1027 %/100
Mdr 30.02 lbllb-molc
M.: ________l!!!! lb/b-mol.
Pb; 23.52 ir Ht
Pt: 4.50 in H2O
Pr: 23.29 ln Ht
t{COr: 105 %
,,LO2: 8.5 %
9{CO: 0.0 X
: E1'0 %
Low Load Run #2
Lo@tion: Huntlngton 1
t@d (Mlir): r93
Date: 4/1212023
Start lime: 9:02
EndTlme: 9:10
Probe / Gas Data
Unadiusted Results
lavt): 24.17 ftl*<
Clsw: 15,940,241 wsdlhr
Adjusted Results
Va(avgl: 23.93 ft/sec
Clsw: 35,580,841 mct/hr
103
Flow RATA Traverse Data
Poirt lD Probe lD StackTamp
(Fl
Corrccted
YrwAnile YawAnd. P7-P2
(derl (L (derl {in H,0}q
Un.dlustcd RCphement Point Usad fwAF
Axlrl Vclcfay Axhl velGlty lot Pointt
V. (ft/se.l V. (lV*.} wAF? u*d
001 106 0 .2 0.13 o.424 23.333
oo2 106 0 .2 o.14 o.4240 24 )14 n/a nla
003 106 2 0.16 0.8240 25.885
ou 106 0 2 0.15 0.8240 25.063
005 106 I 2.2 0.15 o.8240 25 OS1
006 lo7 o o 1s 0.8240 25.086 nla nla
007 t08 0 1.2 0.16 0.8240 2S.93r
oo8 t08 I 2.2 0.15 0.8240 25.09S
009 107 2 5.3 o_12 0 8160 )) 1)9
010 108 0.13 0.8160 23.053
011 108 0 3.3 0.13 0.8150 23.tt4
108 I 4.3 0.15 0.a150 24_799
013 107 I 4.3 o.72 o.4160 22.162
014 108 1 4.1 0.13 o c160 23.047
015 108 3 0.74 0.8160 23.923
o16 108 2 0.15 0.8150 24.763
rverage3 to7.2 0.8 3.1 0.14 0.8200 24.164 nla nla
G P04 3AS -0 2 27 22 -RT - L29 I Page 45 of 278
Low Load Run #3
Locatlon: Huntintton 1
L@d (MW): 191
oate: 4lluzo23
StartTlme: 912
EndTim.: 9:20
Probe / Gas Data
Probe fl Re: 0 degrces
Prcbr f2 Re: 0 degees
Probe rn &@: -33 deStcer
Probef2&ro: -r-:t dctters
B*: 0.10, %/100
Md: 30.02 lb/lb.mole
M.r 28, lb/lb.mole
Pb.: 23.52 in Ht
Pt: 4.50 in X2O
Pr: 23.29 in H8
%COr: 105 9{
O{ gs'k
%COt 0.0 %
81.0 %
Flow RATA Traverse Data
Polnt lo Prob. lD
Corrcct€d
sta*T.mp YawAngle YlwAngle
lcl lA.,l A ld.d
P1-?2
Unrdrusted Rcplacemcnt Point Uscd # wAF
Airl Velo.ity Axlal Veloclty for Poirts
V rftlo.l v lftlk.l WAF? U..da
001 107 0.14 o.424 24.240
002 108 L,2 0.17 o.4240 26.134
oo3 108 2.2 0.14 0.8240 24.249
OM loa 3.2 0.15 0.8240 25.079
005 107 1)013 0.8240 23.127
006 to7 3.2 0.14 o alao )t )o7
oo7 107 2.2 0.14 0.8240 24.22't
008 107 1.2 0.1s 0.8240 25.091
009 106 4.3 0.12 0 8160 47
010 108 4.3 0.13 0.8150 23.092
011 108 5.3 o.t4 0.8160 23.924
o72 108 4.3 0.15 0.E160 )t 904
o13 107 5.3 o.L2 0.8160 22.L34 nla
014 108 s3 o.14 0.8160 23.924
015 108 5.3 0.15 0.8160 )4764
016 108 4.3 0.15 0.8160 24.804
107.5 1.3 3.5 0.14 0.8200 24.112 nla nla
G P043AS - 0 22 7 22-RT - L298 Page 46 of 278
Low Load Run #4
LGation: Huntlngton 1
Load (Mwl:
oatci 41721m23
StanTimc: 9,26
End Time:
Probe / Gas Data
Probc#lReo: 0 de$er
Prob€ #2 Rei 0 degrees
Prob€ *1 Rs6r -33 degees
Probe f2 RsLo: -1J dc$ees
B*: 0.1037 %/100
Md: 30.02 lb/b-mol.
M,: 2E, tb/tEmote
Ph,: 23,52 in Hg
Pr: -4.50 ln H2O
Pr: 23.29 ln Hg
%CO2t ,.O.S %
O2t 8,5 %
%COr 0.0 %
| 81.0 t{
Flow RATA Traverse Data
Polnt lD Probe lD
Corrrcted
St..lTemp YawAngle YawAngle Pl-P2
(F) (drr) O. (d.8) (in H,0)
Unadrustcd R.plaemcnt Point Usld *WAF
Ari.lvelctty Axl.lveloclty for Points
V.(fV5s) V.(ltl5ecl WAF? uiGdc-
001 2 106 0 0.824 23.337
002 2 to7 2.2 0.17 0.8240 26.697
003 108 2 3.2 0.15 o_4240 25.079 n/a
004 2 108 2 3.7 o15 0.8240 2s.079
005 2 to1 1.2 0.14 0.4240 24.227
offi t07 1 2.2 0.15 0.4240 ,s goo
007 2 108 0 l_2 o1 0.8240 26.734
008 2 108 L.2 0.15 0.8240 25.tr3
009 107 2 5.3 0.12 0.8160 22 734
010 tol 2 5.3 0.14 0.8160 23.907
011 108 -l 0ls 0.8160 24.454
o12 104 0.15 0.8160 24.764
013 to7 0.13 0.8150 23.098
014 108 1 4.3 0.14 0-8150 23.953
o15 108 2 5.3 0.14 o 4160 )1 9?A nla
016 108 4.3 o15 0.8160 24.804
lvetaSe3 107.5 1.0 3.3 0.15 0.8200 24.601 nla nla
G P04 3AS -0 2 27 22-RT - L298 Page 47 of 278
Low Load Run #5
Locltion: HuntinSton 1
tod (Mw): 191
Date: 41142023
Strnlime: 9:36
EndTime: 9,44
Probe / Gas Data
Adjusted Results
iavgl: 24.21 l{sec
Qsw: 36,001,700 wsct/hr
Probe tll Re: 0 degrees
Pro0c #2 Re: 0 degrces
Probe rn R{o: -33 deg[q.3
Paobe 82 RjLo: -12 dcfccr
8*r 0.1031 %/100
Md: 30.02 lb/b-molc
M.r 2E.7E lbllb-molc
Pbr: 23.52 ln Ht
P.: 4.50 ln HrO
P,: 23.29 in Hg
%COrr 105 %
ffir'------E%
,6COt 0.0 %
81.0
'6
Flow RATA Traverse Data
Polm ID Prcb! ID
Corrcct.d
StrckTsmp YawAngle YlwAntle ?l-P2
tFl ld€d (L (ded lin H,ol
Unadlult.d Replaccmcnt Point U*d *WAF
Axhlveloclty Axlolvolclry for Points
V, (fVrx) v. (lvsccl wAF? Usdc.
oo1 to7 2 3.2 0.14 0.424 2l 2M
002 lo7 1 2.2 0-15 0.8240 25.075
003 108 0 o.l7 0.8240 25.731
004 108 0 1.2 0.16 o 8240 25.933 ala
005 107 0 7.2 0.13 0.8240 2t ?ss
OG 107 3.2 o.74 o.4240 24.204
007 108 01 0.8240 26.695 n/a
008 108 1 2.2 0.15 0.4240 )s 910
oo9 105 4 7.3 0.12 0.8160 22.026
010 L07 3 6 o ls 0.8160 24.699
011 108 1 4-3 0.14 0.8160 )7 960
01)104 2 5.3 0.15 0.8160 24.765
106 2 o1 0.8160 21.170
014 106 1 4.3 0.14 0.8160 ?3 914
o1s 108 2 5.3 0.t4 0.8150 23.925
o16 108 5.3 o.15 0.8160 24.765
lYeraces 107.3 1.6 3.E 0.15 o.4200 24.459 nla nla
G P04 3AS -02 27 22-RT - t298 Page 48 ot 278
Low Load Run #6
Lo6tlon: Huntlngton I
Load (MW): 192
Date: 4i1212023
StanTimei 9:46
Endlimci 9:54
Probe / Gas Data
Prob€ f1 Re: 0 drg.e6
Probc fl2 Rm: 0 degreG
Probe f1 Rao: -33 d€8rees
P,obc #2 R.Lo: .12 degrces
Bs: 0.10, %/10O
Md: 30.02 lb/lb-moh
M,: 28, tbltEmote
Pb/ 23.62 inHg
Pt: -4,50 in H2O
Pt: 23.29 in Ht
%COr: 10.5 %
'hozt &51i
%CO! 0.0 %
81.O %
Flow RATA Traverse Data
Polnt lD Probe lD
Corccted
StaclTemp Y.wAngle YawAngl. ?l-Pz
(R (der) q (dG8l (in H,0)
Unadru5t.d [e-mail] Polntusd
'WAFAxialvclclty Axialvaloclty ior Points
V.lfvscl v.ltvs6c) WAF? Us.dc"
001 707 1 o.15 0.424 25.078
002 108 o 0.16 0.8240 25.935
o03 108 0 t.2 0.15 o.4240 25.tl3
004 108 1 2.2 0.16 o 4240 25.923
005 106 1 016 0.8240 25.471
006 107 o.17 0.8240 26.691
007 108 2 3.2 0.15 0.8240 25_O79 nla
008 109 0 t.2 o.16 o a?40 25.959 n/a
009 106 0.12 0,8160 22.174
o10 106 I 0.14 0.8150 2?.921
011 108 4 7.3 0.1s 0.8150 )4 671
0t2 108 o o1 0.8160 24.A33
013 107 5.3 0.12 0.8160 22.r34
014 108 4 0.14 0.8150 23.836
015 108 1 4.3 0.14 0.4150 )3_96t
016 108 1 L?o1 o 4160 24.4U
NeraSes 107.5 1.3 3.5 0.15 0.8200 24,76 ala ila
G P04 3AS -0 2 27 22-Rr - L298 Page 49 ot 278
Pjobe {1 Rsor 0 deSrear
Probc f2 Re: 0 dcgroes
Piobetrl Rao: -33 d€grec3
Probe *2 &Lo: -r,2 dGgreGs
8*r 0.1050 %/rO0
Md: 30.02 lb/lb.mole
M,: 28.15 lb/b-molc
Pb.: 23.52 ln Hg
P,: .4,50 in HrO
P!: 23.29 in Ht
%COr: 105 %
%Ozt 85 %
%CO: 0.0 %
I El.o %
Low Load Run #7
Locatlon: Huntington 1
to.d (MW)r 190
oate: 4l,,212023
St.rtTim€: 9:56
EndTime: 10:04
Probe / Gas Data
Unadiusted Results
Iavtl: 24.08 ftlscc
Clsw: 35,756,193 wcflhr
Flow RATA Traverse Data
Polnt lD Probe lD
coraact€d
StECkTemp YawAnglc YlwAnde
(Fl (dql O(desl
PI.P2
(in H,0)
Unadlurted Rlplaemcnt Polntusd fWAF
Axhl VclGity Axhl Veloclty lor Points
v. lft/rcc) v, (ft/sec) wAF? Usedc-
001 108 1 2.2 0.13 0.424 23.373
oo2 2 109 1 2.7 0.1s o.4140 25.129
003 109 0 1.2 0.16 0.8240 25.966
004 108 2 3.2 0.15 0.8240 25.086
oo5 2 108 0 t.2 0.14 0.8240 24.264
006 109 o o 14 o 4740 ?4 )A9
007 109 1 2.2 0.14 0.8240 24.277 n/a
004 2 109 2 3.2 0.14 0.8240 24.257
009 106 o1 o 4160 11 1?O
010 107 3 6.3 0.13 0.8160 23.003
011 to7 1 4.3 0.14 0.8150 23.949
o1)104 s.3 o.15 o_8150 24_775
013 106 2 5.3 0.12 0.8160 22.L20
014 108 I 3 0.13 0.8160 23.098
015 108 0 3.3 0.1s 0.8150 24.440
104 5.3 015 o.4150 )4775
rreraIeS 107.9 1.3 3.5 0.14 0.8200 24.083 nla nla
G P043AS-0 227 22-Rr - L298 Page 50 of 278
Probc fl Reo: 0 d.geet
ProtE f2 Rm: 0 deg.ees
Prob! rl R$o: -33 dctrees
Probrf2Rsro: -12 detrees
B*: 0.1046 %/l(xt
Md: 30.02 lb/lbnol.
M.: 2E.75 lb/lEmol.
Ph,: 23.62 ln Hg
Pd .4.50 ln H2O
P.: 23,D ln H8
%COr: 10.5 %
%Or: 85 %
',KOt 0.0 X
t{N,: 81,0 %
Low Load Run #8
L@tioni ]luntlngton 1
t6d (Mtryl: 195
Dat.: 4/1212023
StartTime: 10:06
EndTime: 10:14
Probe / Gas Data
Unadiusted Results
lavtl: 24.42'r1w
Qsw: 36,281,653 wr<flhr
Flow RATA Traverse Data
Point lD Probe lD
corcct€d
Stad(Temp YawAngle YawAngle ?l-P2
(F) (derl (L {der} lin H,0)
Un.drurtcd Rcplaement Point UsGd #WAF
Axial VclGlty Axial Vcloclty fo, Polnts
V, (ttl5ec) V- lft/recl WAF? usedc
001 707 3.2 0.14 o.424 24.2t2
002 108 3.2 0.15 0.8240 2S.084
003 2 109 L 01 0.8240 25.O78
o04 109 0.16 0.8240 25.951
005 LO1 0.13 0.8240 23.351
006 108 2 3.2 0.14 o 4240 24.233
007 2 108 7)617 0.8240 25.704
ooa 109 2.2 0.16 0.8240 25.951 n/a
009 105 2 5.3 o.12 0.8160 22.174
010 lo7 s3 o14 0.8160 23.972
011 108 5.3 0.16 0.8150 25.585
072 108 5.3 0.15 0.8160 24.773
013 t07 2 5.3 o.1l o_a160 21.196
014 104 53 o1 0.8160 23.062
015 108 4.3 0.15 0.8160 24.409 n/a
016 108 2 5.3 0.15 0.8150 24.773
lvGrages 107.8 1.8 4.1 0.14 0.8200 24.424 nla ala
G P043AS- 0 2 2 7 22-Rr - L298 Page 51 of 278
Prcbe*lRDo: 0 degreet
Prcbef2nsor 0 defees
Prcbe fl Rsor -33 detres
Ptobe#2 Rao: -12 dc!.Gca
8*r 0.1046 t6lr00
Mo'-199lb/E ote
M3r-:!:Zgtb/b-more
Pb,r 23,52 in Hg
Pr: 4.50 ln H2O
Pr: 23,29 ln Ht
%COrr 10.S r(
%qr_________tr%
%COr 0.0 9{
Low Load Run ll{l
lMtlonr HuitinSton I
l.@d (Mwl: 190
Datq 4l72l202t
st.rt ?ime: 10:16
Endllme: l0t24
Probe / Gas Data
Unadiusted Results
lavg): 24.40 trlscc
QSw: 36,240,259 mcr/hr
Flow RATA Traverse Data
Polnt lD Probc lO
corrccted
Stack Tmp YawAryle YlwAngle Pl-P2
(Fl (ded (L(ded (lnH,o)
Un.dlustcd Repl.cem€m Polnt Usd fWAf
Axlrl Veloclty Arl.l Veloclty lor Points
V.lft/*c) v- lftli.cl wAF? uedc
001 2 707 2 3.2 0.15 o.424 25 062
002 7 707 0 tq 0.8240 25.062
003 2 108 0 t.2 0.16 0.8240 25.94L
004 2 109 2.2 0.15 o.4240 25.951
00s 2 106 2 1.)o e)40 23.3!L
OG 108 2.2 0.16 0.4240 25.924
007 2 108 o 1.2 0.8240 29.941
008 2 109 0 1.)o.1s o a)40 25.140
ooq 106 4.3 0.12 0.8160 22_190
010 1 L07 0 3.3 0.13 0.8150 73_lO3
011 108 2 3 o ls 0.8160 24.773
01?109 0 3.3 o.L4 0.8160 24_Otl
013 1 LO7 4 7.3 o.t2 0.8160 2a_osz
014 1 107 4.3 o.13 0 8160 23.076
o15 104 4.3 0.14 0.8160 23.968
016 109 1 4.3 0.15 0.8160 24.431
lverates 107.8 1,1 3.4 0.14 0.8200 24,397 nlz ila
G P043AS - 0 22 7 22 - Rr - L298 Page 52 of 278
lr*mEr'Wo.3nl
lrrpll5rr
llrrellttrr
t'rnwrr
Inght ?415t
EPA tlethod 4 Dahsheet
lmplntsr
lmellttrr
lmplryrr
lmph3er
lrnpirEcr
AU T.!!
(0.01
Tot l Arrc.ltG Totsl(o.01 lo.mol
4
lnllld Hirl
L/Sc,o 5o6,8
/6s-t t/Vz.z
3,/.o 331,r/
5o3-5 5t2.,
t73b,[,)62.2.5
Es.?
tl
hHrl Hid
50b,x f"s,5
'/7zz ,73.?
331.Y 3?3,r
5lz, I 5Ll -
lw,5 /7?zL|
79. t
lun I LITI:
IATAR&nl trr($:
[.nrliE:,rl Lrtlr.hdlld
ltoDftB!t6r'f.ri l.rf ctftl
S.iilc
I.il
Sa.rfh
uebmc(dl O6Ircnrpffl
hlct Oodlt
Irn.O|tLt
Tsno FFI
rlrllrum
litfilaHffl.ol
G P04 3AS -0 22 7 22 -RT - t298
iltlhtlu.[ lta{firum
Revicwad: FPM CPM
Page 53 of 278
ri':;',
EPA toffiod 2F'Fast Flow,, Datasheet
UtGtCod.nra.' n?z*LL lrrmtlcPrrlrrml.lIl:L3.bL hE
Ctcrrts '{*i;,*aro HcPlurr(.ilrOl:-4.S Nr"lqlu:!ANTb .r t totrD/Al|lnranr tl?lB<Probccmfion v
Eenodrl:
- fAr;l(k lDGurohlD <r) -'l (n.Eollrl to.flrEulLIZRl-ctChortl'ltr0f:?-.( "L(xI
lun t ,od t tutrhc **f.brTlnc AX<q,@
Ilrurmffi
tFon+om
SrtlTrorl
Itl
tlrAdr
iDlr
uuo.tr.PrHp,
lPl.P,zl
HElaPrHpl
lir.95t
hnmltlll:
6)I t,o n b.lLloL7>O-/t
3 la?I ^. tE
vl loZ r:- t1a
\l l)tc n 6.tHLI o.t-7-o.t L3l07Io, ll,tl toy D, 15
Unl- I l-ou) L lHTlnc:h qoz hnfhc %e
,ort
ItclImS
l"Ft
rhrl|h
tfr
lrblotftf |Dl'ttlOf
IPl+Zl
]UrrpfHpt
ln.+51
CmmmB:
tr I lDb o b.ll
?-lob t)n.lqt
Ir:L o lvt)goltf,11,T Or o b.t afrltlol,I 0, 15
b l0+D h. t1--5 loY t h.t
t4 lof(0 -,q,
G P04 3AS -0 2 27 22 -Rr - r29 I Page 54 of 278
EPA tethod 2F ,Fast Flow, Datasheet
1i"..., , 1 ;\:/l ,t , t",i ;. ,.i { p, ; ;t
' : ,rl[ !_(lllt-|ilr..1.r.,G.!
['C!ctCod!llo\'tfraV hruGlcPrxrI'Hd:73,l"t Uo,lblc '0alcl('.xo ffiPtrfqrfltrol:- v.5 Nto
touE t+NTt tl I IrdrD/tbnrlt is3 FtufrCorfrdon t/Dltru{rl:/aol -rc-Dffi:tDr ?f\-"mr(Il to. {hte ul/nlfu,lrtOErfllpF ?.e'l orOal R.5
hltl l-^r.}\Irrtfhtrs bTLil:
Irrrrr:Fdlt
lFlll+ftt
llrrtTunj
Itt
Yrrfrlh
rDI
ttd!+a'fEO
Gr+zt
haPl'ttiol
lFl+lrl
hnrrnB
(5 ,oL Ll h,
2_loL ,l r).t?
3 /oT r>- l<
arl tn>h o,ls
L I ioJ L 6, lLqL)r*L D. )_S
.3 lo*L O, )q
u lo I f),t \
unt I Ldht L mftrE Ilrlhr.:
lcrt
Itrtllcng
("Fl
Ibuar;L
thr
rft{ofrlPfllpl
0r+,tr
rurcPfxpl
naflil
bmmcnts
04 >D,IL
4 lotr l-b,l33t Dt(f)/). r ?.
L)lo{,\ ,\.
{t ,to+D. t2-
L la{D, I?
3 loN L o, Jt4
L4 lo:L A.rti
Etllnll bItt:E
b_$
llrcttm3
(.F)
Yrrl4l
fDr
Udo*rrPfBpl
l?r+zt
HrlPfHpl
lm.Dnt
Emurnb
B)l06 o, lz^
"-ll.tK I rl. r<
3 /oK Z-D-t4
r/tfrK I 0,t1
t4 I lo7 L o. t2_\y L loi L O.lt
3 D7 L o,l5
L .lD*,o .,5
G P043AS -02 2 7 22-Rr - L298 Page 55 of 278
ll ''.1
EPA to0rod 2F "Fast Flou/' Datasheet
i':/i t ,'t'd i. r"i.{. e, ; l::
illi .ltfllt'l\ ,.!rrljr._ ri!
G P04 3AS -02 27 22 -RT - r29A Page 56 of 278
EPA toffiod 2F'Fast Flouf Datasheet
,1.^,;,, ;\:ii.\.rl'd ;. r: t r,;1.:
' i {I! .t_t,!lLtT\ 4rilljr,.(1
Prlhdcdc Dtoi' ozz+n llurtl?nrnClIl:3.bu l.EchlE[/i. {-..r'r'trPnrnnilth -V,R L!iuu:-1tru19 u-l ItobrP/efilurrc t31 PlotrGmfilon t/
hcrrodrh rtu)l Dfardrf r\-L Prlll ta.5DTEu L:-ILi l*ord|-HpF ?."+'or(rl z.s
hrl I l.,rrJ t4 ftrlirlnr:qLb Ert',;q3 L]
IrruraDft
lDptt.PoUl
iElanl
fFl
Y.rAt;hrr Udlq.r|.Hfl
o1+ll
rb.PrHpl
lxr+51
bnaunt*
I3 I 'IO L D, IL
a,,eT O-ttlatDxo, t<
v,to{o.t swloToo,l1
?_foK I o,l tl
3 ID11 L D,l I
Ll I Ol{,f), I5
hnl | /.r.*l 5 hilTlil:alc blhe q t{'l
,qR
HTrnuj
rFt
tlrllhrr rEbGrrlPf}tol
TPT+iU
HraPfHpl
naJsl
hnnentr:
IZ I lot a o,lL
L lo7 o,l I3toYID.I LI
L{ln{L o-, <
9 (lDt 2-o.l tIJa-td n- tut3lonLo- tflt,/o{?-h. t<
hlll )Q tlltTlael Qhe blhr:L€ L{
Pq(t
bclTmg
("Fl
XilrAt;h
tht
Udo.frr0flt0!
Gr+a
rffirPrHrol
llll.tlrl
hnmrntc
Bl r lot ta--o-t2^
L ,OA I o. lulo{'Ll D,l !
ul ln.{at>o,l<
l14 I hrL L O, ,LwLlo9{Ll O-lt-
3 la I D' lL
u lotr I Ot15
G P043AS-02 2 7 22-Rr - t298 Page 57 of 278
EPA tetftod 2F 'Fast Flour" Datasheet
g^1,-,, iVlrt.,l';l ;. r'l{ /,',}l
' ; nlt .;.1!tlt'l'r irillrr..rt
G P04 3AS -02 27 22 -RT - t298 Page 58 of 278
EPA Uoffiod 2F.Fast Flonf Datasheet
r", {.. /, ; l,'i[i' 't; t i'/i rt , t'd ;.
{llr .ltrllr.l.!
PtqGGlGodE Orti'D&\2i2-lrrurlttPrrsrt.llrh 23,1o2-kE' ?ari{<ayo HPnrnrefhpF - Y-s [r"fma:-iltttc, rlr hlrP/rErrt __lr3 HrCardtbn t/9prmor{rl:tridl lDffiD Jl] -z-DIIIt fo-fDIEIbt lttT,?-\r.rEl-rtt,F ?,q "orlxl 2,s-
trrt I I Dl^)brTh-lNl"lbpftrra loltl
m llrllh
th
ItldrlPfrpl
IPr#ll
PhdrtPl'ttol
lF.+!il
- .-..!
(tf Emrm.ni=
L-T tob z-o,12-L to+,L o. tLt3lof'Cq)#.),
vl lnV 2_D- t<It t6+L n.l IY7-lox L D.ta
--to{D, tq
v{lo 2-D,l5
G P04 3AS -0 227 22 -RT - L298 Page 59 of 278
Appendix A.3.L.2
High-Load Flow Data
G P043AS-0227 22-Rr -L298 Page 50 of 278
Client PacifiCorp
Unit lD Huntington I
load Hith
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("HrO)
02 (7ovd)
CO2 (%vd)
Vr. Volume of Water Condensed (mL)
Vm Volume of Stack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("HrO)
T. Temperature at Gas Meter ("F)
Calculations
Pm Absolute Pressure at Gas Meter ("Hg)
T. Absolute Temperature at Gas Meter ('R)
Vwc(nrry Volume of Water Condensed (scf)
Vm(*d) Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B*o, Saturated Moisture Content (/0/100)
Bs Measured Moisture Content (%/100)
B*. Stack Gas Moisture Content (/./100)
23.38 23.38 23.38
-4.50 -4.50 -4.50
7.5 7.5 7.5
t2 12 t2
2L5.4 275.4
99.648 99.648
0.9783 0.9783
1.8 1.8
66 66
23.51 23.5L
525 526
10.14 10.14
76,87 76.87
43.2 42.9
0.7L2 0.110
0.L17 0.117
0.L12 0.110
{saturat.d) (s.turat.d)
23.38 23.38 233A
-4.50 -4.50 -4.50
7.5 7.5 7.5
L2 12 r2
23.38 23.38 23.45
-4.50 -4.50 -4.50
7.5 7.5 7.5
L2 12 t2
134 62.7 60.6
50.798 26.20t 29.042
0.9783 0.9783 0.9783
1.8 1.8 1.8
70 71 56
23.51 23.57 23.58
530 531 516
6.31 2.92 2.85
38.89 20.02 22.9r
43.4 43.3 42.5
0.113 0.t12 0.108
0.140 0.t27 0.111
0.113 0.112 0.108
(S.turat.d) (Saturated) (S.turat.d)
2L5.4 L42.4
99.648 75.552
0.9783 0.9783
1.8 1.8
56 72
23.51 23.51
526 532
10.14 5.70
76.87 57.52
43.5 43.7
0.113 0.115
0.LL7 0.104
0.113 0.104
(Saturat.d)
142.4 147.4
75,552 75.552
0.9783 0.9783
1.8 1.8
72 72
73.51 23.51
532 532
6.70 6.70
57.62 57.62
43.2 43.4
0.112 0.113
0.104 0.104
0.104 0.104
GP043AS-0227 22-RT -L298 Page 6L of 278
Probe #1 RM: 0 dcgrces
Probe #2 Rm: 0 detreer
Probe#l&@: -33 dcgtecs
Prcbe*2RsLo: .12 dcgte€s
B..r o.ru6 %/100
Md: ,0.22 lb/b-molc
M.r 2E.E5 lb/lb-mol.
Pbi 23.:18 ln Hg
P.: -4.50 in H2O
P.: 23.05 ln Ht
%COr: l2O %
<r4oa ,S %
%CO: 0.0 %
High Load Run #1
Locatlon: Huntintton I
toad (MWl: 493
Dare: 4l73l2g2l
StartTime: 6112
End Tim€; 5:50
Probe / Gas Data
Unadiusted Results
iavgl: 55.05 ft/s*
qsw: 80,578,120 wcf/hr
Flow RATA Traverse Data
Polnt lO Probe lD
Cor.e.ted
st.ctTemp YawAngle Yawangle P7-?2
rn ldnl O..ld*l lln H.ol
Un.diusted Replacrment Point t sed SWAF
AdEl V€lcity Axial velcity ior Polnts
v- aItl*cl v- (lV*.} wAF? U..dC
001 106 o,2 0.55 o a)t ) 79?
oo2 108 t.2 0.7s 0.8240 56.365
003 10 o t.2 o.14 o.4240 55.086
004 o.2 0.1 0.8240 55 ?g
005 10 0 L.2 0.70 0.8240 54.549 n/a
offi o.2 o.70 o.4240 54.609
007 -0.E o.72 0.8240 55.379
008 0.2 0.72 0.8240 55.384
oo9 108 0.69 0.8160 53.507
010 110 o7 o 4160 55 133
011 110 0 3.3 o.7s 0.8160 55.835
o12 110 0 3.3 0.7 4 0.8150 55.452
013 109 o 070 0 4150 53 895
014 110 2.3 0.74 0.8160 55.509
01s 110 2.3 0.7s 0.8160 55.883
016 110 o7 o 4150 55 153
lvetages 109,7 .{r.8 r.5 0,72 0.8200 55.059 nla nla
G P043AS-02 27 22-RT - r29 I Page 62 of 278
High Load Run #2
Lo.ation: HuntlnSton I
toad (Mw): 493
Datei 4i1rl2023
StartTime: 7$6
EndTim.: 7:26
Probe / Gas Data
Adjusted Results
Va(avg): 53.71 fr./sec
Qsw: 78,766,L51 rad.lht
Probe tl Reo: 0 defecs
Probe f2 R@: 0 degrees
Prob€ #1 Rao: .3.3 dcirs
Probe f2 RrLo: -li degre.s
B*: 0.u02 %/100
Md: :}0.22 lb/lb-nole
M.: 28.87 lbllb.mole
Pb,: 23.:18 lnHg
P.: -4.50 ln H2O
Prr 23.05 ln Hg
96COrr 12.0 %
%oi_fa%
%CO: 0.0 %
: 80.5 9{
Flow RATA Traverse Data
Polnt lD Prcb. lO Stlck Temp
(Ft
corrected
VrwAngle YawAngle Pl-P2
(derl O-lderl (ln H,0l c.
Unadluned Rcpltccment Polnt Usrd #WAF
AIl.l Veloclty Atlal Veloclty for Points
V- Ittlse.l V. lft/secl wAF? us.d
001 107 -l 0.2 o.71 o.424 54.788
002 109 -1 o_2 o_74 0 tr&55.032
003 110 0 t.2 o.72 0.8240 55,307
OM 110 0 L.2 0.70 0.8240 54.533
005 109 -2 -0.8 o.67 0.8240 53_312
005 110 -1 o)o70 0.8240 54.545
o07 110 0 1.2 0.73 0.8240 55.690
ooa 111 0 t.2 0.71 0.8240 54.970
009 707 0 3.3 o.66 o.4160 s2 225
010 108 ,1 0.70 0.8160 53.877
011 110 -1 0.72 0.8160 54.738 nla
012 110 -t 0.70 0.8160 33.972
013 108 -2 1.3 0.69 o.8150 51.946
014 109 o 3.3 0.68 o.8150 53 103
015 110 o 3.3 0.73 0.8160 55.070 n/a
t10 -t 0.70 0.8160 53.972
lverates 109.3 4.7 1.6 0.70 0.8200 54.255 ala nla
G P043AS-0227 22-RT - L298 Page 63 of 278
High toad Run #3
tocltlon: Huntinllon 1
t@d (MW): 493
Date: 4ll3l2o23
StartTlme: 1149
End Time: t:09
Probe / Gas Data
Piobc *1 Re: 0 detre.s
Prob€ f2 Rer 0 dcgrees
Proberl R.s: -33 deS.ees
Probe f2 RjLo: -r,2 degreca
Bur 0.u35 %/100
Md: 30.22 lb/lb-molc
M,: 28.83 lb/llmol€
Pb,: 21.38 ln Hg
P.r {.50 in HrO
P.r 23.05 in Ht
c)6COi 12.0 e,4
%O2, 7 S 'h
%COr 0.0 %*
Flow RATA Traverse Data
Polil lD Prob. lD
Correctld
StackT.mp YawAngle YlwAntle Pl-Pz
(Fl (decl Olded {ln H,ol
Unadlusted Rld.emut Point Used #WAF
Axial Veloctty Axlal Veloclty for Polnts
v.(fvs€c) v.(lvsed wAF? usedc-
001 2 LOl o.2 0.70 0.824 54.438
oo2 2 109 o.2 0.68 0.8240 s3.750
003 2 0 1.2 o.70 0.8240 54.61E
004 2 0 L.2 0.68 0.8240 53.880
005 2 10 0 t.2 o.71 o.4240 54.959
offi .o8 o7 o a2ao 55 743
007 -0.8 0.73 0.8240 55.832
008 0.2 0.72 0.8240 55.405
009 108 o 3.3 0.65 o.8160 51.909
010 110 o ?3 o70 0.8160 53.963 n/a
011 111 0 3.3 0.69 0.8160 53.623
012 111 -2 1.3 0.6E 0.8160 53.308
013 1 109 2.3 o65 o.4160 5) 397
014 110 2.3 0.68 0.8160 s3.232
015 111 0 3.3 0.70 0.8160 54.010
016 o 3.3 o67 o at60 ) ato n/a
lYetages 110.3 4.7 1.6 0.69 0.8200 53.997 nla nla
G P043AS-0 2 27 22 -RT - L298 Page 64 ot 278
High toad Run #4
Lo6tionr Huntlngton 1
l6d (Mli4r 495
Date: 417312023
StartTime: *26
EndTiile: 8:45
Probe / Gas Data
Adjusted Results
53.60 ftlsec
Qsw: 78,406,740 w*tlht
Probe fl Reo: 0 deg.ccs
Ptobc f2 Re: 0 degrees
Pmb.tnRao: -33 de&e6
Probe #2 &ro: -12 d.grees
B*: O.LO42%1100
Mdr :10.22 lbllb-mol.
M,r 2E.95 lb/b-mole
Pb.r 23.3E in Hg
Pr: -4.50 ln H2O
P,: 23.05 ln H8
%CO, ILO,,A
%Ozt ls'h
%COr 0.0 %
80.s 16
Flow RATA Traverse Data
Polnt lD Probe lO Sta.lTemp
(F)
Correclcd
YrwAngle YawAngle Pl-P2
{dcr) Olderl (in H,ol c
Unadrurtad Rcdecmnt Point Usd f WAF
Axislv.lcity Axialveloctty fo. Polnts
V-lft/s6) V,lft/s.cl wAF? uted
oo1 107 0 L.2 0.65 o.424 52.344
002 109 0 t.2 0.71 0.8240 54_803
003 112 t.2 o.72 0.8240 55.333
o04 1t2 -1 0.2 0.70 0.8240 54.571
005 109 0 t.2 0.69 0.8240 s4.026
006 111 -2 -oa o7 o a)40 55.291 n/a
007 112 0 t.2 0.72 0.8240 55.333
008 172 -1 o.2 0.70 0.8240 54.571
009 108 -3 o.3 o.67 o 4160 \) 6U
010 t10 1.3 0.70 0.8160 53.933 n/a
o11 LL2 -1 2.3 0,12 0.8160 54.764
072 112 0 3.3 o.73 o_8160 ss.09s
013 109 0 3.3 0.66 o_8150 52.250
014 111 o6s o 8160 3.564
01s t1)2.3 0.68 0.8160 53.221
112 3 0.3 o.7t 0.8150 54.425
lvcrates 110.5 -0.9 1.3 0.70 0.8200 s4.138 ala nla
GP043AS-0227 22-RT - L298 Page 65 of 278
High Load Run #5
Location: Huntington 1
t@d(MW: 495
Dste: 417il2023
St.rt lim: 9:02
EndTlmc: 9t22
Probe / Gas Data
Probe #lRe: 0 detrees
Prob! 02 Re: 0 degrees
P,obc rn Rso: -33 delxcet
Probe f2 &,o: -12 d.g.es
B*r 0.1042 %/100
Mdr 30,22 lb/lb-mol.
M,r 28.95 lb/lb.mole
Pbi 23.3E in H!
P.: 4.50 in HzO
P.: 23,05 ln H8
%co{ ________:g!%%Oi 1s'A
'ACOt 0.0 %
80.5 %
Flow RATA Traverse Data
Polil lD P,obe lD
CoilGCted
StsckT€mp YawAngle YrwAngle Pl-P2
(Fl (ded (L ld.d lln H,ol
Unadrustrd ReplacGmcnt Poirtusd #WAF
Arill Vlloclty Axial Vcloclty tor Polnts
v.llt/secl v.lrt/sc) wAF? Usedc
001 10s o 0.68 o.424 53.S86
002 109 I 0.2 o.1 o 4240 s4.81S
oo3 110 1 0.2 0.75 0.8240 55347
004 110 -2 -o.a o.70 o.4240 54.470
005 108 o?o68 o.4240 53.S97
006 110 0 t.2 0.70 0.8240 sd 46i
oo7 11r 0 1.2 o.70 0.8240 54.511
008 -) {8 o_1 0.8240 55.291
009 109 0 3.3 0.70 o a160 53 810
010 110 0 3.3 o.72 0.8160 54.627
011 o7s 0.8160 55.796
ot2 111 2 1.3 o.70 0.E160 53 q80
o13 108 0 3.3 0.65 0.8160 51.807
014 10q -1 3 o74 0.8160 55.373
015 111 1 2.3 0.70 0 8160 53 950
016 111 0 3.3 0.69 0.8160 53.518
109.a 4.7 1.6 0.71 0.8200 54.373 nla nla
G P043AS -02 27 22 -RT - t298 Page 66 of 278
High Load Run #5
Lo@tion: Huntlngton 1
l@d (MW)r 192
D.te: 1ll3l2i23
Startlim!: 9:59
EndTimei 10:19
Probe / Gas Data
Prcba rll Re: 0 dett.et
Prctp #2 Rm: 0 detres
Probc #1 Rs: -33 degrees
ProbetnRqo: -12 degr€es
E$r 0.1042 %/100
Md:-1!31|b/lb-mol.
M,: 28.95 lb/b-mol.
P,;_31Aln H3
Pt: .4.50 ln HrO
P,'_!1{1ln Hg
%CA2t 7LO%
XOi ,s'r1
t{COr 0.0 X
80.s 16
Flow RATA Traverse Data
Polnt lD Prcbc lO StackTeilp
(Fl
Cor.ccl.d
Y.wArUl€ YlwAntlg ?7-?2
(ded (L(drrl lin H,ol C
UnidlGtcd Replfficnt Polnt Us.d # WAF
Axialvclodty A.lrlvelclty for Polnts
V-.ft/scl V-(ft/e.l wAF? Us.d
001 109 -1 o.7 0.6s o a)4 s) L!7
002 110 o1 o.1 0.8240 54.863 nla
oo3 110 0 1.2 0.70 0.8240 54.453
004 111 0 1.2 0.69 o.a)40 54.120
005 109 -3 o10 0.8240 54.401 nla
offi 110 .2 -0.8 0.71 0.4)40 54.858
007 110 0 7.2 o.70 0.8240 s4.463
008 tt2 0 7.1 o72 o a)to qq ?31
oos l0q -l 2.3 0.64 0.8160 51.496
010 110 -1 2.3 0.70 0.8150 53.903
011 111 -3 0-3 0.68 0.8160 s3-216
0t2 l1 -1 )1 o66 o 4160 5? 3S n/a
013 109 o65 0.8150 52.250
014 110 3.3 0.71 0.8160 54.240
015 111 -1 2.3 o.73 0.8150 5S.094
016 111 0 3.3 o.70 0.a150 s3.904
tverates 110.2 {r,9 1.4 0,59 0.8200 53.E40 nla nla
G P043AS -0 227 22 -RT - L298 Page 67 of 278
High Load Run #7
tocltlon: Huntlngton 1
tocd(Mw): 485
Date: 4lt3l202,
StanTlme: 11:15
EndTime: 11:35
Probe / Gas Data
Probe fl Re: 0 dotr€at
Probc f2 Re: 0 degiees
Probc *1 R{o: -33 dettecs
Probe *2 RsLo: -12 detrce3
8*: 0.1x19 %/100
Md: 30.22 lb/lb.molc
M1: 28.84 lb/lb.molc
Pbrr 23.:18 ln Hg
P.: 4.50 in H2O
P.: 23.05 in Ht
%COz, l2.O %
%O' L3%
%cO: 0.0 %
Flow RATA Traverse Data
Polnt lD Probc lO
CorrectCd
StackTemp YawAngle YawAngle P7-P2
lFl (der) O.. ldeel lln H.ol
Unadr$t.d Repl..amrnt Pointu*d fwAF
Axhl Veloclty Axlrl vcloclty lor Point5
v-lft/secl v.lft/recl wAF? Usedc-
001 2 109 0 o67 o.424 s3.335
002 2 110 0 1.2 o.74 o a?40 55.101
oo3 111 0 1.2 o.74 o.4240 56.150
004 2 -)-o8 o.72 o.4740 55.393
005 2 109 -1 0.71 o 4240 54.91S nla
OG 2 110 0 1.2 o.72 0.8240 55 334
007 -0.8 o.72 0.8240 55.393 n/a
008 111 .I o.2 o71 0.8240 ss.781
009 1 108 0 3.3 0.67 0.8160 52.694
010 109 0 3.3 o.72 0.8160 54.673
011 1 110 .3 0.o7l o.4150 ss.568
o12 1 110 .2 0.7r 0.8150 \4 415
013 109 o 3.0.65 0.8160 52.346
014 110 ?070 0.8160 53_956 nla
1 111 -1 0.73 o 4160 sq 1s
016 tt2 1 2.3 o.72 0.8160 54.864
110.1 .{t.8 1.4 0.71 0,8200 54,757 nlz nla
G P043AS-0 2 27 22 -Rr - t29A Page 68 of 278
High toad Run #8
L4ation: Huntlngton 1
l@d (MWl: 47
Datei 4ll3l202a
StanTime: 11:50
Endlime: 12:10
Probe / Gas Data
Probe sI Re: 0 d€g.ees
Prcbr 12 Re: 0 deg.ecs
Prcbc fl1 R.d -3.3 degrees
Prcb€ *2 &Lo: .12 degrces
B*r 0.U25 %/1(x,
Md: 30.22 lb/lEfrolc
M,r 28.85 lb/lb-mol.
Pbr: 23.38 in Hg
Pr: 4.50 ln H2O
P,r 23.05 ln H8
%COz. 7LO,)4
,LO2, 7.5 ,N
9{CO: 0.0 9(
Adjusted Results
Va{avg): 54.31 ftlsec
qsw: 79,55O419 mcf/hr
Flow RATA Traverse Data
Polnt lO Probe lD StaclTemp
(F)
Corrcctcd
YtwAngle YawAngl. P7-Pz
(d.8) Q. (desl (in H,0)c.
Unadjuncd Rcpl.cemcnt Poirt Used
'WAFAxi.l Velfifty Axlal VelGlty for Polrts
V. (ftl$c) V. (lvs.l wAF? ui.d
001 1Gl 0.2 0.77 o.424 54.911
oo2 110 o.2 0.74 o.4240 s5.108
oo3 110 .2 -0.8 o.7s o 8240 s6.481
004 111 0 o71 0.8240 s4.995
005 10a L.2 0.66 0.8240 52.884
006 l lo 0 L.2 0.72 o.4240 55_333
007 111 -2 '0.8 o.76 o a)Lo 55.905
008 111 0 o7 0.8240 55.755
009 109 0.58 0.8160 53.t7 4
o10 110 0 3.3 0.75 o.a160 55.95
011 110 -3 0.3 o.7)0.8160 54.407
072 -1 0.73 0.8150 55.191
013 r0t 0 3.3 0.64 0.8150 st.497
o7L t09 0 3.3 0.71 0.8160 s4.248
015 111 1 o.7s 0.8160 55.942
016 111 -1 o6q 0.8160 53.657
ueraSes 109.9 -{r.8 1.4 0,72 0.8200 54.851 ala nla
G P043AS-0 2 2 7 22 -Rr - t29A Page 69 of 278
High toad Run ll!)
Locatlon: Huntintton 1
Lold (Mwlr 492
Date: Al4l2O23
Stanllm€: 6.4
EndTlme: 6|32
Probe / Gas Data
Prcba #1 Reo: 0 dcgr.es
Prcbc f2 Reo: 0 d.grc.s
Prob. #1 &6: -33 detrEs
Probc fil Rsro: -L:I dGtres
8*: 0.1075 %/100
Md: 30.22 lb/lb-nol.
M.: 28.91 lb/lEmole
Pb,: 23.45 lnH!
P.i {.5{, in H2O
P,: 23.12 ln Hg
oACO2t ,'2.O
"l%O, 75%
t(co: 0.0 16
80.s 9(
Flow RATA Traverse Data
Polnt lD P.obc lO Stack Temp
IFI
Corrrctcd
Y.wAngle YlwAngle ?l-Pz
fd.d o ld.el lln H-ol c
Un.dlustcd Rlpl.emcm Poliit Usd *WAF
Axl.l V.lfitty Arlll Velclty ior Points
V- lftlk.l v- lltl..d wAF? Usd
001 108 .1 0.2 0.67 0.824 53.158
002 7 109 -1 o.2 o.74 0.8240 55.916
003 109 o7z o.4240 55_525
004 109 1.8 o.76 0.8240 56.639
005 to7 -2 -0.8 0.58 0.8240 53.502
offi 104 o.1 o_70 0.8240 54.336
007 109 1 0.2 0.75 0.8240 s6.292
008 109 .1 0.2 0.76 0.8240 56.665
oo9 108 0 3.3 0.56 0.8160 s2.162 nla
010 108 0 3.3 o.7L 0.8160 54.101
011 108 1 2.3 0.73 0.8160 54.905
o11 108 .2 1.3 o.14 0.8160 ss.310
013 108 I 0.68 0.8160 52.99I
014 109 -3 0.3 0.70 0.8160 53.855
015 109 .3 0.3 o.12 0.8160 54_519
016 11U 0.73 o t160 55 00?
lverales 108.5 -1.3 0.9 0.72 0.E200 54,685 nla nle
G P04 3AS -0 2 27 22-RT - L298 Page 70 of 278
EPA mothod 4 Datasheet
l,rld.l fflC
lmphrgor
lmd![ r
lmpl4sr
lmplrg.ra(g
LITVO $L.1
L)gS.,l fll,t"
316-q y{7.2
52A,1 5H,z
lXol,,2-Zou. A
as..l
lnplagr?
lmphlarso.-1-
lmph-lcr
lltlph!!r
lmpinca
""/
lmpln3CrwGlhr
tl?h8.1
UtlPinter
lnrphpr
lmphrcr{ lt(
4
/I,Jtfrd Hd
,57fr V?o.z
y77A 5t/3,o
I ta.j 37t.7
,/Ft.t 5tz.(
twr{.4 t?s7.c
I y2-',l
rl
lnldrl Fml
fro,z 5t+.q
184. 1 5V{.+
315,L 356,2
5 tz.l 5E,t
1gos.b t737.6
l3l/.0
(o.oe)
G P043AS - 02 27 22- RT - L298
Reviewed: FPM CPM
Page 7L oa27T
4
rdud Er!.1
Lt7?-rl 5rv-z
Lt??.9 5o7-t
3r5.ff 32I.tr
5ot.z $t0.6
, trt{.3 tt?b.1
Az- I
Ixt,htr):
I IA&Ill !z(r):
ilrrtltnc:)rt-TGtLrtChact
Eoltno:b.t-Tr!tttll6rct
S.mC.
nrrr
ldi..Prlcur
J.mph
volunr({t'l Dc[irmpfrl
lnlrt old.t
ItrU.Odr
T.rDfR
VErurr
l'ld6HrHrol
(0.01 (0.mo)
G P04 3AS -0 2 27 22 -RT - 1298
(0.01 (0.0)(0.0)
Page 72 of 278
Jt6-s
tt 5 o't
Mrrtnn fllttlum
G P043AS-02 2 7 22-Rr - L298 Page 73 of 278
EPA tsthod 2F Datasheet,';t, t. r I
ffi6.h olyi- ff"?zZ2-0nrrrurftl:btu lrz R.-
CTlrG N^;A'rn a lrrmlfitPrrmrl'llrl:L3:?,(lo.
hrrr:IlJtm- ,l HcPruml'll0l:- u.5 Irrtrffilon t/
rc 4 lB lzt HrlD/lhrnrtt il? I t?\qEl l?^ o
[il1 l*icl fi^rr I lrrtdtrrf l.llOl:4iz"Ltr!a"-z-
llrltftne:J DLIT-_bTlns dl,#-[ptrt
IlrnlrrFoht(Fct+oln0
Strdlanrf
rh
IrrftE
lrD.d
UlHratfHpl
0r+21
ruraP('llpl
rI.4!$hnmmE
'l )(lob .,o.bb NA
L /oY h D,7<I
3 ltb n D.w."
&l l/ /-t i.7L
2l I ilD o b,4D
?-lil -,D.vO
3 llt *)^-7LLllt t -t ()- fz-v I ln{-,h- /"9
2_I trr \l D" J?
?Itn r)^.7<t{Itrt /)o,Tl
J)I ItQ n ^-7,^-{2_Itn'-l n.4U
3 Irn rl n-?5
tl I lr)-4,e.-7<I
Scharrdc
I)hrtcter(DF
Pffit lbt FrunsLctwefi
1
l=
t=
2
3
4
5
6
t
N
Port lD
A
B
c
D
Rwianed: FPM CPM
G P043AS-02 27 22-Rr - L298 Page 74 of 278
lroLctGoth fml-tffiE-0rntorkl:fa)lrt-lD
thft 'l"t{;c.xo lrunctlcPnrsmClill:"3 {?{io^
burr:l1$1rb v I Itrds Prrrrur: l'Hlol:- u.5 MaGqdltlon V
)rts:tl lnlz=Pmbr lD/Alaunrnu tr*l nt 0clrl t1 o
lmt lh;f 8i,., z-lretdtrrtPllrh <:+"DfiI ?.4
ltlilftnr:r nToL lhTlnr:6724 ilto El
_.r, :, i , : ,, ,, EPA ileftod 2F Datasheet
Ranlewed: FPM CPM_
Page 75 of 278
IlrrrrrrHrtlPct+olnd
lE*Tunl
fFr
YrwtlSlc
liDGd
VrbdUlPl'Hrol
tP&Piil
PldraPl'Hpl
l9a,P5l Domntntt:
fr I taa-b.+l Ntl
L ln.t7,a-Lt I
3 llr ,\,>'ahl-
Ll llb o n -*o
tZ tDq -7 n. b7
7_lln b,+f\
ltb o.73
u Itt /1 o.At
lnl n l1 Ar
L totr h,*)
3 Itt't n 72-
:\L.t lln h-7h
)la*hL<
11 L toq h h- l^(
3 ,ID b n-lLB
u ilt\-l ^-+h
Schmtc
Dhmaer(D1=
ceA=
ca B=
ffil IIsi. Frmr SladrWdl
I
t
N
2
3
4
5
6
Poil lD
A
B
c
D
Ulrcdon
G P043AS-0227 22-RT - L298
hrcGrdr Do;-orz-fzJrgl,ofi,{0d,t frtutltc tL-
IhtG 'Qair*'c,o bqTGEfiHTIESFTTft L3l,3y E
Iqtr$,.lh,IYl- tr I rcb$r*dr - y-5 hjEf*frli V
4 lrt lz<HrB#fElfiir il+/ tl\Ari.ffi lLa
hnt Ll*h Ftaut ?tdor*EtrpF 3.'6 ',Bts 7.5
mffE -o+{i htItlG c)Yo?rph.[
EPA teffiod 2F Datasheet6,r\ l!}?NI$9fl
Rcrlarud: FPU iCP
Page 76 of 278
hn1,*rt'krIiffil,
hdltrrj
.tb
wfis
r*E*Ii'
lihcrFtel
. ,:Ftif!L ,..Ih*lrrtmn}.
,I I to*-t l). +o tlh
2_lDq -l h- fa(3 ltl'r)6r?a
v t/L t\ D, L?
?)tl ilo (>b.4l
?-tll D,7?
3 I t?--L D.77
v Itt n.Vi
(<,tAy r,D. L<
L Iln A b,Art
?ilt b h -/^q
u lt t -?D. AC
/14 I o.i D
\J/?- flx D. L?
?lt t r,O.aa)
u ll t ()b [^+
Ech.ilSc
Otgnctcr(DF
EaA=
Gt B=
Eohilf t[LFrun$ctvH
I
2-
3_
1
5-
5-
t
N
EgTID
A
B
c
D
G P04 3AS -0 227 22 -RT - L298
, i r_Jl,lii i 1 i. ),. ii EPA teftod 2F Datasheet
lir ' t.'Ir. ,( r, I
rnd.dGodG flri-oztTl2-D.lrbdrl:A9/TL LE
fhnt -O-',;C'...rr burrttErrrll.ld:z3-3t h.
Iqmls
t!LINIf'. t T ffilnsnFlfrOl:-u.<hdrGorldcr l,/
DrL'rl /rt lz e [6rD/fhnlrrc ttt /t3\FIlII t2-o
htnl *:cLt dlu H rrtlrd(.]ll0h | ?.N,'DfiI a,5
)trrtltnr:6*ze lbftna:ox4l rplll
IleurnrDolrttFctffil
$rdTrnp
r.n
ILullrl.
IrEl
YtlodrlPfHpl
lEr-E l
PHrlPfHpl
tF."Dsl hruurtshIlnZfi, [.r1 ttb
L toq ,i)./>.4 I
E t 12_n A. *z
q 1.,2_el h a4t
(?),D.tr h n- i^a
.l-tl t -7 ^-*3 lt7-/)o.l?
1 t 17_o.7a,
R loK n- Latv2-Iln -?A, - Jfi
?1n A. +7
u n7 b h ae.
h lnQ l\D. Ld
U L HI D. /-q
3 ilL f) /,
L4 lz--?D -+t
Ech.rr0c
DHilfr(DF
EIAF
cg B=
Pofrill U.r. FlUr SHVYJI
I
2-
3_
4
=-6
1
N
Fod lD
A
B
c
D
Ranlered: FPM_CPM_
Page 77 of 278GP043AS-0227 22-RT - t298
r : ',':]'' : ',
l,
, , ,' ': 'i EPA tethod 2F Datasheet
Ht !6d.nroi- ozz}zz-0DilEf{31:hllrr-[.m
ILrG ' {t:--L.^^lounrEhPrrrrml'15:z<( <v frn
loru:itrnu tLt IrdcFtrrqnl'll0h - r/.5 Pld:ffin V
DTD:Ll /rz lza MrD/Ahmac tri /rc<Dqfil 17-a
mnt A rA,,r 5 Lalffit'll0l://, l "Lff}(.5
illrtTlaE:"o?oL ,Enftn :og?z )rplr0
IlerrrrlohlFal+tr!
tirtTu4
rtl
tUAnJ.
IrD.d
uddlrtPfHpl
lrl+nt
HrlPfHpl
lna+!51 hnmoil*
tt I to/o o.by NE
L t6c O,7l I
3 Illrl D.+<
Ll il6 o,?a>
'z)IoY -l lt, /af,
L Ito ,h D.4n
3 ln f) o,=b
tl ,1,-7 D-+'L
1 ,oq 6 D.AD
t-tln t1 D.az-
3 ilt o A,7S
r-l ll t n__ D,?rs
L t6X 6 f), .lo5
\,(L la9 o,7q
3 llt h-7r,
L4 lt t o o. bQ
Schsrdc
IIarffir(DF
EIh!I D|LFmnSlrclU'tllll
1
f,=
F
2
3
e
5
6
t
N
Fod lD
A
B
c
D
Revlewed: FPM__.,1CPM_
Page 78 of 278G P043AS -02 27 22-RT - t298
;!,i$ ,.i r :.i ,i,. ii EPA llethod 2F Datasheet
ilr r lr .r r,
hdrctGodr I nai- ozz+?2-frru{d:fArs ltl im
qhnG
Srrm:
h:
hnt
rrttPnst
cPtrrynfllrl
r D/tllmul
otrd('ll€l:
fhc:
-rl-.rPllii
?t-7"
cadnhr
lz,-o-=-f.s
o)otst fr*+
{3 ffi@ prl@
lnwrFohtFiltffi
Srllrmp
ftl
Yill[h
lrDrd
Itr{odtf ltl'ltol
lEl+nl
mrarl'ltgl
tBrJltl Eurnltllls
ff I loq -l b. {,5 tw,
L tU o,7l
ts llD C)b.7n
Ll ilI o 6 .bQ
12)thq -?h.a
2_,tls h.?r
3 ,lA h h,7^
Ll tl7 b o-7?
t4)It9 -l x Acl
L I,rr\n,7r\
3 tn ??\. L(
t,,l O, t^L
$loq D A. LL
{L il6 o D.+l
?llt 6-a:<
rl I r)b, a.r,I
Schrrdc
Dlan#(Dts
naA--
rca B=
Pomt Dlt.Flutr6t ctvtfil
1_
)_
3a-
=-
6
Porr lD
A
B
c
D
Rev{ewed: FPM_CPM_
Page 79 of 278G P04 3AS -02 27 22 -RT - L298
EPA tethod 2F Datasheet
lnsr:FohtDat+ohtl
Strdlomp
ftl
Ilrfrth
lrD.d
wotfrratfllPl
lEr#il
ffirlPfHpl
lFafl$ComllEntr
It I lo9 b D,6+fie
a tth f)D,7LI
3 tll o a,?Ll
Ll tt I -7-o,7L?)toq D,7l
2_lt^-t)b,+i-
lt I -7 h.+2-
vl l, I -l b. +?
3),;4 n Ft l^1
?-t6q b D.+2-
3 Ito -\0,Yu
Ll ,t r|_?71.71'
l"l I l6q r)n , [oL'
-f L l|n n n.?+)
3 rlt o.2
Ll tr?-o,*7
Schurtadc
Diamcmrpp
Ml IrhLFqrSbd(VtUl
I
f,=
BE
2
3
4
5
6
t
N
PorflD
A
B
c
D
I
I
I
Revlmed: FPM CPM-
Page 80 of 278G P043AS -02 27 22 -RT - L298
, 1ri,r ,,;1,r : ; ,i,,. ;;, EPA tethod 2F Datasheet
,rdGdcodc ft/Di- n?2-?71L 0rrrukl:frqbt/TL n6
Ildrt 'l/n;*,n.o irmmllrtPnraml'lLl:23.3v nra
tam::a IUtvfl- ,t,t fficPrrrrrrFll0l:- u.5 P[drGqdtrbn t/
hE;tl /t<,lzt hot lDlAlIilE t ll7lrlt sqIIl lz. o
lunl rtif ol,r t(lltotrcll'll,ol:t3.b'DfiI 7.d
il.illlrng u rtso lEofhne:tztD/lt otll
IlrrerrrHrtftr&nfi$
SdTsnf
fn
Yrrrfh
ITDII
UddrtPl'llpl
Dr{lt
tldrlPl'lllol
tn +51 Eannfits
li I lDq -l o,7l NN
L ,th -l h.4i
3 /tA -2 D.+s
tl ll t h d-+t
9)l' lnJ{n f>. AA
2_tlb t)o-72-
3 ilI -2 o31
u ll,b D.7
?)t'lbq -t A. /"7
I nA f)^.zq3/lr)-?o,42_
1 lt t -l ^-R,14
I ,;*o D- /-Ll
z-lnO o o- a-i
3 1ilI -t h.7<
rl ttt -t D, 6q
Echordc
Offitet€r(D)=
Poht, DhtFrornstrd(Urlt
I
AF
B=
2
3
4
5
6
t
N
PaTlD
A
B
c
o
Revlewed: FPM CPM_
Page 81 of 278G P04 3AS -02 27 22-RT - L298
, ,.r ii ,, i i , ,; ,:,,',; EPA Method 2F Datasheet
tEL.tCod!nrt:- h77-a19 0nrnto{rl:ffunlaL fm
Ihrt '?Ls*a,o lrrmolc?rurarr Plld:L<,9<L.
bure:r{ilTk u-t hdcPrranrul'll0l:-4 *PlobcCardldcr ,/ ,/
h:tlltrl- lzl lrohlDrAhrmcttt rr*/ r31 elrl {
Nml l+,td.-hoa I trrtdtoctl'tl{l:t3.8"BfiI 12,a
ItrrtTtna:O to tz-lunllno:OLSL ruolxl f.6
Fruraffit(mffil
SlrclTrmi
Itl
trlCfr
lrDerl
VdodUCPl'lt0l
(Er#il
mroPfHrol
tFr45l loltrncill:
1oN o,61 aln
L liQ t\,au(I
3 tAq A n.+u
t,toq -?b,TL
,-\ -to-_L 0. (rY
L/L r oI/6.-+1J
l6q r),+5
L,l tL.o,+L
<)-16,n ^. Ll
2_lox ozto{
at I D7(-a_Ll) - 1l ro(-l
.2-loq -?b,74
1 l6t'*?o,+L
LI IA o,+3
8oficne0c
Dlametar (D)=
ceA=
cc B=
Poml lrht Frcm StecftWrll
t_
2_
3_
o_
5_
5
t
N
PdTlD
A
B
c
D
Raniewed: FPM CPM
Page 82 of 278G P043AS - 0 227 22- RI - L29 8
I
Appendix A.3.1.3
Instrumental Test Method Data
GP043AS-0227 22-Rr - L298 Page 83 of 278
PROnO22722
Paclficorp
Huntlngton Unlt I
rltt - 4lt4l2o2t
rt/rr MUN I KUST
Run *
StenTme
Stop Time
1
6tL2
6:50
3
7149
8:09
4
8i26
8:46
I
6i72
6:32
5
9:02
9172
2
7tO6
7126
6
9:59
10:19
7
11:15
11:3S
8
11i50
12:10
EPA Method 3A,6C,7E and 10 Data
CO, (%w)
so, (ppmw)
No. (ppmvw)
No, (ppmw)
co (ppmw)
Ma$ Emksion Calculatlons (Usln8 EPA Method 19)
10.9
23.7
108.4
0.0
143.9
1
Lr.2
23.7
99.9
0.0
797.4
2
10.7
22.7
95.8
0.0
135.8
3
11.1
22.6
95.1
0.0
263.1
o
LL.2
21.0
97.3
0.0
195.9
5
11.0
21.5
99.5
0.0
189.0
5
10,8
20.3
LOz.3
0.0
A7A
7
10.8 11.0
22.4 23.0
103.0 702.4
0.0 0.0
61.3 39.0
Fc scf/mmBtu
so, (lb/mmBtu)
No, {lblmmBtu)
CO (lb/mmBtu)
so, (lblhr)
No, (lb/hr)
co (lblhr)
Plant CEMS Data
1800
0.053
o.274
0.173
305.4
t033.6
835.5
1
0.054
0.792
0.231
311.0
939.6
1130.1
2
0.052
0.193
0.167
287.O
894.8
772.4
3
0.061
0.184
0.309
294.3
890.7
1499.5
4
0.056
0.185
0.230
275.9
915.9
7t28.7
5
0.059
0.195
o.226
274.5
927.7
!072.5
6
0.056
0.203
0.0a2
267.5
969.7
389.1
7
0.052
0.205
o.074
296.L
978.2
354.5
8
0.063
0.201
0.047
304.9
974.7
226.r
9
Unit Load (MW)
co, (%w)
so2 (ppmvw)
SO, (lb/hr)
SO, (lb/mmBtu)
No, (ppmvw)
No, {lb/hr)
NO, (lb/mmBtu)
co (ppmw)
co (lblhr)
CO (lblmmBtu)
GPO43 A5-0227 22- RT- 1 298
493
10.6
20.9
259.8
0.059
111.3
1033.7
o.225
148.9
8rt4.5
0.183
493
10.8
21.O
256.5
0.058
99.8
909.9
0.198
185.1
1077.4
o.223
493
10.9
20.5
267.7
0.057
99.1
903.7
0.196
729.6
772.9
0.156
496
10.9
20.4
257.9
0.056
879.4
0.190
258.9
1458.6
0.310
495
10.9
18.8
234.7
0.0s2
98.4
896.7
o.794
190.1
1045.6
o.224
492
10.8
19.3
241.2
0.0s4
100.3
924.7
0.200
743.7
1000.0
o.223
485
10.6
19.1
244.7
0.054
702.2
941.9
0.208
63.6
340.3
0.079
487 492
10.6 LO.1
19.9 23.2
256.1 303.1
0.0s6 0.06s
103.8 704.9
96L.2 985.0
0.211 0.211
56.8 17.5
303.7 274.3
0.070 0_046
Page 84 of 278
PRaro22722
PacifiCorp
Huntington Unlt 1
4lL? - 41L412023
40 CFR Part 75, Appendix A
56.5.6 Pollutant Stratification Test
Port Point fime
stack Dia meter: l.5r551-l
Stratification Test Point 1: t4.2" (4.4%l
Stratification Test Point 2: 47.2" 1L4.6%l
Stratification Test Point 3: 95.6 " (29.6y"1
5ozCO,
1
1
1
1
1
1
2
2
2
2
2
2
3
3
3
3
3
3
4
4
4
4
4
4
t 4l!3/2O236:L2
1 6113
2 6:14
2 5:15
3 6:16
3 6:L7
t 4lL3/2O236:23
t 6:24
2 6:25
2 6:26
? 6:27
3 6:28
L 4/L3/20236:34
I 6:35
2 6:36
2 6:37
3 6:38
3 6:39
t 4lL3/20236:45
1 6:46
2 6:47
2 6:48
3 6:49
3 6:50
11.0 22.5
11.0 22.5
11.0 22.5
11.0 22.L
11.1 22.5
Ll.L 2L.4
11.0 20.8
11.0 20.8
11.1 20.6
11.1 21.2
11.1 2t.2
11.1 21.a
LL.2 23.6
Lt.z 24.0
1L.2 24.O
11.4 23.9
Lr.4 23.9
Lt.4 24.0
11.6 25.3
tt.7 25.5
LL.l 25.5
LL.7 24.5
LL.7 24.5
LL.7 24.7
Mean
Max Deviation From Mean
Max Devlation l%)
Short Une?
Slngle Polnt?
11.3 23.0
0.4 2.4
?,8% to.s%
ot( No
OK OK
G P043AS-0227 22-PJl - L298 Page 85 of 278
PRO1422722
PeclfiCom
Xuntington Unlt 1
4i1r-4/141202t
Tcst Run #l
Start Time
Run Length
Stop Time
6iL2
2t
6:50
PROt422r22
P.cmCorp
Huntlngton Unit I
4/13 -4i1412023
Tatt Run f2
Stan Time
Run Length
Stop Time
Uncorrected Analyrer Data
7.06
2r
7.26
Uncorreded Analyzer Data
Minutc
1
3
4
5
6
7
8
9
10
11
L2
13
14
15
15
77
18
19
20
2l
22
23
24
Tlmc
6tL2
5:13
6'.14
6:15
6:16
StLj
6:23
6124
5:25
6126
6i27
6:28
6134
6:35
5:36
6:37
6:38
6:39
6:45
6:46
6i47
6:48
6t49
5:50
Mlnutr
1
2
3
4
5
5
7
8
9
10
11
L2
13
14
15
16
r7
18
19
20
Time
7:06
7tol
7..04
7tO9
TtLO
7..L7
7172
7173
7174
1:75
7:76
7tl1
7t!8
7tLg
7t2O
7t2l
7t22
7123
7124
1125
cor sor No, co Nor
Xw ppmw ppmw ppmw ppmw
11.0 22.5 121.8 331.6 -0.1
11.0 22.5 123.0 369.1 0.0
11.0 22.L L2L.4 292.7 0.0
11.1 22.6 t2t.2 459.1 0.0
11.0 21.8 t22.2 428.4 0.1
11.1 27.4 r2t.2 /185.9 0.0
11.0 20.8 116.s 15.8 0.1
11.1 20.6 11s.0 9.6 0.0
Lr.2 21.0 113.5 t2.\ 0.1
11.1 2L.2 113.8 16.0 0.0
11.1 2L.2 113.6 1s.9 0.0
11.1 2L.E 774.7 17.2 0.0
ll.2 23.6 108.7 68.6 0.0
L1.2 24.0 108.9 57.9 0.0
11.s 24.7 108,0 91.9 -0.1
11.4 23.9 107.0 68.4 0.0
11.s 24.O 105.9 67.0 0.0
77.4 24.O 105.6 50.5 0.1
11.6 25.3 104.8 93.5 0.1
77.7 zs.s 103.9 L49.1 0.0
11.5 25.0 105.6 100.5 0.0
LL.1 24.5 104.0 97.4 0.0
Lt.l 2s.3 102.5 118.3 0.1
LL.7 24.7 102,8 105.3 0.0
cor sor No, co ilor
Xw ppmw ppmw ppmw ppmw
r1.7 24.9 104.5 24r.9 {.1
77.7 24.2 104.9 190.6 0.0
11.9 24.2 104,0 267.2 0.0
11.8 24.3 103.3 307.0 0.0
11.9 24.2 LO4.2 321.8 0.0
11.9 24.4 104.8 399.s 0.1
11.8 24.2 104.5 271.1 0.0
11.8 23.s 104.1 227.0 -0.1
11.6 23.4 102.4 24s.0 0.0
11.6 23.4 LO2.6 186.5 0,0
11.6 22.7 100.4 124.3 0.1
11.5 22.7 98.8 105.2 0.0
11.5 22.s 99.5 L24.2 0.0
11.6 23.\ 99.8 122.A 0.0
11.5 23.7 100.7 8S.8 0.1
11.s 23.s 101.0 707.7 0.0
11.4 22-a 101.8 79.5 0.0
17.7 23.8 99.5 277.2 -0.1
t7.7 24.3 100.8 205.1 0.0
11.8 2s.0 100.1 283.4 0.1
-0.1 0.3 0.9 0.2
-0.1 -o.1 0.5 0.0
.r).1 0.1 0.7 0.1
9,3 26.7 160.5 159.5
9.3 26.3 152.9 151.4
9.3 26.s 155.7 1s5.5
8.9 25.5 153.8 1s0.9ffi
Averate
Co r.
c.
C. p,.
c6
c..
con€cted Arerag€:
11.3 23.1 111.9 '.49.6 0.0
0.0 -0.1 0.1 0.7
-0,1 0.3 0.9 0.2
-0.1 0.1 0.5 0.5
9.2 26.3 156.7 154.3
9.3 26.7 160.s 1s9.5
9.3 26.5 158.6 155.9
8.9 26.5 153.8 150.9ffi
27 7126 71.7 24.6 100.7 168.2 0.1
AvG.ate ll.7 23.8 102,0 203.3 0.0
Co ro
c6
C" p.
c,
c."
Coreded AvcraSe!
G P04 3AS - 0 2 2 7 22 - RT - L29 I Page 86 of 278
PROt422r22
P..mCorp
Huntlngton Unit I
4it3-41t412023
Test Run f,3
StartTime
Run Length
Stop Time
7'.49
27
8:O9
PeoJ422722
Pacilrcorp
Huntlngton Unlt 1
4113 - 41t412023
T6t Run lr4
StartTime 8:26
Run Lentth 2l
Stop Time 8:45
Uncorrected Analyzer DataUncorrected Analyzer Data
to.7 27.t 92.S 157.5 0.0
10.7 27.3 92.5 146.4 0.0
10.8 27.2 92.1 132.3 0.1
10.9 27.4 91.8 1s1.6 0.1
10.8 2L.8 92.6 t21.3 0.0
10,8 27.6 92.7 104.1 0.0
10.9 22.2 91.3 157.3 0.0
10.9 22.0 92.5 168.6 0.0
10.9 22.5 94.7 167.0 0.0
11.0 22.7 94.5 122.5 0.0
10.8 27.7 95.2 134.5 0.0
10.8 20.5 94.2 93.4 -0.1
10.8 20.8 94.9 99.2 0.0
10.9 20.9 94.6 108.4 0.1
10.8 20.7 95.1 76.2 0.0
11.0 27.0 94.7 119.2 -0.1
10.9 20.5 93.8 LO4.2 0.1
10.9 20.9 .3 135.5 0.1
11.0 21.2 93.5 158.3 -0.1
11.1 21.3 93.7 176.s -0.1
2L 8:09 11.0 21.0 93.6 160.1 0.0
Awngc 10.9 21.3 93.5 133.5 0.0
cor sor No, CO Nor
fime '(w
ppmw ppmw ppmw ppmw
11.0 27.9 93.9 14L.6 -0.1
11.0 22.2 92.6 rs2.L 0.0
11.1 22.O 91.3 189.3 0.0
11.0 2t.9 91.8 2L0.6 0.0
11.1 21.2 91.8 2!s.6 0.0
11.0 20.9 92.4 192.3 0.0
11.0 20.5 93.0 155.8 0.1
10.9 20.1 92.5 158.9 0.0
11.0 21.3 91.5 166.5 0.1
11.1 21.8 92.2 767.7 0.0
Lt.2 21.9 92.2 365.1 0.0
11.1 2r.9 90.8 528.0 0.0
LL.2 22.3 90.8 538.6 0.0
11.0 2!.4 9L.2 319.9 0.0
11.0 20.3 a9.7 183.1 0.0
11.0 '9.7 88.5 248.3 0.1
11.0 19.5 89.9 254.7 0.0
11.1 20.2 89.9 393.0 0.1
11.0 20.5 91.0 320.6 0.0
11.0 20.7 91.3 226.a 0.0
cor soz No, co Nor
Time ,6w ppmw ppmw ppmw ppmw
! 7149
2 7,50
3 7:51
4 7,52
5 7:53
6 7:54
7 7155
8 7:56
9 7157
10 7:58
11 7:sg
8:00
8:01
Mlnutc
1
2
3
4
8..25
8127
8:28
8..29
14 8102
15 8:03
16 8:04
17 8:05
18 8106
19 8:07
20 8:08
5 8:30
6 8:31
7 8132
8 8133
9 8:34
10 8:35
11 8135
72 8137
13 8138
14 8:39
,.5 8:40
16 8141
17 8142
18 8:43
19 8:44
20 8:45
Co o.
Qru
c.
C. p,.
c.
c."
Corc.ted Avcratc:
-0.1 -0.1 0.5 0.0
-0.1 0.2 0.4 -0.2
.0.1 0.1 0.5 {.1
9.3 26.3 152.9 151.4
8.9 X4.9 t47.0 145.4
9.1 25.6 150.0 14t.4
8.9 26.5 153.8 150.9ffi
2t 8146 10.9 20.4 90.6 185.8 -0.1
Avcraac 11.0 2,-.l 9,-A 254.t 0.0
Co p.
q
C"p,"
ch
c*
Correded Av€ralc:
-0.1 0.2 0.4 -0.2
o.2 -0.2 0.0 -1.9
0.1 0.0 0.2 -1,1
8.9 24.9 L47.O L45.4
8.8 24.6 L48.2 144.1
8,9 24.8 147.6 14/,,8
8.9 26.5 153.8 150.9ffi
G P043AS-0 2 27 22-RT - t298 Page 87 ot 278
PROt-022722
PilmCorp
Huntlngton Unk 1
4lt -4/14/2021
Test Run 15
StartTime
Run LenSth
Stop Time
Uncorreded
9:02
27
9.22
Data
cor sor No. co Nor
96w ppmw ppmw ppmw ppmw
10.9 21.4 94.6 2L0.7 0.0
10.9 20.5 95.2 198.5 0.1
11.0 20.2 95.0 252.2 0.1
10.9 19.4 95.8 159.9 0.1
10.9 18.9 95.4 212.7 -0.1
10.9 18.4 94.9 155.7 0.0
10.9 L9.2 9s.6 202.7 0.0
10.9 19.9 95.2 725.7 0.0
11.0 2r.4 95.2 123.8 -0.1
11.1 zt.X 94.L 7rO.7 0.0
7t.2 20.8 94.8 150.9 0.0
11.1 20.1 94.3 192.0 0.0
LL.2 19.6 93.7 187.3 0.0
LL.2 19.s 93.1 299.9 0.0
11.1 18.9 92.3 334.6 0.0
11.0 78.2 94.0 193.0 0.0
LL.2 18.5 92.6 224.9 .0.l
11.0 18.8 92.9 166.7 0.1
11.0 1E.3 92.9 106.7 0.1
11.1 18.5 91.6 L74.5 0.0
11.0 18.4 91.4 194.3 -0.1
PROt422722
9.clnCorp
Huntlntto. Unh I
41L-4l,,.l202'
Test Run 116
Start Time 9:59
Run Len8th 2l
Stop Time 10:19
uncorrected Analyzer oab
Mlnutr
1
2
3
4
5
6
7
8
9
10
11
L2
t4
15
16
11
18
19
20
27 10119 10.6 18.8 99.1 8s.5 0.1
AEEge 10.8 19.9 t6.5 1t1.2 0.0
0.1 0.7 0.5 -0.9
0.1 0.0 0.1 -2.4
0.1 0.1 0.3 -1,7
8.8 24.6 148.9 145.5
8.8 24.5 149.1 143.7
8.8 24.6 149.0 144.3
8.9 26.5 153.8 150.9ffi
co! sor f{q co Noz
%w ppmw ppmw ppmw ppmw
10.8 18.4 93.8 270.3 0.0
10.9 18.7 92.5 319.0 0.0
70.7 18.8 95.2 259.0 0.0
10.8 18.8 94.5 204.4 0.0
10.8 79.7 94.1 284.5 0.1
10.9 20.2 94.3 251.0 0.1
10.8 19.9 9s.0 230.4 0.0
11.0 19.9 94.3 312.8 0.1
11.0 19.6 95.9 361.s 0.0
10.8 19.5 97.4 167.! 0.0
10.9 20.0 96.2 134.5 0.0
10.8 20.3 96.1 158.3 0.0
ro.7 20.3 96.1 180.9 0.0
ro.7 20.3 98.3 114.3 0.1
10.7 zL.L 98.8 89.4 0.0
10.8 2L.9 98.0 114.8 0.0
10.6 2L.2 100,0 64.7 0.1
10.6 20.4 99.4 35.1 0.1
10.5 20.4 98.5 81.5 0.1
10.6 19.6 99.1 82.0 0.1
Mlnutr
1
7
4
5
6
7
8
9
10
11
72
13
74
15
16
77
18
t9
20
27
Tlmc
9:02
9:03
9:04
9:05
9:06
9:07
9:08
9r09
9r10
9:11
9r12
9r13
9:14
9r15
9:16
9..17
9:18
9r19
9:20
9tZ7
9:22
Timc
9:59
10:00
10:01
10r02
10:03
10r04
10:05
10:06
10:07
10:08
10:09
10:10
10:11
10:12
10:13
10:14
10:15
10:15
10:17
10:18
Awrat!
Core
q
C. p,.
C, q,
c,
c,.
Corr€d€d Avcraae:
0.2 -0.2 0.0 -1.9
0.1 0.2 0.5 {.9
0.2 0.0 0.3 -1.4
8.8 24.6 L44.2 1/t4.1
8.8 24.6 148.9 145.5
8.8 24,6 148,6 !t4,E
8.9 25.5 153.8 150.9@
Coo,
c.
C, pr"
C. pt
c.
C..
Coirected Averair:
G P04 3AS -0 2 27 22 -RT - L298 Page 88 of 278
PROI-O22722
Pacmcorp
Huntlngon Unlt 1
4lt3-4lt4l202a
Test Run t7
StartTime
Run Length
Stop Time
11i15
21
11:35
?ROt422772
PaclflCorp
Huntlngton Unlt 1
4173 - 411412021
Tcst Rur f8
Start Tlme
Run Length
StopTime
11:50
27
12:10
Uncorrected Analyrer Oata Uncorreded Analyzer Data
1 U:15 10.6 21.4 100.2 722.9 0.0
2 lltL6 10.8 2f.X 98.9 95.0 0.0
3 11:17 10.7 20.9 100.5 87.2 0.2
4 11:18 10.7 20.3 99.8 55.1 0.0
5 11:19 10.8 20.1 99.6 77.3 0.1
6 11:20 10.5 19.8 101.0 60.0 0.1
11:25 10.8 77.9 99.8 44.8 0.0
L7t26 10.7 r7.7 100.4 63.3 0.0
17127 10.7 17.5 101.0 36.5 0.0
17128 10.8 L7.8 99.4 40.9 0.0
11129 11.0 18.6 98.6 70.0 0.0
11i30 10.9 L8.7 99.3 112.9 0.0
7 LLt21 70.7 19.4 100.2 76.7 0.0
8 tLt22 10.5 19.0 101.7 30.9 0.1
9 11:23 10.7 18.7 101.1 49.3 0.0
10 7717.4 10.7 18.4 100.5 39.6 0.0
11
L2
13
14
15
15
77 10.8 18.3 100.1 54.2 0.0
cor sor tio, co t{or
Tlme %w ppmw ppmw ppmw ppmw
l.1i3l
cor sor ilo, co Nor
9aw ppmw ppmw ppmw ppmw
11.0 27.5 100.8 727.2 0.0
10.9 20.2 101.s 77.8 0.1
70.7 19.r. L02.7 33.3 0.0
10.6 t7.7 L03.7 14.0 0.1
10.8 19.8 107.7 32.1 0.0
10.8 27.2 101.4 44.8 0.1
10.8 27.2 100.5 59.1 0.0
10.8 27.r 102.1 55.1 0.0
10.9 21.9 101.3 54.8 0.0
10.8 27.8 101.6 s0.8 0.1
10.9 22.2 100.3 73.2 0.0
11.0 22.4 100.5 74.2 A.1
10.9 22.r rcl.1 54.9 0.1
10.9 22.L 101.0 77.1 -0.1
11.0 22.6 100.3 79.1 0.0
10.9 22.4 101.3 88.0 0.0
10.8 22.L 103.3 43,3 0.0
10.8 22.0 103.5 32.8 0.0
10.8 22.0 102.5 43.2 0.0
10.8 22.L 102.1 38.8 0.0
Mlnute Time
1 11:50
2 11:51
3 11:52
4 11:53
5 11:54
5
7
8
9
10
11
72
13
t4
15
16
L7
18
19
20
11i55
11:56
L!.57
11:58
11:59
12r00
12:01
!2102
12:03
L2tO4
12:05
12:06
12:07
12r08
12:09
18 11t32 10.9 18.9 99.3 73.4 0.0
19 11133 10.8 18.5 101.1 44.7 {.1
20 LL:34 10.8 18.6 101.3 30.4 0.0
2L 11:35 10.9 18.9 100.3 54.2 0.0
Cor
q
C. p,"
0.1 0.0 0.1 -2.4
0.1 0.0 0.4 -3.8
0.1 0.0 0.3 -3.1
8.8 24.5 149.1 143.1
9.0 25.4 1s1.9 1i14.5
8.9 25.O 150.5 143.t
8.9 26.5 153.8 150.9@
Q*
Co e*
c.
C. p.
C. por
c,
c-.
Cor€ated AvGrala:
21 12:10 10.7 21.5 102.4 31.6 -0.1
AvcrelC 10.8 21,4 101.7 55.3 0.0
0.1 0.0 0.4 -3.8
0.1 0.2 0.2 -4.1
0.1 0.1 0.3 {.0
9.0 25.4 151.9 t44.5
9.0 25.2 151.6 t44.4
9.0 25.3 151.8 144.5
8.9 26.5 153.8 150.9@
c.
c..
Coracted AvGrailr
G P04 3AS -0 227 22-RT - L298 Page 89 of 278
?ROI4X2722
PaclftCon
Huntlniton Unh I
4h3-417412023
T.d Run fi)
StanTime 6172
Run Length 2l
stopTime 5,32
Un@rreded Analyzer Data
Mlnui!
1
2
3
4
5
5
7
8
9
10
77
72
13
74
15
16
17
18
19
20
2t
nmc
5:12
5:13
6:14
5:15
5:16
5117
5:18
6:19
6:20
612r.
5:22
6:23
6t24
6t25
6:26
5t27
6:28
6:29
6:30
6:31
6:32
cor 5oz No, co tor
taw ppmw ppmw ppmw ppmw
11.1 24.3 104.6 52.6 0,0
11.1 2s.2 t04.2 30.3 0.0
L7.2 24.6 104.7 25.3 -0.1
tt.2 23.9 103.9 37.7 0.0
11.3 23.2 103.6 43.s 0.0
tt.z 23.3 70d.2 58.8 0.0
11.1 22.6 103.9 Ll.s 0.0
11.3 22.5 103.9 31.9 0.0
1r.3 22.8 104.8 41.8 0.0
11.1 22.2 105.5 38.2 -0.1
7!.2 23.0 70/--2 60.3 0.0
11.3 24,4 104.5 47.0 0.1
11.2 21.7 104.9 39.9 0.0
11.2 23.5 104.3 66.4 0.0
11.1 23.0 70/..Z 7r.0 0.0
11.0 22.4 10s.1 42.7 0.0
11.0 22,0 105.8 27.3 0.0
11.0 22.4 105,5 32.3 0.0
11.1 22.6 106.1 26.5 0.0
11.1 ZZ,9 105.4 23.9 0.0
11.2 22.1 707.7 25.1 0.0
AYtratc
€o c.
Qq
q
Qn r.
C. po
c.
c..
Comctad AEragcr
11.2 21.2 10'1,9 /O.0 0.0
0-0 0.0 {.2 -1.0
0.1 -0.1 -0.2 -1.4
0.1 -0.1 4,2 -1.2
9.0 26.4 155.2 155.9
9.2 27.L 159.2 159.7
9.1 26.8 157,7 11t8.3
8.9 25.s 1s3.8 150.9@
GP043AS'0227 22-RT -t298 Page 90 of 278
Appendix A.3.2
Unit 2
G P043AS-0 22 7 22-Rr - L298 Page 91 of 278
Appendix A.3.2.L
Low-Load Flow Data
G P043AS-0227 22-Kf - L298 Page 92 of 278
Client PacifiCorp
Unit lD Huntington 2
load Low
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hg)
Stack Static Pressure ("H2O)
O, (%vd)
CO, (%vd)
Vr" Volume of Water Condensed (mL)
V. Volume ofStack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("H20)
Tm Temperature at Gas Meter ("F)
calculations
P. Absolute Pressure at Gas Meter ("Hg)
Tm Absolute Temperature at Gas Meter ('R)
Vwc(std) Volume of Water Condensed (scf)
Vn(stu) Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B**t Saturated Moisture Content (7"/100)
B* Measured Moisture Content (/"/100)
Btr Stack Gas Moisture Content (9r'./100)
23.38 23.38 23.38
-4.30 -4.30 -4.30
8.5 8.5 8.5
t\ 11 11
64.L 54,L
37.558 37.558
0.999s 0.9995
1.7 t.7
68 58
23.57 23.51
s28 528
3.O2 3.02
29.48 29.48
40.7 40.6
0.098 0.097
0.093 0.093
0.093 0.093
23.38 23.38 23.38 23.38 23.38
-4.30 -4.30 -4.30 -4.30 -4.30
8.5 8.5 8.5 8.5 8.5
11 11 11 11 11
23.38
-4.30
8.5
11
64.L 70.8
37.558 41.796
0.9995 0.999s
1.7 1.7
58 75
23.51 23.51
528 535
3.02 3.33
29.48 32.38
40.8 41.3
0.099 0.101
0.093 0.093
0.093 0.093
70.8 70.8
47.796 4L.796
0.999s 0.999s
L.7 L.7
75 75
23.51 23.51
535 535
3.33 3.33
32.38 32.38
40.3 39.6
0.095 0.093
0.093 0.093
0.093 0.093
(Saturatcd)
70.8 70.8 70.A
4L.796 4r,796 47.796
0.9995 0.999s 0.999s
1.7 1.7 1.7
75 75 75
23.51 23.51 23.51
535 535 535
3.33 3.33 3.33
32.38 32.38 32.38
39.2 40.8 40.5
0.090 0.099 0.097
0.093 0.093 0.093
0.090 0.093 0,093
(Saturated)
G P043AS - 0 2 27 22-Rr - L298 Page 93 of 278
LowLoad Run #1
Loetlon: HuntlnSton 2
L@d (Mwl: 188
oate: 4lBlm23
StartTim€: 14:29
EndTime: 14:34
Probe / Gas Data
Adjusted Results
Va(avgl: 24.54 W*c
Clsw: 36,L25,759 ssrtlht
Osd: 32,772,2U
Prcbe *1 Rm: 0 degrecr
Prob€ f2 Rel 0 deg.eci
Prcbe #1 Rso: -33 dcSrer
Probe s2 &Lo: .12 d.t ..!
B$: 0.0928 %/100
Md: 30.10 lb/b-mol.
M.: 28.98 lbflb-molc
Pb.: 23.38 in Hg
P.: .4.30 in H2O
P,: 23.05 ln Hg
%COr: fl.o X
%O2t 85 rA
%CO, 0.0 %
80.5 X
Flow RATA Traverse Data
Polr* lD Probc lD
Corrlded
StaclTcmp YawAngle YlwAnSlc Pl-P2
(R ldel o-(del (in H,ol
Unadlusted Replicament Polntu*d SWAF
Axhl vclcity Axhl Veloclty tor Points
V. (ftlnc) v. (ft/*c) wAF? Usedc-
001 105 0 0.1s o.423 25.O72
oo7 r0s -o_8 0.1s 0.8230 2S.053
003 106 -l 0.2 0.14 0.8230 24.227
004 105 0 7.2 0.15 0.8230 25.0S0
m5 106 0 7.4 0.13 o.8230 23_?40
006 105 t.2 0.13 0.8230 23.340 nla
007 106 -1 0.2 0.15 0.8230 25.O77
008 2 t0s -2 -0-8 0.16 0.8230 25.e74
009 105 3.3 0.1 0.8250 22.421 nla
010 104 0 3.3 0.14 0.8250 24.203
011 105 -3 0.3 0.16 0.82S0 25.939
t05 -q 1 o17 o 4250 26.750 n/a
013 103 1.3 0.12 0.8250 22.419
014 105 0.3 0.15 0.8250 25.116
015 106 4 -o.7 o.15 o.8250 25.961
016 106 4 -o7 0.t7 0.8250 26.750
lverales 105.3 -r,7 0.5 0.15 0.82/10 24.788 nl. nl.
G P043AS-0227 22-Kf - L298 Page 94 of 278
Low Load Run #2
L@tlonr Huntlruton 2
t€d (Mw} 189
Date: 4ltllzo2t
Sta.tTime: 14137
EndTimer L4:41
Probe / Gas Data
Prcbc #lRe: 0 d€gr€ss
Prcbc *2 Re: 0 defees
Probe*l &@: -33 degrees
Probe*2Rso: -12 detrees
B*r 0.0928 %/100
Md: :X!.10 lb/b-mole
M.r 28.9t lb/lb.mole
Pbi 23.38 in Ng
P.: 4.30 ln H2O
P,: 23.05 ln Hg
%COr: 11.0 %
Kr'-----------9i*
%CO: 0.0 X
Flow RATA Traverse Data
Polnt lD Probr lO StackTemp
(R
coil.ded
YawAntle YawAntlc Pl-Pz
(desl O. (dsr) {in H,0}c-
Un.dlustcd
Axl.l VclftIty
v.(tvsl
Replffi€nt Point Us.d f WAF
Axial Velclty lot Points
v,(ft/scl wAF? Ured
oo1 105 0 1.2 0.14 0.823 24.200 n/a
o02 105 -2 -0.8 0.15 0.8230 25.075 nla
003 -3 1.8 0.15 0.8230 25.055
004 2 -3 o17 0.8230 )6 6U
00q 1()4 0 t.2 0.13 0.8230 23.299 nla
006 105 -1 0.2 0.14 0.8230 24.205
007 106 -2 -o.8 0.15 o a2?o 25.O7S
o0a 0 L.2 0.!7 0.8230 26.691
009 103 0 3.3 0.11 0.8250 21.434
010 104 1_3 o.14 o-8250 24.437
011 106 -3 0.3 0.17 0.8250 26.761
012 105 -3 0.3 0.16 0.8250 25.939
013 103 0 3.3 o.12 0.8250 22.387
014 105 -1 2.3 0.14 0.8250 24.245
01s 10s -)0.16 0.8250 25.933 nla
015 106 -3 0.3 0.17 0.8250 26.161 nla
lverales 105.1 -1.6 0.7 0.15 0.82'l{t 24.874 nla nla
G P04 3AS -02 27 22 - RT - t298 Page 95 of 278
Low Load Run f3
Location: Huntington 2
Load (Mw): 188
Date: 4lBlm2,
StartTimei 14145
EndTimei 14:51
Probe / Gas Data
ProbeflREo: 0 degrecs
Probef2RDo: 0 degres
Prcbe #1 Rao: -33 dcgrces
Ptobe *2 Rao: -12 degrccs
E-: 0.0928 961100
Mdr 30.10 lb/b-.molc
M!: 2E.98 lb/lEmolc
Pbi 23.3E ln Ht
Pr: {30 ln H2O
P,: 23.06 ln Hg
,t4r.O.t l,..O 't$
%Or: 85 %
%CO: 0.0 96
| 80.5 t6
Flow RATA Traverse Data
Polnt lD Probe lO
Correct€d
stlctTemp YswAngle YrwAnglc P\-P2
tn ld.rl o ldcd fih H"Ol
Unadrustcd Repl@ment Polnt Used # WAF
Axlalvelctty Axialvelocity tor Polnts
v-llt/secl v.tttl*c| wAF? t tedL
001 1M -2 -0.8 0.13 0.82 23.302
002 2 t06 -2 -o.8 0.15 0.8230 25.a97
003 2 106 0 L.2 o 16 0.8230 25.894
ooa 2 to7 0.2 0.15 o 4230 25.099
005 2 t05 -2 -0.8 0.13 0.8230 23.323
006 2 tol -3 o1a 0.8230 24.236
007 2 105 -3 1.8 0.15 0.8230 25.055
008 106 o 1.2 0.16 0.8230 25.894
009 1 103 -2 o1)0.8250 22.4L9
o10 105 .3 0.3 0.15 o 4750 25.116
011 106 4 -o.1 0.15 0.8250 75 961
072 1 106 o_16 0.62s0 25.9s6
013 1 103 -1 2.3 0.12 o.8250 22.406
014 105 -3 0.3 0.14 0.82S0 24_264
015 106 -3 0.3 0.15 o 8250 25.138
015 105 )1 o 17 0.8250 26.740
,eiag6 105.4 -2.O 0.3 0.r5 0.E2'{,24.794 nla nla
G P04 3AS -0 2 27 22 -RT - t298 Page 96 of 278
Low Load Run #4
Loetion: Huntlngton 2
Ioad (Mw): L87
Date: 4lt3l202,
Start Time: 15:15
EndTime: 15121
Probe / Gas Data
Adjusted Results
Va(avg): 25.04 ft/ec
qsw: 36,790,75O wsllht
33,357
ProborllRDo: 0 degreGs
Probe #2 Reo; 0 deg.Ges
Probe f1 Rflo: -33 degrccs
Probe f2 &!o: -lJ d.gres
E .: 0.0933 %/10o
Mdr :10.10 lb/Emolc
M,: 28.97 lb/b-mote
Pb,: 23.:18 in Hg
Pri -4.30 in H2O
Pr: 23.05 ln H8
%COr: 1lJ %
XOr: 8'5 ,{
%CO: 0O %
%
Flow RATA Traverse Data
Polnt lD Probc lD
coredcd
StlckTcmp YrwAngle YawAntle P1-P2
(F) (d6sl q(des) (ir H,0)
Unrdlustad Rcpla@mcnt Point Us.d #WAF
Adll Voloclty Axial Veloclty for Poirts
v. (fvtacl v. (ltlscc) wAF? Ucdq
001 105 -0.8 0.13 0.823 )?7?S
oo)107 .3 -1.8 0.16 0.8230 25.9L2
003 107 .7 -oa 0.15 0.8230 25.923
004 107 0.2 0.16 0.8230 25.9)S
005 107 .2 -0.8 0.14 o.8230 24 )44
OG 107 0 1.2 0.1s o 4730 25.096
007 t07 0 0.8230 26.717
008 to7 0.t7 0.8230 26.723
009 106 1.3 0.13 0_8250 ,3 lqC
010 106 -3 0.3 o.15 0.8250 25.96s
011 106 o3 0.16 0.8250 25.965
o72 106 -3 0.3 0.17 0.8250 26.7il
013 -l 0.12 o.4250 22 444
014 106 1.3 0.15 o ar50 25.134
015 105 -3 o.3 o 1q 0.8250 25-140
016 t07 -)0.16 0.8250 25.981
lveraSes 105.4 -1.9 0.4 0,15 0.8240 25.292 ala ^le
G P04 3AS -0 2 27 22-RT - t298 Page 97 of 278
Probe {1 RM: 0 degrees
Probe f2 Re: 0 degrees
Prcbe rl1 Rao: .33 degrecs
Prob€ *2 Rsro: -1.2 defees
B-: 0.0933 ?6/100
Md: :r0.O lb/b.,mol.
M,: 28.97 lb/lEnol.
Ph,r 23.38 in Hg
P.: -4.30 in HrO
P,: 23.05 in Hg
%COr: U.0 %
%o, : --------------:L1 96
%CO: 0.0 96
E0.5 t6
Low Load Run #5
L@tiffi: Huntinllon 2
tord (Mwl: 188
Date: 4ll3l2023
StartTime: 15123
End Time: 15:29
Probe / Gas Data
Unadiusted Results
[avg]: 25.15 fvs.c
qsw: 37,069,333 wscflhr
Flow RATA Traverse Data
Point lO Plobc lO
Corrected
StackTemp YrwAriglc YawAngle ?l-P2
(Fl (ded Olded (lnH,o)
Unadrustrd Rcpl.emcnt Poant Used * WAF
Arial Velocity AxiEl Velodty for Polnts
v-lrt/sec) v.tlt/*cl wAF? Uied€"
001 10s -2 -0.8 0.13 0.823 25.375
oo?10s -o3 o17 o a2to 26.673
003 106 3 .1.8 0.r7 0.8230 26.686
004 to7 -1 o.2 0.16 0.8230 25.915
oo5 1S o o.la o 8230 )a ))n
006 106 0 t.2 0.15 0.8230 25.074
007 106 1 o.2 o.t7 0.8230 26.699
008 2 106 2 -0.8 0.1s o.8230 25.O77
oo9 103 0.13 0.8250 23.324
010 103 1 2.3 0.14 0.8250 24.204 ala
011 104 0 3.3 0.15 0.8250 25.0SS
01)104 o 16 o a?50 25.9r9
013 103 2 1.3 0.14 0.8250 24.2r7
014 103 1 2.3 0.14 0.8250 24.204
01s 103 2 1.3 o_15 o 4250 2\ 067
103 0.17 0.8250 26.686
lV€rales 104.6 -1,4 0.8 0.15 0.8240 25.148 nla nle
G P043AS-0227 22-RT - 1298 Page 98 of 278
ProtE#lRDo: 0 degecs
ProtE f2 RM: 0 detree3
Prob€ fl R.6: -3.3 deare€s
Prob€i2&Lo: -1.2 dcSrGGs
8s: 0.0926 %/100
Md: :10.10 lb/lb.mol.
M,: 2E.9E lbllb-mol.
Ph,: 23.36 In H8
Pr: .4.m ln H2O
P,: 23.06 in H8
%co,:----iE9%
%o, : -------------:L1 %
',&Ot 0.0 %
: 80.5 %
Low Load Run #6
L@tioni Huntlntton 2
L@d (Mwl: 186
Date: 417il2023
Start Tlme: 15:31
Endllme: 15:37
Probe / Gas Data
Unadiusted Results
avg,: 24.86 fVscc
Qsw: 36,72L,555 wdlh.
Flow RATA Traverse Data
Polnt lD PJobe lD
corlccted
StackT.mp YawArUle YlwArtle P1-P2
(Fl (d€81 Q (ded (ln H,0)
Unadiusted RcphcmCnt Point Us.d fWAf
Axial V€l@ity Axhl Velctty for Polntr
v, (fvsl v, (tV*c) wAF? Usadc.
001 105 o.2 0.13 o.423 21 12?
002 o.2 0.1s o arco 25.053 nla
003 104 -1.8 0.16 0.8230 25.840
004 104 -0.8 0.16 0.8230 25.850
oo5 103 -2 -0.8 o.r2 o.azo 22 167
006 103 0 o7l 0.8230 24.156
007 103 -0.8 0.15 0.8230 25.007
008 104 -0.8 0.16 0.8230 25.8S0
009 103 1.3 o_13 0 8150 11a
010 103 0.15 0.8250 25.064
011 103 -3 0.3 0.16 0.8250 25.492
012 103 .2 1.3 0.16 o.4250 ?g 889
013 102 -3 0.3 o.13 o.4250 ,3 114
014 102 .2 13 014 0.8250 24.t92
015 10t 1.3 0.15 0.8250 25.885
016 103 -3 0.3 o.17 0.8250 26.649
rverag€s 103.3 -2.0 0.3 0.1s 0.42/lll 24.ASC nle alz
G P04 3AS -0 227 22 -RT - L29 I Page 99 of 278
Low Load Run fl7
L@tion: Hurtirylon 2
to.d (Mwl: l9O
Date: 4ll3l202l
StanTime: 15:39
EndTlme: 15:45
Probe / Gas Data
t,, 111
g-;;| t;ii J^P,il]\ tH'li[i1'r"i''i':'"rrnu ct IAqlll
i,rAY - g t:i',3
!
AIR OLIALITYot
Probe f1 Reo: 0 deg?ecs
Probe i2 Re: 0 de&ees
Prcbc sl Rro: -33 detrees
Probe*zqro: -12 defcet
E-r 0.0113 %/100
Md: 30.10 lb/lb-mol.
M,: 29.01 lbllEmole
Ph,: 23.38 In Hg
P,: .4.30 in H2O
P,: 23.06 in Ht
COrt \1.0
"4
"1O2t
85
%CO: 0.0 %
| 80.5 X
Flow RATA Traverse Data
Polnt lO Prob. lO
Co.rected
StackTemp YrwAngle YrwAnde Pl-Pz
aFl ld.d d lddl llr H-Ol
Unadiusted Rcpl.cemcnt Point U$d f WAF
Axial Velo.ity tuirl Ve l$lty lor Polntt
V-tft/iecl v-.ft/*cl wAF? t r.dL
001 \o2 1 o.2 0.14 0.823 2t 1)e
002 702 2 -0.8 0.15 0.8230 24.973
003 o.17 0.8230 26.599
004 103 2 -0.8 0.17 0.8230 ?6 60q
00s 102 0 t.2 0.14 0.8230 24.L23
offi 10)-1 o.2 0.1s 0.8230 24.975
007 t03 -1 0.2 0.16 0 8730 )s 417
008 103 -3 1.8 0.16 0.8230 25.805
ooq 102 1.3 0.13 0.8250 23.301
010 t0l -2 0.14 o 4250 14.159
011 L02 1.3 0.16 0.8250 25.851
072 103 -l 2.3 o.17 0.8250 26.555
013 t03 -2 o 4250 21.407
014 103 -L 2.3 0.15 0.8250 25.038
01s 103 -2 1.3 0.16 0.8250 25.874
016 t03 7 o a?so )6 655
qverales 102.5 -1.6 0.6 0.15 0.8240 25.185 nla nla
G P043AS-0227 22-Rr -1298 Page 100 of 278
Probe fl RDo: 0 ditl@s
Prob€ f2 R&oi 0 degres
Prob€ #1 Ri@: -33 de8,es
Prob€f2Rlro: -l.2 degres
B-r 0.0933 %/100
Mdr :10.O lb/b-mole
M,r 28.97 lb/lb-mol.
Pb,: 23.38 ln Ht
P.: -4.30 in H2O
Pr: 23.05 In Ht
%COr: l1.0 %
%Oi a.5 %
96CO: 0.0 %
80.s %
Low Load Run f8
LGtlon: HuntlnSton 2
L€d(Mwl:
DEte: 417t12023
StartTime: 15{7
End Time: 15:53
Probe / Gas Data
Unadiusted Results
lavtl: 25.53 ft/scc
Qsw: 37,558,904 wscf/hr
Adjusted Results
lawl: 25.27 ftlsec
Qsw: 37,L93,215 wctlht
Flow RATA Traverse Data
Polnt lD Probe lO St..k Temp
(Ft
Corrrctad
YawAnSle YlwAngle P1-P2
(d€sl Q. (del (in H,0)c"
Unadiusted RCphemcnt Poilrt Us.d
Axial Vel@ity Axltl VclGtty lor
V.lftls) V- ItVscl wAF?
* WAF
Pointr
Ui.d
001 106 -1 o.2 0.13 o.423 23344
60)0 t.2 0.16 o a2e0 25.895 n/a
003 106 -3 0.17 0.8230 26.646 n/e
004 -3 1.8 0.!7 0.8230 26.646
00q 105 -2 -0.8 o.14 o 4230 24.205
006 106 0 o rq 0.8230 25.074
007 107 -l 0.2 0.16 0.8230 25.925
oo8 L07 1 o.2 o.L7 0.8230 26.723
009 104 2_3 o 4250 23.344
010 t04 1.3 0.15 0.8250 25.090
o11 t05 3 0.3 0.17 0.8250 26.740
105 2 1.3 o.t7 o.4250 78714
013 104 2 1.3 0.13 o.4250 23.157
014 10s -1 2.3 0.15 0.8250 25.921 nla n/a
015 105 -l 0.3 0.16 0.8250 25.942
015 106 0.77 0.8250 26.743
wenSes 105.4 "1.5 0.6 0.15 0.4240 25.s26 nla alz
G P043AS-0227 22-RT -t298 Page 101 of 278
Low Load Run llll
Lo6tion: Huntlngton 2
t@d (MW): 188
Date: 4ll3l2023
StartTimc: 15:55
End Timei 1601
Probe / Gas Data
Probe #1 R@: 0 degraes
Probe #2 R6: ! {gg1ss5
Probe #1 &p: -33 deSrccs
Probe f2 RsLo: -12 d.t.e.s
8*: 0.0933 %/100
Md: 30.10 lb/lb-mol.
M,: 28.97 lb/lb.molo
Pbi 23.38 ln Hg
P.: -4.30 in H2O
Prr 23.05 h Hg
',6CO2t fl,o
"$%Orr 85 %
%COr 0.0 9(*
Flow RATA Traver$e Data
Polnt lD Probe lO
Corrcded
SttrtTemp YawAntl€ YawAngle Pl-42
(R (del o. (d4) (in H,0)
Unrdrurted RCplacement Polntused #WAF
Arislvelcity AxiElvclocity for Points
v. lft/*cl v.lfv*cl wAF? UsedC.
001 102 1 o.2 0.13 0.823 23.265
002 103 0 t.2 0.15 o.8230 25.A2a
oo3 105 o 0.15 0 8230 )s os)
004 2 .0.8 0.17 0.8230 26.697
005 106 0 L.2 0.13 0.8230 23.343
006 106 2 -0.8 o.15 o a2zo ?5 9m
007 106 3 1.8 0.0.8230 26.646
008 105 3 .1.8 0.0.8230 25.585
009 102 1 0.o 8250 )) 149
010 104 1.3 0.14 0.8250 24.239
011 105 2 1.3 0.15 0.8250 25.tt2
o12 1 1.3 0.15 o 8250 )s 9u
01?10q 1.3 0.13 0.8250 23.374
014 106 2 1.3 0.14 0.8250 24.242
015 106 -1 ).3 0.16 0.8250 )s 944
016 106 0_1 0.8250 26.751
rverages 105.0 -1.5 0.8 0.15 0.8240 25.094 nla ila
G P043AS-0227 22-RT - 7298 Page 102 af 278
ruT,11lf,f:
IATA lsrrf I -< Itt^t Et Erlxl:
ftertfhr:tqa?-l}Tdl..tOrrcl Ar a6
llocTlmr:l( o2-t t-T.$r..t6d h.dEh) - orr
S.mplc
TllrE
,rlia Pr.sn
S.trtCc
voerruIfrl DGrTcmpl'$
lnht o0d.t
lilp.Ord.t
Ttrpl'fl
,
Urqrrn
t'lilaHrHpll-Zl L^r),r\t1?-llon'\fat
nA .4a -V ('t 7rt ,,laa-+z-<t€Zaq-r^, TL t I7J^
?fi .?lil(.#o \\.X 4q n 2
La
(0-0)(o.mol (0.0)(0.01 (o.o)t.5
hdnt r
lmCr5 l
tllgll|t?
trrFat|tt
lmpltfrr
lmrt hlrsr
UITA&rrl q -q l*Q f [a,y !i(rl:
brtftr:t4 ,<td.rtLrlorcd rt-aa li -* 'lbtftn:lbnE bit ri.tlr.tor.di b.a'QI
SrnplC
Ih.
)rifrohtgrl
axrHlol
S..'rrac
Udllnftff ocmlarpfO
hltt Odrt
hnp.Odrt
Iorupf0
Vrcumr
rloZao-ZZa
Itt ,.Y-'ar5.k{L 5Y7a.q 5(t(D -?
?x ?1r ^?lf{3t)??1fn :+rl :h 3 E??(x -J-5 t'lL?l q 75 )
-5l'l r--l-r)u I -'aal-l.rt) 2
&4 5d
I
Ir{thl Fhrl
-*v.x 5*a4
,lZt,a ,17?.y
3L5.\9sa1
5zS.u 53",?
/r33 *t?6q.3
7o,l
G P043AS -02 27 22 -RT - L29 I Page 103 of 278
EPA tethod 2F'Fast Flof. Datasheet
pi'' ; ' I i'fl'\.' l 'i ;' ,':'{, r,, t':
' : llE i'.'lltl. ,.rrtr. rr
I PtdrctCod.[h*'.- n,rl)Zlo lrunettPlunl'15:L3 -3{lE
Blrlrt 0d (',o"0 fficPnurel'llfl:- -UrV lro
lqnne:r(rurta ir,-PnobrtD/lhrlrm :on n+Macodlthn t/
DoarEr{rl:tnvJ ltr-lDGqudrlD fr(.i*6,&ff!ll,arc4lr\l L\[rtCltrdl'llzoh 4-'o "Dr lral 9,5
hm,Lor., fr.t l Erilfhn3 tqLq Stofhns:tq?.t
Ileusreffi
lPqlrdro
hrtTurt
(tt
YrrAlth
iD.r
ItdodUlPl'llpl
171+2t
PUrlPl'Hpl
ln.+st
Eillman|ts:
1.I t^L o D,I S AIAL,o<-7 D.'<I3lt\t D. tqtllatr.r)1).,<,J ,/\A D o.13aloho0, tE
3 til.I 0,1|
u th5,L o.lA
frltt L ptr, Ft"ul SrtTtnr:I Ll1?;lbDfhrcE _ tlly?
Port
$rrtlaq
rn
Y.xAnfh
iO.!
l,bh.ry.P fHpl
lPr+21
rurapfHpl
lP.45l
ColnrDctttr
ti loS o D,lU A)*
?lnlo -7 h.tK
1 rnL -?A. i<q lr).?o,17
Z)I to.u o n-, i
?^tDt h. tt-,l
lo(a--L o-,5
U ,A h b. t-
ruat l-3 bs fi"i *rrtfhr:turtS iDThr:t4<l
lort
Yilltlhrr l,lloclt,tPfHpl
Gr+21
ry rr[l
rn
PndrtPfllpl
lPtr+51
Eamt:nt!:
T)(lbrl -L o. r<rtfhzlolr.tL
3 lnL rl o.\l ln:A. r(h l-6I -1 O. t?L ID?-Z D. lrl
3 loh _?D.r('
U D r)n tl^
G P04 3AS -0 22 7 22 - RT - t298 Page LO4 of 278
EPA tettrod 2F -Fast Flouf Datasheet
rj'';;,
hCCdGd.fifii -o?Lue irncnrtthlrrcrllltt:23.\rr t-Ihr I AL.I('.-.rt ffiPnrm|.]t0h -tl.f ll!lrlu:*orr u:Pr6rlD/th;run rq<httOnffion ,/Wltk fDGqrdrlD ?t\ -7 EIlxt It"oD.E
-4 hl lzr l..rtffil'lLol:'a-2 rt qor,9. {
G P04 3AS -0227 22-RT - L298 Page 105 of 278
EPA Ueffiod 2F'Fast Flow,, Datasheet
ti'r." , I i1i,'i:l^, l ,l ;. r':'d" r, :. l'l
nlti l-lilllFt .rItr..trr
ErclCodr fiCti -t<7? zaa lrrurtt?nanr:l'tll:z-l,I X ir-
Ihft t 0.i*".^o ffiPnrrnl'll'Ol:-rl.B h"
lqrcr:* Nttr i7-ldrlD/Albnrnrt il+tdrCadldorl V
DD.]llrbh r*u)-Te-fDfrohlD (tv)3+F rl5-0qlrl Ir. o&:LI l'tl hrlOrdPHrol:3.?'oro.t F.3
G P043AS -02 27 22-Rr - L29 I Page 106 of 278
EPA tlethod ZF *Fast Flow" Dahsheet
ii"t;' I
PruhEiGodr 0ra'i - o22-V?7 llunrttPnrnrtI.lIl:7\.1 r LEIhntr-dS-'o.-ffiePrsraf}t0h ,-. -'/'(Nrolorta:HTfitr rr.z-UeD/Atmom Ld4P tf?hobrcddlUon VJDCftmflg:lA'.,\ I tV lD Cotrh tD:?N-7 DrTXT t'l .oil I ta,l?-\lrrlolrttfhoh t/L(xl 8"5
rr l{ I,eu fh")Itrrttlncr t-5tS lhDltm:15z- tthu:r:Poh
IE*eom
Strc}Tcml
fFt
YilAtth
tDGI
vdoGfriPfHpt
lPt+2t
FHraPfl&ol
lFt+51
Eqnnq*s
I ItL -2_6.r1 nb
?-tnL -?o.ir I3lnLO.t,\vl l".l -t f). I r
tA t trr 5 O. t"L(L lnl -7_O, t53lo-?D. l5
L lo?-1 rr.lL
runl 15 l-a^t E ltrtllnn:t<L<lotImr:l.<21
,ort
SlrdrLmj
(Tt
VruA4h
tDlr
VclodlAPfHr0l
Gr+lt
HdlaPrHrol
lRr.Dsl
csmmantr!
4 I loz D,r<ht*L ln?-l o. rrl I3t rti;D f).,tqlol*2 b" ll-
,o3 *7 D,,tl
7-lo.-l o,lL3loza-4 o ,13
t{/oa -L ^l+
G P04 3AS -0 2 27 22 -RT - t298 Page tO7 of 278
EPA mefiod 2F "Fast Flow, Datasheet
l,n
lrohttcodr fitfi- oflaa2 lrruntlcPnrnrnt lH:z<.?,r irmTh'0).i.Jetrtr fficPrrml.lllol:-A'?[lolilm:l{srrt' i PruhD/thmqlG r[?hdrffiUon r/qFrfrrt+_ t*d lTt lD hude lE ms -l^EorlIl ,l -oDTE;tl lt rL<rlrcrti|-lliol:?.9 fl orlxl E.s
r'nt I ? lour-EJ hrtltrrrr 1531 Sllmc:t-<4<]lorrlnfit
t9amotrd
IrtTanf
fn
f,fr15i
tDrr
lrdodElPfHpt
lPl+tD
ffir.tfHpl
lxao,
Cuunomr:
JI\I laL b,lLl _ilnL/')-lou -z l),1I3/o?-?n. lf-
U /D1 -q o,ta
Z t loL D o, r(
2^tbL o, t5'3 /a-3 b,l tlrllt)-t o, ll-,
G P04 3AS -0 227 22-RT - t298 Page 108 of 278
EPA toffiod 2F ,Fast Flou/, Datasheet
iy.,;', i'r'it,!'l ;. r'.i l,;I:
' : rlli r_t'llt,t\ Jrnl.r.rjr
ffiCodr Ot;- t7r4+'r,luqnrtt Pfr:rrnPlIl:z.3.jr(lrofrl'G _.d*,\{.ro*Idc?nnmFltd:- u,z ho /lqlr:ttttlTct rl2-FldrtD/Afin.t'r i<Plot!CordHon t/DpGilEbl:c/fvJ I lL !DGqldrtD 3D-2_Eltrl tt,ahEAhlz<IsrqtGq(.ltp]3.9 lt Dr(It 8, t'-
frtn, l?br.tdJ ilrtfhtr:1539 lunnr:t 5ls
hnunratr:IlrrrsFft
tEr}Fffi
HTml
Itl
ll:At;h
iElt
rrdr*.Pfirrq
Itr-r:rl
HraPfHpl
mr+rt
f:I loL -2 o ?NT?v 1-lol -2 O-ttt
I o7-o.ltvlll't?D- l=l-
m lD',-2_z)-l LY1?/o\D.l 5
a ,6-3 .L o,l6ulo3A..i<-*
-
t <U+ Ad)lrtlnt- l.eu Flort htftrrr 4i-
vdo.ry6PfHpl
lPl+21
holanr:Etr+ /gsB
tott
Yrrfl|h
tE(Tl
HraPfHrol
lD..nrl
lonmcott:
A"I lo4 D,17 ila?-tbl *1 b.l<3 lot -t 0.ll
t{IDE -7 D-11ll-II tou *1-D.13V2_tD,D,lt
?,65 -?D
L,tr,*l A- ta
vutt lTlan^tFl.-l Itrtltnr:t Sss lbtllnr:J6ot
h8
tlfA[h
thr
t UoftrtP fHpl
lPr+i[
.H tuttl
(Tt
FUr !t fllpl
lf,Jst
IEunrnertr:
9 t loL D.IL
^IA?-lb4 O-ru
3 to(-7 D.IJ
}\.f lnL D.IA
H]ln5 -2-D.17
?*tnh *Z D.1.1
1 TDh -l D-lc
It In ,IL n-lf,T
G P04 3AS -02 27 22 -RT - t298 Page 109 of 278
Appendix A.3.2.2
High-Load Flow Data
G P04 3AS -02 27 22-RT - t298 Page 110 of 278
Client PacifiCorp
Unit lD Huntington 2
Load High
EPAMethod3&4Data
lnputs
Barometric Pressure ("Hgl
Stack Static Pressure ("HzO)
Oz (%vd)
COz (%vd)
Vr" Volume of Water Condensed (mL)
V. Volume of Stack Gas Collected (dcf)
Y Meter Calibration Factor (unitless)
AH Pressure Differential Across Orifice ("H20)
T. Temperature at Gas Meter ("F)
Calculations
Pm Absolute Pressure at Gas Meter ("Hg)
T. Absolute Temperature at Gas Meter ('R)
Vwc(*d) Volume of Water Condensed (scf)
Vn(stu) Sample Gas Volume (dscf)
Stack Gas Temperature ('C)
B*.", Saturated Moisture Content (y"/100)
Bffi Measured Moisture Content (7y'100)
B*, Stack Gas Moisture Content (yol100)
23.45 23.45
-4.50 -4.50
5.5 6.5
L2 t2
191.1 191.1
90.293 90.293
0.999s 0.999s
1.7 r.7
53 53
23.58 23.58
523 523
8.99 8.99
7t.76 77.76
42.3 47.5
0.L07 0.102
0.111 0.111
0.107 0.102
(saturated) (saturat.d)
759.7 159.7
75.67 75.67
0.9995 0.9995
1.7 L.7
70 70
23.58 23.58
s30 s30
7.52 7.52
59.34 59.34
42.5 42.5
0.108 0.108
0.7L2 0.1t2
0.108 0.108
162.4 L62.4 162.4
74.3 74.3 74.3
0.9995 0.9995 0.999s
1.7 L.7 L.7
70 70 70
23.58 23.58 23.58
530 530 530
7.64 7 ,64 7.64
58.27 58.27 58.27
42.5 42.6 42.6
0.107 0.108 0.108
0.115 0.116 0.115
o.to7 0.108 0.108
23.45 23.45 23.45
-4.50 -4.50 -4.50
6.5 5.5 5.5
1,2 t2 L2
191.1 t59.7
90.293 75.57
0.999s 0.999s
r.7 L7
63 70
23.58 23.58
s23 530
8.99 7.52
71.76 59.34
42.0 42.6
0.105 0.108
0.111 0,L72
0.105 0.108
23.45 23.45 23.45 23.45
-4.50 -4.50 -4.50 -4.50
6.5 6.5 5.5 6.5
72 L2 t2 72
(Saturated) (Saturated) (Saturated) (Saturated) (Satur.ted) (Saturet.dl (Saturatrd)
G P04 3AS-0 227 22-Rr - L298 Page 111 of 278
High Load Run #1
L@tiq: Hun0ncton 2
tod (Mwl: tl81
O!tc: 4ll4l2023
St.rtTlm€: 9:0t
EndTlme: 9:46
Probe / Gas Data
Adjusted Results
Va(avg): 55.26 ft/rec
Qsw: 82,599,010 wrcf/hr
PrcbGflReo: 0 degect
Prcbc f2 REo: 0 defees
Prcba ltl &6: -33 degGas
Probeil2Rsro; -1.2 drtrces
8-: 0.1066 161100
Md: :lo.t8 lb/lb-mol.
M,: 2E.8E lb/lb-mole
Ph,: 23.45 in Hg
Pd 4.50 in H2O
P,: 21U in H8
''lCO2t ,'2.O 'h.r6o2t 6.5 'k
9{CO: 0.0 9(
t1.5 %
Flow RATA Traverse Data
Polnt lO Prcb€ lD
Correded
St.clTcmp Y.wAryle YrwAnde Pl-Pz
lFl ldel o..rderl lln H"ol
Unrdrustcd RCplacment Polnt Usd *WAF
Axlslvel6lty Axialveloclty for Points
v- lftlsl v- lftlo.l WAF? t sedc
001 t07 -5 -3.8 0.68 0.823 s3.346
60)10a .3 -1.8 o.7a 0.8230 57.243 nla
003 108 .3 0.77 0 82ao 56.914
004 109 1 0.2 0.78 0.8230 57.361
oos to7 4 -2.4 o.70 0.8230 54.180
006 loa o)07s o-4230 s6.198 ale
007 108 -L 0.2 0.77 0.8230 \6 9!)
008 2 108 -2 -0.8 0.80 0.8230 58.035
om to7 1_3 o.73 0.8250 55.485
010 108 -2 1.3 0.78 o a?50 57.435
01 109 .3 0.3 0.E0 0.8250 58.232
o1 109 .2 1.3 0.82 0.8250 58.941 nla
o1 108 )z o6q o.4250 s3.991
014 109 -1 2.3 0.79 0.8250 57.a27
o15 109 0 3.3 0.80 0.8250 58.137
016 l09 oe)0 ar50 5a 941
lYerag€s 108.2 -2,O 0.3 0,77 0.82/O s6.828 nla nla
G P043AS-02 27 22-RT - t298 Page L12 of 278
High Load Run#2
L@tionr Huntlngton 2
lod (Mw): 'tEoD!te: 4lt4l2023
St rtllm: 10:00
EndTim!: 10120
Probe / Gas Data
ProbcrlRe: 0 dagr.cs
Probc f2 Re: 0 dsgt6.s
PEbr fl Rs@r -33 degrcs
Probo*2Rno: -t: d.gret
E .: 0.m24 X/100
Md: :t0.18 lb/b.,mol.
M.: 2E.93 lb/b-mole
P"n_3Mtn H8
Pr: 4.50 ir HrO
P,: 23.12 in Hg
%to2. 12'0,,1
%Ozt dS %
,{COr 0.0 %
| 81.5 %
Flow RATA Traverse Data
Polnt lO Prcbe lD
Corrected
StrdTemp Y.wAnde YawAngle Pl-P2
(F) {des} q(de8} (h H,0)
Unrdrusted Replaemont Polnt Used #WAF
Axialvtlciv Axi.lveloclty lot Polnts
v. (rvs) v. (ft/ec) wAF? t .€dc-
001 1t)6 o7 0.68 0.823 53.369
002 107 0.2 o.75 0.8230 55.099
003 r07 -2 -0.8 o.7a o.4230 57.204 nla
004 107 -2 -o.a o80 0.8230 57.933
005 101 0 2 0.70 0.8230 54.185
0m 107 -2 -0.8 0.73 0.8230 55.340
007 107 -1 o.2 0.80 o Srto 57.93E nla
008 107 4 -28 041 0.8230 58.230
009 1ffi 1.3 0.70 0.8250 s4.264'
010 to7 -1 0.85 0.8250 59.819
011 t07 .3 0.3 0.84 0.8250 59 513
o72 to7 .3 o.3 o_90 o 4750 61 60)
013 105 1 2_3 o_70 0.8250 54.231
014 107 2.3 0.82 0.8250 58.754
o15 707 -l 2.3 0.84 0.8250 59.466
016 707 -2 1.3 o.91 o a?so 6r qra n/a
lverates I05.E -t.7 0.5 0.79 o.a2&s7.493 nla nla
G P04 3AS -0 2 2 7 22 - RT - L29 A Page 113 of 278
Prob€ ttl Reo: 0 deSrees
Prob€ 12 Re: 0 degrccs
Prcbe*lRsr -33 deSrees
Probe *2 Rao: -12 dcgrccs
B*: 0.1(R6 %/100
Mdr 30.18 lb/b-mol.
M.: 2E.91 lb/b.molo
Pb,: 23.45 in Ht
P.: 4.50 ln HrO
P,: 23.12 in Bt
gl,Cozt l2.O %
Y&2, ___________9!%
%CO: 0.0 X
: t1.5 %
High Load Run #3
Locationi Huntington 2
toad (MW)r '183Date: 4l,q2023
Start Timr: 10:36
EndTim.: 10:56
Probe / Gas Data
Unadiusted Results
fVrcc
Qsw: 85,454,995 wcf/hr
dscf/hr
Adjusted Results
avgl: 57.56 fVsec
Qsw: 84,500,t145 mcf/hr
Flow RATA Traverse Data
Polnt lD Probe lO
Corrected
Stocktemp YrwAryle Y.wAngle P7-P2
td ldel a ldarl lin H-Ol
Unadiusted Rcplaement Polnt Used *WAF
Adsl Vclcity Axial Vel4ity lor Polnts
v lftls.l v lftlo.l WAF? U3edc
001 105 -3 18 o.71 0.823 54.533
002 2 t07 -3 08s o 8230 s9.721
003 2 108 -2 4.8 0.86 0.8230 60.148
004 t0a -t o.7 0.88 0.8230 60.849
005 2 LO7 o)o74 o.a230 ss.750 n/a
006 2 108 -t o.2 0.82 o a?30 sa 738
oo7 2 108 -2 {.8 0.84 0.8230 s9.444
008 t0a -1 o.2 0.90 0.8230 61.536 nla
009 1 t06 33 o67 0 arso s3.o41
010 1 t07 1.3 0.79 0.8250 57.728
011 108 2.3 0.83 0.8250 59.191
0t2 r08 1?oa5 o.8250 s9.933
013 1 101 1.3 0.67 0.8250 s3.163
014 109 -1 2.3 0.78 0.8250 57.431
015 loc 33 OM o.82S0 59.495
016 1 108 .1 2.3 0.E4 0.8250 59.547
107.6 -1.4 0.8 0.8t)0.82,t0 58.141 ala nla
G P043AS-0227 22-Rr -1298 Page 1L4 of 278
High load Run #4
Loetioni Huntington 2
t@d (Mw): 486
Dat.: 4ll4l2023
Start Time: U:12
End Time: U:32
Probe / Gas Data
Probe fllRe: 0 deSreGs
Prcbc *2 R@: 0 deg.c.s
Prob€ ln Rao: -3.3 degr€.s
Probef2RsLo: -1.2 dettees
8*: 0.10t1 %/100
Md: 30.18 lb/lb-mole
M.r 28.85 lbllb-molG
Pbr: 23.'15 inHt
P.: -4.50 in H2O
P,: 23.12 in Hg
9dcorr 12O %
'$O2t 5,5 %
%COr 0.0 %
Flow RATA Traverse Data
Point lD Prob. l0
Corr€cted
StrckTemp YawAntle YrwAngle Pl-Pz
(R (de3) q" (desl (ln H,o)
Unrdrustad Replacement Polrt Used rWAF
Axhl Vllcity Axlll Veloclty tor Poirts
V. (ftlE() V. (fv*cl WAF? usedc-
001 107 "3 -1.8 0.65 0.823 52.263
002 108 -0.8 o.72 0.8230 55.075
003 109 0 1.2 o.11 o 87?0 55.999 nla
004 109 o 0.80 0.8230 58,098
005 108 -2.4 0.14 0.8230 ss.774
oo6 109 .2 -0.8 0.79 o 8?30 s7 7t1
007 109 .){.8 o80 0.8230 s8.105
008 110 0.2 0.84 0.8230 s9.s98
ooq tol 0 3.3 0.69 0.4250 53 91q
010 108 2_3 o75 0.8250 56.308
011 109 1.3 0.80 0.8250 54.237
ot2 110 -3 0.3 0.84 0.8250 s9.743
o13 108 -1 2.3 0.68 0.8250 53.616
014 109 1 2.3 o.72 o.4250 s5 219
015 110 -2 07s 0.8250 55.438
016 t09 0.81 0.8250 58.558
lverages 108.7 -1.5 0.7 0.75 0.8240 s6.606 ala nla
G P04 3AS -0 2 27 22 -RT - 1298 Page 115 of 278
Prcbe #1 Reo: 0 degrees
Prob! f2 REo: 0 defees
Prob€fl &@: -33 degrees
P@b. f2 Rsro: -12 degrees
B-t O.l.O7, %ltOO
Md: 30.18 lb/b,mol.
Mr: 28.E7 lb/bmol€
Pb,: 23.45 in Hg
P.: -4.50 in H2O
P,: 23.12 in Hg
%cO2, 72.0
'ko2t 65 %
%COt 0.0 %
t{N,: 81.5 %
High Load Run #5
l@tionr Huntirytor 2
toad(Mlirl: 484
D8ter 4lt4l202,
StartTim.: 11:/8
EndTim.: l2t08
Probe / Gas Data
Unadiusted Results
Va(avg): 56.96 lVscc
Qsw: 81,57L,927 wrr,,/t't
Flow RATA Traverse Data
Point lD Probe lD
Corrccted
Stacklemp Ya*Ande YawAngle ?l-P2
(Fl (d€sl o- lderl (in H.ol
Unadlusted Rcpllcement Polnt Used # WAF
Axial Veloclty Axirl Volocity fo. Polnts
v.tftlsec) V.(ltl*(l wAF? U.edc
001 tol -2 -0.8 0.68 o.423 s3.4'12
oo)104 -1 o.2 075 o 4230 \6 )1
003 109 3 -1.8 0.77 0.8230 55.978
004 110 0 t.2 0.77 0.8230 57.OM
oo5 toz 1 o_2 0_68 o 4230 s1 t17
006 108 2 -0.8 0.75 0.8230 56.206
007 108 2 -0.8 0.84 0.8230 59.483
008 2 109 3 1.4 0.85 o a2ao 60 116
oo9 L07 1 2.3 0.76 0.8250 56,627 nla
010 109 1 2.3 0.76 0.8250 56.727
011 109 3 0.3 0.80 o 4250 sa.)t7
o12 10q 0.85 0.8250 60.02s
013 108 1 2.3 0.77 0.8250 54.74t
014 109 2 1.3 o.16 o.8250 55 754
o15 110 0.78 0.8250 57.551
016 110 2 1.3 0.78 0.8250 57.551
lverages 108.5 -1.E 0.5 0.77 0.8240 56.950 nla nla
G P04 3AS -0 22 7 22 - RT - L298 Page 116 of 278
High Load Run #5
L@tlon: Hur(lngton 2
t@d (Mw): 479
Date: 417412023
StartTime: 72t22
EndTimer 72t42
Probe / Gas Data
Probe fl Rm: 0 dcgrees
Probc f2 RM: 0 dcSree3
Prob€ fl Rqo: -33 deSrecr
Prob€ *2 Rsro: -1"2 dcgra€s
BE: 0.102 %/100
Md: 30.18 lb/lumole
M.: 28.87 lb/lb-mole
Pb.: 23.45 ln Hg
P,: 4.50 ln H2O
P.: 23.12 in Hg
%CO2t l2.O %
Y<a2t ____________!L%
%CO: 0.0 %
aLs %
Flow RATA Traverse Data
Polnt lD Probe lD StrckTemp
rn
Corrccted
YawAngle YawAnde P7-P2
rdrrl o ld.,l linH-nl c
Unadrusted Rlplaclmcnt Polntused #WAF
Axlal velocity Arlll Vrloclty for Polntt
V, lftlql V- lltlorl WAF? U..d
001 107 0 1.2 0.73 0.823 5S.396
oo2 109 -1 o_2 o.7a 0.8230 s7.375
003 110 -3 1.8 0.80 0.8230 5a_129
004 110 -0.8 0.82 0.8230 58.874
005 107 -1 o.7 0.59 0.8230 53.869
offi l07 0.2 o7 o a?30 ss.40s
007 t07 0 L_2 o.79 0.8230 57.62a
008 109 -2 -0.8 0.82 0.8230 5a.a22
009 107 o68 0 8150 53.593
010 108 .2 1.3 o.74 0.8250 55.957
011 108 1 2.3 0.79 0.8250 s7.7AS
01)109 )3 041 0.8250 58.553
o13 lm 33 o74 0_8250 55.928
014 110 -2 1.3 0.77 0.8250 s7.180
015 110 -2 1.3 0.80 0.82S0 sg )u
015 110 4 -0.7 0.85 0.8250 60.088
lvetaEas 108.6 -1.5 0.8 0.77 0.82t1{l 57.05S nla ola
G P04 3AS-0 22 7 22-RT - t29 I Page LL7 of 278
Probe fl Reo: 0 degrecs
Probc f2 RM: 0 deSrees
Prcbe fl Rso: -33 de8rees
Probe f2 qLo: -12 d.tre.s
B*: 0.1073 %/100
M.: 30.18 lb/lb.mol.
M.r 28.E7 lb/b-molc
Pb,: 23.45 ln Hg
Pt: 4.50 ln H2O
P,r 23.12 ln Hg
c*{o2t l2.O %
%O2t 65
',6COt 0.0 %
High Load Run #7
Lootion: Huntington 2
toad (Mw). 479
Dat€: 411412023
StartTim€: 12:59
EndTime: 13:19
Probe / Gas Data
Unadiusted Results
lVs€c
Clsw: 83,485,257 wscl/hr
Flow RATA Traverse Data
Polnt lO Prob€ lD
Coreded
St.ckTemp YawAngle YawAngle P1-P2
lFt ldccl o.. (d€rl (in H,ol
Unadrust?d Repla@m€nt Point Used * WAF
Arial vclcity Axlal velcity tor Polnts
V. (fvsl V, (fV*cl wAF? Usedc.
001 2 106 -1 8 o.67 0.823 53.00s
002 2 108 -0.8 o77 0.8230 56.945
003 110 0.2 0.75 0.8230 55 3m
004 2 110 o.2 o.79 0.8230 57.744
005 2 t07 -1 I 064 0.8230 53.446
oo5 7 109 0.2 o.7 4 o 8730 55_480
007 110 0 1.2.0.78 0.8230 57.409
008 110 0 o80 0.8230 58.140
009 106 o.73 0.E250 55.475 ala
010 107 1.3 0.81 0.8250 58.488
011 108 ot oa3 0.8250 59.272 nla
o12 110 0.82 o Srso 5a_971
013 ,1 2.3 0.71 o.82SO 54.680
014 108 03 o.78 0.8250 57.459
01s 110 3 0.3 0.80 o.a2so 58.293
110 4 .0.7 0.81 0.8250 sa 653
108,4 -1.9 0.4 0.77 0.8240 s6.888 nla ala
G P04 3AS- 0 227 22-RT - 129 I Page 118 of 278
High toad Run #8
L@tioni ]luntington 2
toad (MW): tlgo
Date: 417412023
Start Time: 13:32
End Time: 13:52
Probe / Gas Data
Probe 81 Roo: 0 degrers
Probe*2Reo: 0 det?es
Prcbe *1 &br -33 degre€s
Probe#2Rsro: -1: degre€s
Bsr 0.1081 %/100
Md: :10.18 lb/b-mole
M,: 2t.t5 tb/Emote
Pb,: 23.45 in Hg
P.: {.50 itr HrO
P,: 23.12 inHg
%COr: 12O%
ffir:-11%
9kot 0.0 %
Unadiusted Results
Iavt): 57.11 ftl:*
(lsw: 83,767,226 w:dlht
Adjusted Results
Va(avgl: 56.53 tVsec
Qsw: 82,929,554 mcr/nr
Flow RATA Traverse Data
Point lO Probe lO
Corrected
StlckTrmp YrwAryle Y.wAnlle P7-Pz
(D (d€rl o-(ded (inH"o)
Unadlustcd Repl.coment Polnt Uscd #WAF
A.l.l Vslocity Arlal Vcloclty to. Points
V.lftlre.l V.lft/secl wAF? us.dC
m1 t07 -1 0.2 0.68 0.823 53.481
o02 108 .1 0.2 o.75 0_8230 55 216 n/a
003 109 .2 -0_8 o.a5 o 4230 59.894
004 109 -2 -08 o84 0.8230 59.540
005 to7 0.2 0.73 0.8230 55.413
0m 108 0 1.2 o.74 0.8230 s5.828
007 109 -3 -1.8 0.81 0_8230 s8.444
008 110 .3 -14 o86 0.8230 60.274
009 l07 -1 0.70 0.8250 s4.350
010 109 1.3 0.75 0.8250 56_3aa
011 109 -1 3 o80 0.8250 58.205 n/a
o12 110 -2 1.3 0.82 0.8250 59.013
o13 108 -1 2.3 o.77 0.8250 54.'tA6
014 r09 4 -o.7 o.'12 o.8250 s5 259
015 110 -3 o3 07c 0.8250 57.569
016 llo 4 -0.7 0.82 0.8250 59.023
lverages 108.7 -1.9 0.3 0,77 0.82'lO 57.105 nla nla
G P04 3AS -0 2 27 22 -RT - 129 I Page 119 of 278
High Load Run llll
l@tion: Huntlruton 2
L@d (MW): 478
D.te: 4h412o23
StartTlm€: 14:07
End llm!: Ut27
Probe / Gas Data
Probcrl Re: 0 d.g.cs
Probc f2 Re: 0 d.tras
Probefl Rsrc: -33 detrccs
Probe f2 Rsro: -12 degreE
8,.. _9tu9%,ltOO
Md: ,0.18 lb/lb-mol.
M,: 2E.E7 lb/lb-mole
PbJ 23.r{i ln Hg
P.: 4.50 in H2O
P,: 23.12 in Ht
%COz, ,'2.O
"6%o.-9:L%
%CO: 0.0 %*
Flow RATA Traverse Data
Polnt lD Probe lO
Corrected
St..lTemp Yawangle YawAngle P7-P2
lFl aderl o- ld.cl lln H"ol
Unadiusted Rephcenent Polnt Used # WAF
Ari.l Velsiw Axial V€locity for Points
v- lft/s.l v- aftlscl wAF? t s.dC
001 106 3 1.8 0.65 0.823 \) )14
002 108 1 0.2 0.76 0.8230 56.587
oo3 109 1 o.2 o.79 0.8230 57.744
004 109 1.8 o.a2 o aTto s8 ao2
005 107 1 0.2 0.67 0.8230 53.084
offi 109 -1 o_7 o.76 0.8230 56.537
007 110 0 t.2 o.79 0.8230 \7 7A)
008 109 1 0.2 0.84 0.8230 59.543
oo9 107 4 .o.7 o.7 0.82SO 55.159
010 108 2 1.3 0.77 0.8250 57.082
011 109 2 1.3 0.80 0.8250 58.235
o11 110 2 1.3 0.84 0.82S0 s9.7 26
L07 1 2.3 0.70 0.8250 54.348
014 110 3 0.3 0.79 0.8250 57.935
01s 110 -7 1.3 0.80 0.8250 58.286
ot5 110 4 -o7 o83 o a?so s9 3ao
lveraces 10E.6 -1.9 0.3 0,77 0,82/O 57.034 nla nla
G P04 3AS -0 2 27 22 -RT - t298 Page L2O of 278
a
ffir Rll!l
q 7/,?t 1,/y',1
'lto,o 5o5-U
3ls,o 3zz*6
5eg. l 1yy', o
t7?4.9 I 7 trA.t
/9/, I
Unf +(rl:
IATAnlrnt Ylielt 6l-,^r n r(x):
ittrtftna:'t-,tl}Tt!!tLtlCllcct la.aal'el *',ilpflnr:ILLIY brt-T.* f..t Or..t .oo5) c.l,
5.md.
Ilcta
Irlllca tnrur
Salnpac
votrmrlftlt DGlllrmpl"4
hhr ol{tr
IthD.Gdtl
Torpf;l
Yboxltt
l'lltaHrxplt$lV - zar
ZD Ir*ktit -1 T rL-agD?aa'-a t ?
.A Ll - cr,u b <u 2,JD I :LI
'ft , ta_t (
I
Ca,t.y 6+q -bVn l,?
fnplr|Gt
hl9arfr
lmphF?
lmEhjrr
hrdoa.,
lnpft;rr
sst,
(0.01 (0.mol
(o.o;(0.000)
(0.0)(0-0,(o0)
lmelllltI
lrhFttG?
tmetl|er
lmrhlCr
55rl
a
lnatbl thr
a9pt 5?7,L
'l{q?,S 5ot.f
322.o 3e6.t
5 44.o srv fu
l*i26.1 l?866
/s?,+
tml ,itrr:
IATAf,trt|T =-n l4ial. ll^.-r Dr(!.l:
il.fifbtr:IL<q "t Frr-Tratt.kOl.ct O.oo t h
ftooltn:lu!u4 lH-T.lttmtCtrd(A, nnY)'O tt
S.lteL
Ihr.
,
llltrPrrlrrr
rlrl'Hpl
. Srmob
Vdunrfit'l
Q2-b,la2-
OG*lTrrFfFl
trht oudcr
llrrp.old.r
Trme frl
fraotrxD
rBd
lla L '4ztla <t{n CIK>. ?t5 <h I
l^a .b9,U Jrs qY
{rn ,Y-. t rl L7 AhbhflU. tl I t lr'Y At
A,'r r-v 7tJ.?nA 1 lql 2
ra (l
,tl
tlrurl H.d
/86,q 5f3.y
{76.r Stt-;t
3'(,3 32n+
S;,1!&563.o
/YJJ.?)?71.3
/62, tl
G P043AS -02 27 22 - RT - L298
(o.ol (0.01 (0.0)
Page L2L of 278
EPA teffiod 2F Datasheet
Irrnrrr PobtlFcl+drtl
Sct?amp
roFt
IlrAnd.
IrD.d
vdofrlPfHpl
lPl+21
PffirlPfHpl
lDa.Dtl Eqnnenlrr
lb -5 D, b(nla
l0 -2 o,%I
3 tofr _?6sl-
u ,oq r\,7X
7 l lo.-u ft -,H)
Z^loa -lt D,l-q
?lnK o,fl
,l,l ln*-,?h. -/n
R lnf-:-l r>-a-7
?It>)-a n^7Y
?tnQ n. !rr)
u lar -a h. </?
t4 lb 7 n- Lq
.)/lia el ritf). Jat
^<ln(n b_*h
u , t\l -.,o-7L I
Schmilc
Dlamcbr(D)=
caAa
ca Be
Pffit Dki.Fmrslad(mll
I
2-
3-
1
5-
6-
t
N
PodlD
A
B
c
D
Revleryed: FPM CPM
Pase tTol277G P043AS -02 27 22-Rr - t298
j,,i.,{. r i i r i .:,.. ii, EPA te$od 2F Datasheet
HcctGode 2ari - o?2-n2 0ornulrl:L*tJrz L-
ilrlrt ' 0.ln:l>--n lrrunrtt?ruml'Hd:
"3,/Ll<
i..
iuu: thrlrr- lr2-*dcPnranl.]lloh -u.<FlohGcnfrn V
Drb:'l /tv lz-t PrtbD/fhnnm tt? I 83 Glrl /2.c
lunl llr.f, fi',r L lltChdl'tl{tl:Z,?"DIII 6.s
lErftnr:v tooo b[nr:lo?a HPlrl
Ilrurrrr ffitFqt+oh0
ttrtllrmp
r+l
Yrllth
Itlr.d
Yrlodrf lPl'll0l
lPr+21
HdlaPrHpl
lr.Dsl EommaDtD
)I toL b. Ar rllfr
z_/o2-f't.+5
3 to+-)D,+R
L4 to7 -7 o. xD
(?)Ittl a D-?n
Z tol -z t>-?<
3 lrr?'t D, *h
Ll lo?-u n,YlItnL-,n- 4rt
2_tD+n.*5
3 t67 b- YLI
t4 lo7 h_ ?t
I)t'tbl n-4t)
\.t/L loT vl O.EL
3 la]0-gL
4 lo?-a U,
Scicerdc
DhmeE(DF
rctA=
rca B=
Fotilt rxt From siffiurt0
1_
2_
3_
4_
5_
6
t
N
Pod lD
A
B
c
D
Revlmrcd: FPM CPM-
Page 123 of 278G P043AS-0 227 22 -Rr - L298
; ,,'i | , ;rr . ' ',. ir, EPA teffiod 2F Datasheet
PuCcctGod!0ai - ozz-vtz Dprrrrlrf:rtul-TL hEillrc- 0)-'-t. *o lrmncEthsrtrrl'lIl:7s.11<Rro
lqrE:Itr'tro ,)z ilrtlc Prrrtm l'lL0l:-11.1 FrOodlthn ,/
h:tl lr.t tt,z trdrlD/tlhnmnt IrTl t37 Eorlll /t-- o
lun I t*i,h ni^ s Lerl6rclPHfl:ls.L*Dlr!4.{
DlutTInr:u ro<L hpltnl:ilr-f A lrp(r.l
IrerorrPolrttDar+dtl
$rctnunp
Itt
Yrrfih
lrDrll
vdodlillPfHrol
m.D:rt
HrlP(.Hpl
marsl Eartilclrttl
rt)I /o6 -R h.J.1 /l ,4.
L /07 A. f,<
3 /Dx -L o,*bt
L.l to?D-'rrX
lD7 b-autLtD{el o,xL
3 ox -z b,*Ll
L4 /oY D,qh
3)lh,Ih b, b?
L ba -z_D.79
3 toK -t o-ffttlleV-?o, *<
t{)I lo?-2-o. A+LJ L /oi -t o,+N
3 lo{D D-X
lt lotr O.KLT
Schcndc
Dlameter(D)=
Pom, Dhr. Fur Strckt',ln
I
[=
2
3
4
5
5Dlctanca B=
I
N
Pod lD
A
B
c
D
G P043AS-0227 22-Rr - L298
Revlerred: FPM CpMPaseaZTfzTS
. . !;i,( r i i i, i.{ iil EPA tethod 2F Datasheet
I
Ptrd€God.0{b;-u22-an-oprnbdrh lau lrL [.m
Ihnt hr)G,nrn l.lunarlcl't:nrlt'llh L3,U4 n-
tdrE:llrutrg tlL SdcPnrlrrFHOI:-Ll.<PtfiGodltbr r/
,IE:tl I tu /z-z Pru!:lDlAhnrnc ilT /t33 EIlxl 12, O
lml thi,l i^:., Ll lulotrrll']l'ol:3.'X 'qo3l 6-s
[eilfhp:'llt>tEpftnr;I l<"-&o(rl
llrucncPoht(Fc+Poht0
Stxllonp
rTt
YrrACh
lr D.d
UddrlPfHpl
l?a'ill
rurt,fHrol
tx.Psl EamrrEl
lt)I lol n- lo<NA
7_ln{-)_h.2L I
3 tDg o o+t-
Ll t0q o o.Yo
')_lh*-Ll f\.2r.l
?-l6a *c A.?q
3 lo'q _?^-3hALlt);-l o-8tl
4 I to7 h /), /ol
?_loK -l n.a<
log -?D.7h
q Lr)-?O,flLl
h I t6r -)D.ky
Y 2-loO -l n,%
3 tt/D,v5
u It\Q -l D-%t I
EclrurtE
Dlarcbr(D)=
ml U!t. Frmt 6trd(Uhl
1
AF
B=
2
3
4
5
5
t
N
FdtlD
A
B
c
D
Revlryed: FPM_CPM_
Page L25 ot 278GP043AS-0227 22-Rr -L298
rroLctCodc ia.,- rYa1?a Mcl:lna lrc-[.6
dhrt '/or^A.o.n lrunrftFrurl'|il:
"3{u 6 t
loum Nrwa tAL SrdcFtrrml'lt€l:- tl,S trlhq5tlht V
h:4 ltu lz<PrutclD/ftunant tt?4rc? Blxl 12, o
tunl l1*'/r^,--1 lgl6rctl'll0l:?.i,"L(rI 6.1
ilrfiImr;u iltt?lbDllttr:t"t7 ltolll
l?rnrrPolrtlPon+&0
$rclTclnl
t"Fl
Y.ull;L
Irtrlil
vdodtrlPfHrol
TPl.P2I
Ht.PfHpl
lDa+!$Canrililr:
tr)lr>7 -2 O,[aP NA
1 loY D.?-<
3 loQ 0,HLqatlDo^-r+,J I to+:l h, (oQ.
,L toK *?o,z7
toK -,h.9tt)
Lf lo4 -?^*L,o t^a *l D.AA
2-lo.D.+1,
lot -?D.'r()
Ll t|J.q -/_0,85
lui to*^.?lV7_tD1 -L D-Al
?, tr,.L o-+{
U Itn -L D-+f,
SG|rcrdc
DlametarlO;=
peA=
ce B=
Pomt unt FmmSacitrJlil
1-
2-
3-
c-
5-
5-
E!ilQ
A
B
c
D
G P04 3AS -0 22 7 22-RT - L298
Revierved: FPM CPI
EPA tethod 2F Datasheet
trolGct CodG D; .rttz*tt-Dcgrtsdrl:Cna /7.-L-
dhnt | 0i.;{.-iuunclrtPruanrFHd:23.vs L^
lqm::l*Wft- tt ?ilrtPnrarcFllfl:-y. <hoDeCandf,on t/
DrUt:Ll I tu )23 trutclD/^hrncrtt tt*/t?<elxl /z.o
Irnl tl,ii n L L hrtdtedl'tl€l:itr. It LfiI b.5
EilTlrr:)L22_fboftncE rq tlZ-[plll
IrrYarrePdrtlPorlPftl
$rclllnq
ltl
Yerl4h
ItDrd
vdodryrPfHf|
tPr+21
mr!rfHpl
tna,Pil bmmutn
fi ba-c)o,T<nn
?-I DCI el o,7x I
3 aI,\-(n. tro
u llrr -L (), Y2-/)t0+D, L1LtbTn-a?
3 to+r>n .74
L,ta,Q o.t,
tq I ,h-_a o- LX
7_to8 -4,b-7rl
3 tbg O,7
v,toq o,?( I
tJ t lol t\oyl
L Ito '2-o,T)i
?llx -a D.YD
lr{ll^-Lt D*S
Ectrqlrtts
DlamcbrlO;=
ffil UH.Frwa&rotWLI
1
fi=
l=
2
3
4
5
6
t
N
PilI ID
A
B
c
D
Revlwed: FPM CPM_
Page L27 of 278G P04 3AS -0 227 22 -RT - L298
tulraGodr fitd-azzHtL hrrrulrl:f*t / ze [.6
ilrnt '!.r)&,^.o trmmrtrlcRrru:l'lll:2_<.4t<nrn
lame:llrtfru t^z-MsfiunrnFtl0l:- tl,5 [oboCandldon t/
ffi:u I rq l2-?PrdclD/Alhtnm t,7 /,\3 Eqfil 12_ o
Nonl a;L ct^,s ?lrtOtr*l,H0h /1,/ 1 rt qfil 6.{
ilrilftm:J rLSq lUnftns:t"iq rp0.l
lrrurrPotrtlPatffil
$rdTrmp
fFl
Ylsltgh
lr o.il
VdoCf,rlPfHpl
mf2l
mrlPfHpl
lPa"D!il iommomr:
tt I lo{,-3 D.b+NI
z /oK .?o.E I
3 ltD -l 6. +5
vl llh -t D.>q
0)to-+-?D-lo'X
2-log -t o.+q
3 lto o D.+*
4 ltzl.h D.*^
I lnL D,7<
L tba -7_h-3,
3 loE -l D r7?
Y ,16 -l h,.p-
Ltt t I n'1"o,+l
{L lo7 o,7K
3 ltt\-t o.ko
u nh -Lt n,xl I
Echudc
DiemeEr(DF
Polnta DL[. FIom Slrctltll
I
[=
B=
2
3
4
5
5
t
N
Po.t lD
A
B
c
D
Revlewed: FPM_CPM.
G P04 3AS -0 22 7 22 - RT - L298 Page 128 of 278
lrdrdGodr 0n1-otz-?zz-Drrmftl:lfid ltc nlr'
TLilU 0^.'rt+r^.^lrunrtlc Pnarr l'llrl:z{, ul S Nr.
lolllra:tiutv iL ffiFlcnml'll'Ol:- a.<FruhGcnfidon t/
D.!tB Ll lrqlz\DulelD/fhnrrnG tr}l t\3 EO"tn t?,o
htrrl H:"t l^,^ (lrlotrtll'll0l:/ U.z"Dlr!6-s
ilrilrlnn:'133>*oofinr:, t(z-ltoHt
EPA iiethod 2F Datasheet
I 'i,1 il
Rolewed: FPM-CPtrt
Page 129 of 278
IleYrrnPolnt(mFohtl
StrclTrOf
rn
YluladC
liod
hbdulPrHpl
Dr.r,il
Hdr aP fHPl
lDa.Pst EomnrnB;
lt I tA*h. l,,Z ltlA
?-to{D,7<
3 lDq -?-o-7.s
Ll loot *?n.Xtlwln?D-+1
L lo(o o.a.l
3 laq -t o.7ttlilll-R h,7t
H,I ,o+h-an
L taQ h,+<
3 lo'o.xo
Ll ilD b,gL
J lnI -l o.
Y L loi -Lt D,Y
llri )I /).+I
"l ilo -Ll D-8L
Schrlrdc
Oarncbr(D)=
EghLl DtsL Fmmstd(Wdl
1
.{=
t:
2
3
4
5
6
t
N
PdTlD
A
B
c
D
G P04 3AS - 0 227 22-RT - t298
,, .: r:,'j'( ' i r i i. ,i.. 'i: EPA tethod 2F Datagheet
I j r |r. | ,
lrd!.tGodc Drfo\ - o"Llb?Drnbdrl:lA't /rr,f-
illcnc f)^,-J{,oc^trunrttPnrnrFlll:23,"1<R-.
lqru:I IttilT(r tt z HcPuanl']lfl:-y-s Prd:Gandltbt t/
lrts:.l lrt lzr:PrdrD/Allrnstt t*lt\\cqEl t2.o
lunl ll'-h O^,.t I lrdChedl'll0l:l4o "ql$c.{
Lrtltrc:r t utnT lbftnc:tu,l27 Hpfil
InurnrDolttlm+oh*l
S[r:tTrlm
l"n
Yrwrnh
lrDrd
lrrlsctrarfHrol
IEr{2I
HdrlPfHpl
1s+3t Eomnrrnl*
tr I lob -?D- /q4,ila
L IDJ(-l n-+L I
tDq _,b.+4
L{lrrl -7 h-{L
t)I loZ ,l 6,AZ
7^lDq -l D.7A
3 Jltb D o-ry|
t4 t^q -l 6,RLI
?)I lbJ--L'h.72-/7-tx(1 b-+l-
I tbq -2 t *r)
u lln - t_-b,*Ll
tl\t to+-t o.44
{?-ilh D-+a
3 t,r)-?b.70
u ,rb -Ll 0,1\I
tchamatc
IIamebr(D)=
Potrill Dm. Fom grcf VtEil
I
fi=
BE
2
3
4
5
6
t
N
PdtlO
A
B
c
D
Revlewed: FPM_CPM_
Page 130 of 278G P04 3AS - 0 22 7 22-RT - L298
Appendix A.3.2.3
Instrumental Test Method Data
G P043AS -02 27 22-RT - L298 Page 131 of 278
PROt422722
PacmCoIp
Huntington Unit 2
4lul2o2.
EPA Method 2 Data
Run, 1
StartTlme 9:08
StopTlm. 9:45
2
10:00
10:20
2
3
10:36
10:56
3
4
71172
71132
4
5
11:!l8
12:08
5
#rt,S\iN t,tH)!
6
!2122
12t42
6
7
12:59
13:19
7
8
13i32
13:52
8
9
14t07
14t27
9
Q Exhaust Flow (wscfh)82,s99,010 83,768,267 84,600,445 82,204,459 82,736,208 82,874,743 82,650,405 A2,929,s54 82,83s,307
sO, (ppmw)
No, (ppmw)
NO, (ppmw)
CO (ppmw)
Mass Emlsslor Celculatlons (Uslng EPA Method 191
37.0
L72.7
0.0
59.9
I
31.1
L72.3
0.0
34.3
2
28.8
114.5
0.0
38.3
3
24.4
104.1
0.0
114.9
4
23.3
105.1
0.0
183.9
5
27.2
105.9
0.0
145.6
6
22.4
109.1
0.0
234.7
7
27.3
LlL,2
0.0
155.8
8
B.a
110.1
0.0
191.5
9
Fc scf/mmBtu
SO, (lb/mmBtu)
NO, (lb/mmBtu)
CO (lb/mmBtu)
SO, (lb/hr)
No, (lb/hr)
co (lb/hr)
507.6 433.4 404.7 339.0
1106.0 7123.3 1158.1 7022.2
359.8 209.1 235.7 686.7
37.8 31.8 29.5
s16.3 433.6 402.7
1800
0.107
o.232
0.075
0.090
0.234
0.044
0.083
0.236
0.048
0.070
0.210
0.141
0.056
0.215
o.228
0.050
0.218
o.181
0.065
0.223
o.292
0.061
0.224
0.194
0.058
0.227
o.241
320.8 292.4 312.9 294.0 327.6
1048.0 1057.9 1076.7 1101.3 1089.2
1106.2 A77.7 1470.2 939.5 1153.4
PlantCEMSData I 2 3 4 5 6 7 8 9
Unit Load (MW) 481 480 483 486 4A4 479 479 480 478
10.6 10.5 10.6 11.0 10.9 10.8 10.8cor(%w)
SO, (ppmw)
50, (lb/hr)
5o, (lblmmBtu)
NO, (ppmw)
No, (lb/hr)
NO, (lblmmBtu)
co (ppmvw)
co (rb/hd
co (lb/mmBtu)
GPo 43 AS -0227 22-RT- 1298
23.5 22.7 24.4
0.107
115.2
0.090 0.083 0.069 0.066 0.060 0.065 0.062 0.058
1133.3 L747.6 1154.4 1031.8 1059.8 7072.7 1091.7 7727.0 1113.3
0.235 0.239
50.0 29.0
0.238 0.272 0.218 0.222 0.227 0.233 0.231
183.1 140.4 229.9 150.4 184.9
25.2 24.0 27.8
334.9 320.4 290.5
to.7 10.7
294.2 328.3
116.3 115.1
0.226
Page 132 of 278
313.s
113.8t 16.9
173.6
34.1
707.9
111.8
110.2
0.220
299.3 203.9 650.2 7077.6 827.7 1341.0 886.1 1088.4
0.052 0.036 0.042 0.133 0.170 0.279 0.184
PROt-O22722
PaclfiCorp
Huntingon Unit 2
41t412023
rrc CFR Part 75, Appendix A
56.5.6 Pollutant Stratification Test
Port Point
stack D ia m ete r : l.523 J-;'l
Stratification Test Point 1: 14.2"
Stratification Test Point 2: 47.2"
Stratification Test Point 3: 95.5 "
Time CO,NO,
I
1
1
1
1
1
2
2
2
2
2
2
3
3
3
3
3
3
4
4
4
4
4
4
t 4h4/2o239:O8
1 9:09
2 9:10
2 9:LL
3 9:12
3 9:13
t 4/L4/2O239:t9
t 9:20
2 9:21
2 9:22
3 9:23
3 9:24
t 4/L4/20239:30
I 9:31
2 9:32
2 9:33
3 9:34
3 9:35
t 4/L4/2o239:4t
L 9:42
2 9:43
2 9:44
3 9:45
3 9:46
10.3 111.8
L0.2 114.5
L0.2 LL2.6
10.4 108.8
10.4 L09.7
10.3 Lt4.6
10.5 Lr4.2
10.5 116.0
10.5 LL7.7
10.5 115.8
10.6 113.9
10.6 115.3
to.7 111.s
LO.7 LLL,4
t0.7 tL2.9
10.8 tL2.4
10.8 113.3
LO.7 113.6
10.6 116.1
10.6 113.5
t0.7 115.1
10.6 115.8
10.7 Lt6.7
t0.7 LL7.4
Mean
Max Deviatlon From Mean
Max Deviation (%)
Short Line?
Single Point?
10.6 113.9
0.3 s.l
3.L% 4.5%
ot( oK
OK OK
G P04 3AS -02 27 22 -RT - 1298 Page 133 of 278
PROt4227,j2
P.clficorp
Hurtlngton unh 2
4lt4l2023
TCrt Run *1
StartTime
Run Lentth
StopTime
Uncorreded Analyzer oab
9r08
24
9:46
PROt422r22
Paclicorp
Huntlnlton Unh 2
41t412023
Teit Rur f2
Stan Time
Run Length
Stop Time
Uncorreded Analyzer oata
10:00
7L
10:20
Mlnut.
1
2
3
4
5
6
7
E
9
1o
11
72
13
74
15
76
17
1E
t9
20
27
22
23
24
Tlm.
9:08
9r09
9:10
9r11
9i12
9:13
9:19
9tzo
9i2l
9i22
9:23
9:24
9:30
9:31
9:32
9:33
9134
9:35
9141
9i42
9:43
9..44
9:45
9:46
@r sor No, CO No,
Xuw ppmw ppmw ppmw ppltw
10.3 38.6 111.8 38.0 0.0
10.2 37.0 114.s 33.3 0.0
10.3 38.5 LL2.6 47.L 0.0
10.4 40.3 108.8 s2.8 -0.1
10.4 4L.6 109.7 49.8 0.0
10.3 40.3 114.6 M.t -0.1
10.6 38.1 LL4.2 55.9 0.0
10.5 37.3 116.0 65.5 -0.1
10.4 36.9 1L7.7 62.A -0.1
10.5 37.7 115.8 66.7 0.1
10.5 37.2 113.9 50.3 0.0
10.6 37.3 115.3 67.4 0.0
LO.7 37.7 111.5 70.4 -0.1
LO.1 37.5 711,4 55.3 0,1
to.1 37.3 112.9 63.1 -0.1
10.8 36.6 Lt2.4 68.9 0.1
10.8 37.6 113.3 94.8 0.0
LO.1 37.t 113.6 64.7 -0.1
10.6 34.4 116.1 52.8 0.1
to.1 34.3 113.5 66.8 0.0
10.6 34.3 115.1 55.1 -0.1
10.7 34.1 115.8 63.s
70.7 34.8 7L6.7 72.3
10.7 34.0 717.4 65.5
cor sQ No, co Nor
*truv ppmw ppmw ppmw ppmw
10.7 35.5 116.0 24.4 0.0
10.6 33.4 118.4 18.5 0.0
10.8 32.5 114.3 24,6 0.0
LO.l 32.2 113.9 36.6 0,0
10.6 29.5 L17.6 20.5 -0.1
10.6 29.2 116.8 i!0.9 0.0
10.6 31.6 116.5 27.6 0.0
10.5 37.4 115.6 31.8 0,0
10.6 30.4 116.3 22.7 0.0
10.6 29.r 117.0 '16.8 0.0
10.8 29.6 113.0 38.9 0.0
10.6 29.5 LL7.5 30.4 {.1
10.s 3L.4 L77.7 24.1 0.0
LO.1 31.9 rt5.4 34.a O.2
10.7 32.9 114-5 45.3 0.0
10.6 37.7 116.5 39.8 0.0
10.6 42.4 177.0 4t.1 0.0
10.8 32.9 L14.2 55.1 0.1
LO.1 32.3 115.6 53.2 0.0
10.7 32.9 117.0 29.s 0.1
10,7 32.9 118.0 29.8 0.0
10
11
72
13
14
15
16
t7
18
L9
zo
21
Tlme
10:0O
10:01
10:02
10:03
1O:04
10:05
10:06
10r07
10:08
10;09
10:10
10:11
10:12
10:13
10:14
10r15
10:16
10r17
10:18
10:19
10:20
0.0
0.0
0,1
AEng€
Co p.
10.7 at,? 116.1 92.' 0.0
0.1 0.1 -0.3 -3.3
0.1 0.1 -0.2 -3.7
0.1 0.1 .{r,3 -3.5
9.3 27.2 1s9.1 1s5.4
9.2 26.4 159.1 1SS.7
9,3 27.O 159.1 155.6
8.9 26.5 153.8 150.9ffi
Awrata
q
q
c..
Corect.d ArcEle:
10.6 97,1 11t.9 59.4 0.0
0.1 0.0 -0.3 -1.6
0.1 0.1 -0.3 -3,3
0.1 0.1 {r.3 -2.5
8.9 26.0 L53.7 151.4
9.3 27.2 159,1 155.4
9.1 25.6 156.4 153.4
8.9 26.5 1s3.8 150.9ffi
q
q
c,.
crrcctld Avangc
G P043AS -02 27 22-Rr - L29 I Page 134 of 278
PRat422122
Pa.t icorp
Hundntton Unlt 2
4lt4l202a
f$t Run fl
Stafr Time
Run Lengh
stop Time
Uncorreded
10:36
2L
10:56
Dab Uncofteded
11:12
2t
11:32
0ata
PR()Jl!22722
P.cmCorp
HuntinSlon unh 2
4h4l202i
Tert Run 14
Startlime
Run Length
StopTime
Mhutc
1
3
4
5
5
7
8
9
10
11
t2
13
L4
15
16
18
19
20
2t
Tlre
10:36
10:37
10:38
10:39
10r4O
10:41
lOi4Z
10:43
LO"44
10:45
10:46
10147
10:rl8
10:49
10:50
10:51
10:52
10:53
10:54
10:55
10:56
Mlnute
1
2
3
4
5
6
7
8
I
10
11
!2
13
74
15
16
71
18
19
20
21
Timc
lLtl2
11r13
11:14
11115
11:16
11117
11:18
11:19
Ur20
l|2L
lt22
lLt23
lli24
LLt2S
11:26
L1t27
U.:28
11:29
11:30
11r31
11:32
co, sor No, co f,or
vt PPmw ppmw ppmw pPmw
to.7 28.5 122.5 67.3 0.0
to.7 28.0 727.7 35.7 0.0
10.8 30.7 118.3 34.0 0.0
10.8 29.8 118.0 31.6 0.0
10.8 27.7 722.0 25.3 -0.1
10.8 27-3 723.0 35.8 -0.1
10.8 27.3 !24.2 44.4 0.0
10.8 27.1 !27.3 49.3 0.0
LO.l 30.5 120.s 49.5 0.0
10.7 30.2 122.0 38.0 -0.1
L0.7 30.3 119.5 42.3 0.0
t0.7 30.2 116.9 37.6 -0.1
10.8 30.3 113.9 44.7 -0.1
10.7 30.3 115.3 36,0 -0.1
10.8 29,6 113.5 30.5 0.1
10.8 29.4 111.9 27.4 0.0
10.9 30.5 110.4 33.4 0.0
10.8 29.5 110.4 19.9 -0.1
10.8 24.? 108.9 23.1 0.0
10.9 29.4 108.0 31.0 -O.1
11.0 3d.0 to7.a 38.6 0.0
cor sor Nor co Nor
,6w ppmw ppltw ppmw ppmw
11.2 29.7 LO1.2 773.5 0.0
11.1 27.9 103.1 1s9.9 0.0
11.0 26.7 104.3 101,4 0.1
11.2 26.7 103.6 130.6 -0.2
11.1 26.5 1(N.1 737.7 0.0
11.0 25.4 104,9 130.9 0.0
11.1 25.4 LO4.2 732.4 0.0
L7.2 25.3 103.3 138.4 0.0
11.1 2s.2 10s.0 118.8 0.0
LL.L 25.L 106.8 63.8 -0.2
L!.2 25.4 105.5 83.9 0.0
11.1 2S.L LO7.7 47.5 0.0
11.1 25,7 108.3 56.0 0.0
11.0 24.6 108.5 U.2 -0.1
11.3 25.0 106.0 166.5 0.0
11.3 24.4 107.6 137.2 0.0
11.1 23.8 109.1 133.2 0.0
LL.2 24.6 108.0 124.4 0.1
11.1 23.7 109.5 107.2 0.1
11.1 23.0 108.8 87.O 0.1
tt.2 22.3 108.0 89.6 0.1
AEn!.
q
q
c..
conactld AEntt:
10,t 29.3 116.6 '7.0 0.0
0.1 0.1 -0.2 -3.7
0.1 -0.1 -0.2 -2.L
0.1 0.0 4.2 .2.9
9.2 26.8 159.1 155.7
9.3 27.2 154.0 152.5
9.3 2r.O 156.6 154.1
8.9 76.5 1s3.8 150.9ffi
AYaEtc
q
c. ".
c-
c..
Con.ctcd Avcntc:
0.1 -0.1 -0.2 -2.L
0.1 0.1 -0.3 -1.9
0.1 0.0 {r.3 -2.0
9.3 27.2 1s4.0 152.5
9.4 26.8 L59.7 L54.3
t.il zt.O 156.9 153.4
8.9 26.s 1s3.8 150.9@
G P043AS-02 27 22-RT - t298 Page 135 of 278
PROt422722
PaclfiCo.p
HuillnGon Untt 2
4lt4l2oi1?
T.st Run fs
Start Time
Run Length
Stop Tlme
11:48
2L
12i08
Data
PROJ.022r22
Prcmcorp
Huntl]l3ton unlt 2
4lt4l2023
Tllt Run 16
Start'lifre
Run LenEth
Stop Tlme
12122
2L
t2142
lJhcorreded Uncorrected Analyzer Oata
Mlndr
1
2
3
4
5
6
7
8
9
10
11
12
13
L4
15
L6
t7
18
19
20
2L
Tinc
11i48
11r49
11r50
11:sl
11:52
11:53
11:54
11:55
11:56
11:57
11:5E
11:59
12:00
12:01
12ioz
12:03
12:04
12:05
12:06
12107
12:08
@r !i{rr Nq CO ilo,
Xw ppmw ppmw ppmw ppmw
r1.2 26.2 111.1 280.8 0.0
11.1 25.3 111.8 267.5 -0.1
11.0 24.4 L74.L 767.9 0.1
11.0 23.9 111.8 1ss.0 {.1
11.1 24.1 110.9 177.4 0.1
11.1 23.E 111.0 161.5 -0.1
1L.2 23.9 110.3 252.4 0.0
11.1 24.2 111.3 237.L 0.0
11.1 24.1 110.2 184.0 0.1
11.0 24.L 111.3 148.8 0.0
10.9 23.2 7L2.7 97.3 0.0
11.1 23.8 109,3 191.4 0.0
11.1 23.8 111.0 240.0 -0.1
11.0 23.3 111.3 72!.7 -0.1
11.1 23.2 7L7.2 209.0 0.0
11.0 23.5 111.5 20L.2 -0.1
10.9 22.4 111.9 L3r.2 0.0
11.0 22.7 110.5 142.1 -0.1
11.0 23.0 110.3 L77.5 {.1
11.0 23.2 110.8 L62.6 -0.1
10.9 22.A 7t1.7 t47.3 0.0
co, so, a{o, co Nor
Tlm. ,{ ppmw ppliw pplrw ppmw
12:22 11.0 25,0 111.5 L73.5 0.0
12123 10.9 24,4 113.1 158.7 0.1
L2t24 11.0 23.6 tlz.A 156.0 0.0
L2125 11.0 23.'1 LL2.2 131.5 0.0
12126 10.9 2X.0 113.0 135.3 0.1
12t27 10.9 23.6 111.7 158.5 0.0
12t28 10.9 23.2 112.0 163.6 0.0
12t29 11.0 23.3 111.5 787.5 -0.1
12f30 11.0 22.4 112.9 198.0 -0.1
12t37 10.9 27.6 113.1 742.4 -0.1
!2t31 10.9 21.8 111.9 164.s 0.0
12:33 10.9 20.7 L17.4 151,2 -0.1
12:34 11.0 20.1 111.3 194.9 0.0
12135 11.0. L9.4 Ltt.1 159.3 0.0
12:36 10,9 18.6 713.7 747.2 0.0
12..37 10.9 18.9 7L4.4 135.3 0.0
12:3E 11,0 2O,7 120.1 122.9 0.1
72.39 11.1 20.6 722.3 4A.4 {.1
12t4O 11.0 2O.3 7L4.6 131.5 0.1
l2t4L 11.0 20.1 115.8 L36,2 0.0
9.3 26.9 764.2 152.E
9.3 27.7 163.7 153.4
8.9 26.5 153.8 150.9ffi
10
11
L2
13
74
1S
16
77
19
20
Arent
q
c.,.
q
c..
Correctcd Arcra8a:
11.0 23.8 1t7.2 ttt.4 0.0
0.1 0.1 -0.3 -1.9
0.1 0.0 -o.2 -3.3
0.1 0.1 -0.3 .2.6
9.4 26.a L59.7 L54.1
9.3 27.2 163.1 153.9
9.4 27.O 161.4 154.1
8.9 26.5 153.8 1s0.9ffi
2! L2142 11.0 79.4 115.5 97.5 0.0
Avcntl 11.0 2r.6 113., 147,A 0.0
c.re 0.1 0.0 -0.2 -3.3
Qo 0.1 -0.1 -0.2 -2.6
q 0.1 .o.t 4.2 -3.0
c.r. 9.3 27.2 153.1 1s3.9
c.
Cr"
Corrccted Av.r.i.l
GP043AS-0227 22-Rr - 1298 Page 136 of 278
?rc!ot2?x2
PecffCorp
Hunth6on Unh 2
4lt4l2o23
Ted Run f7
StartTlme
Run Length
StopTime
12:59
21
13:19
PROJO22,22
Pacif,corp
Hundntto Unh 2
4174l20z3
Tett Rur rB
StartTime
Run Length
Stop Time
L3t32
2L
13:52
Uncomcted Analyrer Data Uncorreded Analvzer Data
cor sor ilo, co Nor
Tlm€ l$uv ppmw ppllw ppmw ppmw
12:59 10.8 24.4 118.6 150.4 0.0
13:00 7O.7 24.O 117.0 246.9 0.0
13:01 10.7 23.4 L17.4 277.5 0.1
13:02 11.0 23.5 116.6 2L1.3 0.0
13:03 11.0 23.9 177.2 205.8 -0.1
13:04 10.9 23.4 119.0 130.5 0.0
13:05 11.0 22.1 118.4 178.8 -0.1
13:06 11.0 22.8 LL7.6 197.3 0.0
13:07 11.0 27.7 116.5 302.8 0.0
13:08 11.0 23.2 1L7.0 311.2 0.0
1309 10.9 24.2 118.3 433.7 0.1
13:10 10.E 23.4 116.8 239.4 0.0
13:U. 10.9 23.5 113.9 363.s 0.0
13:12 10.9 23.5 115.0 325.4 0.1
13:13 10.8 27.6 115.7 188.7 0.0
L3174 10.8 22.2 115.0 19E.0 {.1
13:15 10.9 22.A 173.7 250.3 0.0
13:16 10.8 22.4 177.7 267.2 0.0
!3tt7 10.9 22.A 118.4 151.4 0.0
13:18 10.8 23.0 116.8 216.7 4.1
0.1 -0.1 4.2 -2.6
0.1 {.2 {.3 -2.2
0.1 .o.2 {r.3 -2.4
9.3 26.9 L64.2 152.8
9,2 27.2 165.5 153.8
9,3 27.1 16,t.9 153.3
8.9 26.s 1s3,8 150.9ffi
cor 3o: t{o, co No,
taw ppllw ppltw ppmw ppmw
10.E 23.7 119.8 199.3 0.1
10.8 2!.L 123.0 85.9 0.1
t7.2 2t.5 119.3 214.8 4.2
11.0 21.2 120.9 151.5 {.1
10.9 21.9 722.6 t77.2 0.0
10.9 27.s L2L.4 122.L 0.0
11.0 21.0 Lr9.7 151.0 -O.1
11.0 20.2 t77.6 773.L 0.0
10.8 20.s 118,7 161.6 0.0
10.9 20.4 LL9.7 151.9 0.0
10.8 22.7 1L7.2 188.5 0.1
to.7 22.5 119.5 t35.7 0.1
10.8 22.2 118.0 162.s 0.0
10,8 22.6 7L9.7 L42.6 0.0
10.8 22.7 120.2 165.6 0.0
L0.7 22.3 120.5 L73.4 0.0
10.E 22.4 119.5 1,10.9 {.1
10.9 22,9 L!7.7 199.8 {.1
10.8 27.A 119.5 162.5 0.0
10.8 21.S t20.7 139.2 0.1
11.0 zL.A 179.2 774.0 -0.121 13:19 10.8 22.9 1L7.4 186.1 0.0
AwEt 10.9 29.2 116.9 239.8 0.0
10
11
t2
13
14
Mlnn.
L
2
3
4
5
5
7
8
9
1o
11
L2
13
14
15
76
77
18
19
20
)7
Tire
13:32
13r33
13:34
13:35
13:36
L3137
13:38
13r39
13r40
13:41
7!42
13:43
13r44
13r45
13r46
13147
13:48
13:49
13:50
13r51
13:52
15
16
l7
18
L9
20
Qr
q
Q,o.
q
q-
Cold.d ArentE:
Awn!.
qp,.
q
c,
c*
Corrlctcd Av!at!:
10.9 21.8 119,7 157.t 0.0
0.1 {.2 -0.3 -2.2
0-1 0.0 -o.3 {.5
0.1 .o.r {r.3 -3.4
9.2 27.2 165.s 153.8
9.3 27.1 155.9 151.5
9.3 27.2 !65.' 132.7
8.9 26.5 1s3.8 150.9@
G P04 3AS -0 227 22 -RT - L298 Page L37 of 278
Ptut42272:2
PaclfiCorp
Hun$ntton Unlt 2
4l14lmi,3
T6t Run 19
Stan Time
Run Lergth
Stop llne
Uhcoreded AnalEer Dah
cor s{rr l{q co Nor
TlmG *us ppmw plmw ppmni ppm
14tO7 7O.7 26.3 120.3 151.4 0.1
14:08 70.7 25.2 120.8 158.1 {.1
14:G, 7O.7 2/r.0 U1,5 L1O.2 0,0
14:10 10.8 24.6 120.6 140.5 0.0
14iu 10.8 U8 120.0 158.5 0.0
14112 10.8 24.7 119.0 179.0 0.1
14:13 10.7 2t.7 119.7 155.4 O.O
14:14 10.8 23.7 119.3 155.9 0.0
14:15 7O.7 23.7 119.5 754.2 0.0
10 14t76 lO.7 23.2 120.5 ,45.2 0.0
11 14177 LO.V 22.9 119.5 2?3-6 {.1
12 14:18 10.8 23.6 118.1 178.1 0.0
13 14:19 10.9 25.0 116.6 221.2 0.0
1.4 L412O 10.8 24,1 1173 2L5.7 -0.1
15 14:21 LO.z 24.O 118.1 277.6 0.0
L5 L4t22 10.8 24.5 116.5 292.4 0.0
L7 ,.4t23 10.7 24.2 118.0 258.6 0.0
18 74124 10.8 24.5 11E.6 235.8 0.0
19 14:25 10.8 24.5 119.3 252.7 0.1
20 14:26 10.8 24.? 119.5 233'.0 O.O
27 ,.4127 10.8 24.6 719.7 232.9 0.1
Arcr.a3 lo.E A.a 119.2 1!14.1 0.0
Qn 0.1 0.0 {.3 {.5
c.m 0.1 -0.1 -0.2 -3.0
q 0.r .o.1 .0.3 -3,
c.o" 9.3 27.1 155,9 151.5
L4tO7
2!
!t7,
q
c*
Corroctad Awragrl
9.2 27.1 L57.2 153.8
9.3 2t,L 166.5 152.1
8.9 26.5 153.8 150.9ffi
GP043AS-022722-RT -L298 Page 138 of 278
Appendix A.4
Example Calculations
G P04 3AS-0 227 22 -RT - 1298 Page 139 of 278
PaclflCorp
Huntington I
4lL3l2O2'
Run S1 Sample Calculations
CPA Method 4: Determination of Molsture Concentration in Stack Gases
(40 CFR Part 610, Appendix A-31
P.= Pb,+(AH/13.5)
= 23.38 + (1.8/13.5)
= 23.51 in. Ht
Tn=460+t.
=460+66
=S25R
V*ddl= KlxVk
= 0.04705 x 21s.4
= 10.14 scf (Eq. 4-1)
Vht.d)= KaxYxvmxPm
Tm
= 77.64x0.9783x 99.648 x 23.51
526
= 76.87 dscf
8s= Vxktd)
(Es.4-3)
LO.t4 + 76.87
= o.Lt7l96ltool Gq. aa)
B*,**-r, = 1o(n'lt/(t*c)))
Pstarsl
= tO {3.i0765 '(17501!5/(.r.2 r 2:5.0n)
585.38
55.3S
varlable Value )eflnltlon Unit of Measurement
Plil 23.38 Iarometric Pressure in. Hc
AH 1.8 ,ressure Differential across Orifice in. H20
P-23.51 qbsolute Pressure at Gas Meter in.Hg
tm 66 emperature at Gas Meter .F
Tm s26 \bsolute Temperature at Gas Meter .R
K1 0.04706 :onve6ion Factor ft'/mL
215.4 : of Water Condensed E
10.14 /olume of Water Condensed scf
K,17.64 :onstant "R/in.Hg
0.9783 vleter Calibration Factor Unitless
99.648 /olume of Stack Gas Collected dcf
75-a7 iample Gas Volume dsct
B*.o.tLl ;tack Gas Moisture Content %/700
110 itack Temperature
43.2 ;tack Temperature 'c
P -4.50 itack Static Pressure in. HrO
Pst:lst 23.05 \bsolute Stack Pressure in. Hg
Plab)s8s.38 \bsolute Stack Pressure mm Hg
A 8.10755 :onstant mm Hs
B 1750.286 :onstant mm HE
c 235 :onstant "c
B*skarrratcal o.Lr2 ;aturated Stack Gas Moisture Content %/LOO
G P04 3AS -02 27 22-Rr - 129 I
= o.tt2l%lfiol
Page 140 of 278
Cllent
Source
Date
Run I
PacifiCorp
Huntington I
4lLil2ozt
1 @ Hish Load
Variable Value )eflnition Unit of Measurement
%co2 t2 :oncentration of Carbon Dioxide Dry Volume Percent (Yovd)
%o,7.5 oncentration of Oxvsen Dry Volume Percent (Yovd)
Md 30.22 )ry Molecular Weight ofthe Stack Gas lbllb-mole
B*.0.112 ;tack Gas Moisture Content %H|O / 7OO
28.86 \dual Molecular Weight of the Stack Gas lbllb-mole
Pu",23.38 : Pressure in. Hg
P"4.50 itack Static Pressure in. H20
Ps 23.05 \bsolute Stack Pressure in. Hg
te 105 ;tack Temperature at Traverse Point i
.F
T 566 \bsolute Stack Temperature at Traverse Point i "R
K.85.49 lonversion Factor (ft/sec) x v(((lb/lb-moleXin.Hs))/(('R)(in.H,o)))
APr 0.56 )ifferential Pressure of Stack Gas at Traverse Point i in. H2o
cp 0.824 ,itot Tube Calibration Coefficient Dimensionless
€v(il -7 vleasured Yaw Angle of Flow Velocity at Traverse Point i degrees
Rsro 7.2 lotational scribe Line offset of Probe degrees
6v{i)0.2 :orrected Yaw Angle at Traverse Point i degrees
52.793 itack Gas Axial Velocity at Traverse Point i ft/sec
55.0s9 Verage Stack Gas Axial Velocity Across All Traverse Points ft/sec
A 570.084 :ross-Sectional Area ofthe Stack ft'
Toa 528 ;tandard Absolute Temperature
109.7 Werage Stack Temperature Across All Traverse Points
.F
569.7 Werage Absolute Stack Temperature Across All Traverse Points
Psu 29.92 itandard Absolute Pressure in. Hg
WAT 0.99 /y'all Effects Factor from EPA Method 2H (1.0 if not used)Dimensionless
o.*79,47L,339 Nerage Wet-Basis Volumetric stack Flow Rate Corrected to standard conditions wscf/hr
q"70,9s4,212 \verage Dry-Basis Volumetric Stack Flow Rate Corrected to Standard Conditions dscflhr
G P04 3AS -0 227 22 -RI - L298 Page L4t of 278
Paclf, Corp: HuntlnEton I
EPA Method 2G Sample Calculetidns
Run rl @ Hlth Loed, S.mple Polnt 1 (04/13/20231
Md r (0.44 x %CO2) + (0.32 x %Or) + 0.28(10G%COr%Or)
= (0.44 x 12) + (0.32 x 7.5) + 0.28(100-12-7.5)
= 30.221bllb-mole
Mr= Max(l-B*J + (18.0x Bwt)
= 30,22 x (1 - 0.112) + (18.0 x 0.112)
= 2t.E6lb/lb-mole
Pr= Pui+(P/13.6)
= 23.38 + (.4.s/13.6)
= 23.05 in. Ht
Td= 460rtsr
= 460 +106
=565 R
(Eq.2G2)
(Eq.2G3)
(Eq.2G-s)
V.trt =lqxCex
85.49 x 0.82 x
.52.79?ltlsec
Q*=
x (cos011)
x (cos 0.2)
(T6 x PJ
(T1*,%r]
(s28 x 23.0s)
(s70 x 29.92)
(Eq.2G-6)
x WAF
x O.99
(Eq.2c-9)
3600 x (V.1"6) x (A) x
= 3600 x (55.059) x (570.08) x
= 79,871,119wsd,lhr
qd= Qcwx(1-BB)
= 79,871,339 x (1 - 0.1116)
= 7a;954,2t2Mlhr
(Aplr x T"ro
(P3 x MJ
G P043AS-0227 22-Kl - L298 Page 142 of 278
P.clfiCorp
Huntlngon Unlt 1
4lt3 - 4lL4l2O2'
Run *1 Sample Calculatlons
EPA Mathod 3A: Dct.rmln.tlon of Oxyten and Carbon Oloxlde Concentratlons ln Emlsslons from Statlonary Sourc.s
(lnstrumental Analyre, Procedur!l
(tlo CFR Pan 60, Appcndlx A-2)
(caw - q)x cma
(c. - q)
= 10.9 %w (Eq. 7E-sb)
Variabla Valu€)effnltlon Unlt of Maasuremcnt
C",r 11.3 Werage Unadjusted Gas Concentration Y"uw
q -0.1 \veraEe Prc/Post Zaro 6as Response vw
C..8.9 bncentration of Upscale Calibration Gas vo
c-9.3 \verage Pre/Post Upscale Gas Reponse !w
cr.10.9 \verage Gas Concentntion Adjusted for Bias vw
G P043AS-0 227 22 -Rr - L298 Page 143 of 278
PaclfiCorp
Huntlntton Unlt I
4ltr-41t41202t
Run S1 Sample Calculatlons
EPA Method 6C: Determinatlon of Sulfur Oloxide Emlsslons from Statlonary Sources
(lnstrumental Analyrrr Prcccdurrl
(40 CFR Pa.t 60, Appcndlx A{l
vsrlablG Valuc )eflnltlon Unlt of Measurcmant
23.7 ryerage Unadjusted Gas Concentration ppmvw
q 0.1 ryerate Pre/Post Zero Gas Response ppmvw
26.5 of Ups6le Calibration Gas ppm
c.26.5 Nerage Pre/Post Upscale Gas Reponse ppmvw
23.1 Nerage Gas Concentration Adjusted for Bias ppmvw
54.05 Volecular Weisht lbllb-mole
385-3 385.3 e of one Pound of ldeal Gas at standard conditions scf/
F.1800 : Factor from EPA Method 19 scf/mmBtu
c*3.84E-06 Pollutant Concentration, Wet Basis pound/wet standard cubic foot
COzo/ow 10.9 :O, Concentration wet volume percent
0.053 :mlssion Rate pounds per million British thermal units
Q*a 79,871,,339 :xhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
Eun,306.4 :mission Rate pounds per hour
(c-r-q)xc."
(c, - q)
(23.1-(0.1))x26.51
(26.s - (0.1))
= 23.1ppmw (Eq. 7E-sb)
= 3.84E{16 lb/scf
Er/*m= (cw) (FJ (1001
(COz%w)
= (3.84E-06) (1800) (100)
(10.e)
= 0.1|b/mmBtu (Eq. 19-7)
Ern,= (c*) (a*o)
= (3.84E{6) (79,871,339)
= 306.4 lb/hr
G P04 3AS - 0 2 2 7 22 - RT - t29 I Page L44 of 278
PaclfiCorp
Huntlngon Unlt I
4lLt - 4lL4l202t
Run *l Sample Calculatlons
EPA Method 7E: Determlnatlon of Nltrogen Oxldes Emisslons from Statlonary Sources
(lnstrumental Analyrer Procedure)
(tl0 CFR Pan 60, Appcndix A{}
c..=(C",,-C.)xC."
(c, - co)
(111.9-(0.5))x153.8
(1s8.5 - (o.s))
= 108.4 ppmw (Eq. 7E-5b)
= 1.29E-05 lb/scf
Et/o.u=(c*) (F.) (1oo)
(COr%w)
(1.29E-os) (1800) (100)
(10.e)
= 0.2|blmmBtu
furt'= (Q) (a*ar)
= (1.29E-0s) 179,e7 13391
= 1033.5 lb/hr
lEq.79-7)
Varlable Value )eflnltlon Unit of Measurement
111.9 \verage Unadjusted Gas Concentration ppmv
q Weraqe PrelPost Zero Gas ResDonse ppmw
C..153.8 :oncentration of Upscale Calibration Gas ppm
c.158.5 \verage PrelPost Upscale Gas Rcponse ppmw
108.4 \verage Gas Concentration Adiusted for Bias ppmvw
MW 46.01 vlolecular Weieht lb/lb-mole
385.3 385.3 /olume of One Pound of ldeal Gas at Standard Conditions scfllb-mole
F 1800 Factor from EPA Method 19 scf/mmBtu
c*1.29E-05 ,ollutant Concentration, Wet Basis pounds per standard cubic foot
COao/ow 10.9 :O? Concentration wet volume percent
Etv.^m o.274 :mission Rate pounds per million British thermal units
q*.n 79,871,339 :xhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
ErrA,1033.6 :mission Rate pounds per hour
G P04 3AS -02 27 22 -RT - L298 Page L45 ot 278
Paclficorp
Huntln8ton Unit 1
4lLt - 4lL4l2O2'
Run *1 Sample Calculations
EPA Method 10: Determlnatlon of Carbon Monoxlde Emlsslons from Statlonary Sourccs
(lnstrumental Analy:er Procedurel
(tlo cFR Part 60, Appendix A{)
(c""s-q)xc,a
(c, - q)
= (149.6 - (0.4s)) x 1s0.9
(1s6.e - (0.4s))
= 143.9ppmw (Eq.7E-sb)
(ce,) (MW)
(106) (38s.3)
(143.9) (28.01)
(101 (3ss.3)
= 1.05E{,5 lb/scf
Er/*a= (C*) (F.) (100)
(COr%w)
(1.0sE-os) (1800) (100)
(10.s)
= 0.2|blmmBtu
Er6,= (C*) (a*,o)
: (1.05E{5) (79,871,339}
= 83s.6 lb/hr
(Es. 19-7)
V.rleble Value )ellnltlon lJnlt of Measurement
cil x49.5 Werage Unadjusted Gas Concentration ppmvw
q 0.5 \verage Pre/Post Zero Gas Response ppmvw
c."150.9 :oncentration of Ups6le Glibration Gas ppm
c-156.9 Werage Pre/Post Upscale Gas Reponse ppmvw
Cro 143.9 Werage Gas Concentration Adjusted for Bias ppmvw
28.01 vlolecular Weisht lbllb-mole
385.3 385.3 /olume of One Pound of ldeal Gas at Standard Conditions scf/lb-mole
F 1800 Factor from EPA Method 19 scf/m m Btu
c*1.05E-05 : Concentration, Wet Basis pounds per standard cubic foot
CO2o/ow 10.9 lO, Concentration wet volume percent
Evt o.L73 :mission Rate pounds per million British thermal units
Q*'o 79,87L,339 :xhaust Flow Rate (From EPA Method 2F)wet standard cubic feet per hour
E rr'r,835.6 :mission Rate pounds per hour
G P04 3AS -0 227 22 -RT - L298 Page L46 of 278
Paciffcorp
Huntington Unit 1
4hr-4h412o23
Relatlre Accuracy Test Audlt Sample Calculations
NO, (lblmmBtul
Run t d2
1
2
3
4
5
6
7
8
9
10
11
72
0.274 0.225
o.L92 0.198
0.193 0.196
0.184 0.190
0.186 0.194
0.195 0_200
0.203 0.208
0.205 0.2L1
0.207 0.2t7
-0.011 0.00012
-0.006 0.00004
-o.oo3 0.oooo1
-0.006 0.00004
-0.008 0.00006
-0.005 0.00003
-0.005 0.00002
-0.006 0.00004
-0.010 0.00010
Average 0.197 0.204
Sum nlz nle
5um2 nla nla
-{t.007
-o.060
0.0036
o.@00s
0.(xxt45
nla
= 0.(X13
CC=(h-r') sd
= (2.306) (0.003)
= 0.002
RA= ldl+lCCl ,roo,
RM
=@'!:991 11ss1
o.797
= 4.4%
variables
td-,0.00045 ium ofthe squared Differences
IIdJ,0.0036 ;quare ofthe Summed Differences
n o {umber of Test Runs
sd o.oo3 itandard Deviation of Differences
h.ous 2.306 -value from P52, Table 2-1
cc 0.002 1.5% Confidence Coefficient
tdl 0.007 tbsolute Avera!e Difference
lcc 0.002 \bsolute confi dence coefficient
RM o.197 \verare RM Value
M 4.4%lelative Accuracv
G P043AS-02 27 22 -RT - r29B Page L47 of 278
Appendix B
Facility Process Data
G P043AS -0227 22-RT - L298 Page 148 of 278
Appendix B.1
Unit 1
G P043AS -0227 22 -RT - 1298 Page L49 of 278
Appendix B.1.1
Low-Load Flow RATA
G P043AS-0227 22-Rr - L298 Page 150 of 278
Average Data - Low Flow Run 1
Plant HUNTINGTON PLANT
lnterval: 1 Minute
Type:Block
Report Period: 0411212023 08:52 Through 0411212023 09:00
Time Online Criteria: 1 minute(s)
Source
Paramet6r
(Unit)
Ut12n3 08:52
UNIT,I
t,Ai(HKEUS
(NHG)
vtJz
(PCr)
FLqWSUFH
(scFH)
STKFLOW
(KSCFM)
STI(EMP
(DEGF)
UNITLOAD
(MVv)
23.565 9.9 35,767,751.8 u3.1
Ut12n3 08:53 35,949,995.6 828.5 '107.4ii 189
Ut12n3 @:54 9.9 36,058,759.9 831.6 'to7.85 189
Ut12n3 08:55 *,273,521.3 &t6.7 'to7.94 189
Ul12n3 08:56 9.7 36,184,155.7 E34.5 107.83 '190
Ml12n3 08:57 36,108,882.1 trj2.7 107.81 '191
Ul12t23 @:5E 23.9 36,264,026.5 107.77 191
Ut1zng 0E:59 23.564 36,173,845.0 &|3.9 107_58 't92
Ul12nO G):00 8.9 36,026,540.0 192
Average
Minimum
Maximum
Summation
hduded Oata
P^id.
Totral nmb6r of
nd, 9^i^rc
23.565
23.g
23.565
212.@1
9.7
9.5
10.0
87.6
831.9
923.1
836.7
7,4€7.5
107.5E
106.61
107.94
968.24
36,089,719.8
35,767,751.8
6,273,521.5
324.@7An.5
190
189
192
1,712
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4ll2/23 O9:26
GP043AS-0227 22-R-l - L298
G = Galibration
S = Substituted
T = Out Of Control
Page 151 of 278
Average Data - Low Flow Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0411212023 09:02 Through 0/.l'12/2023 09:10
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Oq1A23 09:02
UN]T1
BARPRESS
(INHG)
coz
(PCT)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNII LgAU
(lvlw)
36,',177,251.2 107.28 192
ut1u23 09:03 23.562 9.6 36.383.362.4 838.6 107.47 193
o4t1a23 36,257,186.8 107.68
04t1u23 09:05 23.562 9.6 36,056,903.9 8a1.7 107.87 193
o4na23 09:06 23.562 9.6 35,960,273.0 107.U
olt12t23 9.6 35,663,680.7 822.3 107.68 19rl
ut12t23 09:08 23.561 9.6 35,427,246.9 821.5 107.69
o4t12t23 35,954,954.8 828.9 107.55 194
Ul1A23 09:10 23.560 s.7 36,101,722.9 88't.8 107.17
Averago
Minimum
Marmum
Summetion
lncluded Oata
P^inta
Total number of
nd. P^i6la
23.561
23.560
23.563
212.O53
9.0
9.0
9.7
86.5
30,020,291.4
35,627,24€.5
36,383,362.4
324,182,822.6
830.4
821.5
838.6
7,473.8
107.58
107.17
107.47
968.23
193
192
1W
1.739
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated:. O4h2/23 O9:26
G P043AS-0227 22-RT - L298
C = Galibration
S = Substituted
T = Out Of Control
Page 152 of 278
Source
Parameter
(Unit)
0411?,23 09:12
Average Data - Low FIow Run 3
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: C4,11212023 09:12 Through 041122023 09:20
Time Online Criteria: 1 minute(s)
36,134,060.194
UNITl
BARPRESS
(NHG)
co2
(PCr)
FLOWSCFH
(scFH)
U I ATLUW
(KSCFM)
UI AI tsMlJ
(DEGF)
UNI I LUAU
(MW)
432.07.46
Ul1A23 09:13 23.560 9.7 36,089,022.2 832.3 107.75
Ul1A23 09:14 23.560 9.7 35,791,489.7 107.49 192
Ul12l23 09:15 23.560 9.7 35,772,130.0 824.2 107.18
Ul12l23 09:16 23.560 9.7 35,729,263.7 107.19 190
Oq1A23 09:17 23.560 9.7 35,720,322.6 423.2 107.33 189
UnA23 09:18 23.560 9.7 35,780,901.3 824.5 107.28
ut12t23 09:19 23.560 35,577,568.2 819.5 107.05 190
o1l12t2X 23.560 9.7 35.284.403.0 812.6 106.96
Awrage
Minimum
Maimum
Summetion
lncluded Data
P^inr.
Total number of
n.t. P^i^la
23.560
23.560
23.s60
212.UO
35,764,351.3
35,284,403.0
36,134,060.9
321.879. t61.6
9.7
9.7
s.7
87.3
424.2
812.6
832.9
7.417.1
107.30
106.96
107.75
965.69
191
189
194
1.721
F = Unit Offline
E = Exceedance
! = !nvalid
M = Maintenance
Report Generated: 04/L2123 O9227
GP043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 153 of 278
Average Data - Low Flow Run 4
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 04/12i2023 09:26 Through0411Z2023 09:34
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
UnA23 09:26
UNITl
BARPRESS
(tNHG)
cgz
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
5I KI EMP
(DEGF)
UNITLOAD
(tvlVV)
23.559 35,895,549.5 427 107 '192
04/1?/23 09:27 9.7 35.552.713.2 r07.35
Ml12l23 09:28 9.7 36,111 ,649.4 1o7.17
0{,/12i23 09:29 36,175,026.6
Ul12l23 09:30 36,121,064.1 8i)1.6 106.73 192
04l'12123 09:31 36,087,537.4 831.1 't06.95
Oq1A23 09:32 9.6 35,898,790.0 827.0 107.09
Ul1A23 09:33 35,702.666.3 822.1 106.86
Ul1A23 09:34 35,379,1142.1 106.66 191
Average
Minimum
Maximum
Summation
lncluded Data
P^ihra
Total number of
n.lr P^inre
23.559
23.559
23.559
212.031
9.6
9.6
9.8
86.8
35,924,937.6
35,375,142.1
36,175,026.6
323,324,438.6
827.5
814.4
833.0
7.447.1
107.00
106.66
107.35
963.00
'192
191
193
'l,727
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/ t2/23 O9:59
G P043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page L54 of 278
Average Data - Low Flow Run 5
P|ant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0/,11A2023 09:36 Through 0411212023 09:44
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ml12l23 09:36 1919.6 35,607,704.4 8't9.r r06.25
UNITl
BARPRESS
(rNHG)
co2
(PCT)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW
ut1u23 09:37 23.559 9.6 35.&2.249.4 820.O 106.34 192
ut1u23 09:38 23.559 s.7 35,831,549.9 824.5 192
Mna23 09:39 23.559 820.79.7 35.666.099.9 106.44 192
o4t12123 23.559 1919.7
191
35,644,581.2 820.r
823.7o4t12t2309:41 23.559 35.805.548.9 106.29
o4t12t23 3s,991,660.5 a27.5 105.96 190
04112t23 09:43 23.559 9.8 36.202.247.3 832.3 't05.9t 190
una23 09:44 23.559 36,310,341.4 8i!5.1 106.12
A\rerage
Mlnimum
Maimum
Summation
lncluded Data
P6i^lc
Total number of
nql. D^i^ta
23.559
23.559
23.559
212.O31
35,855,775.9
35.607.704.4
36,310,341.4
322,70',t,542.5
9.7
9.6
9.8
a7 _5
824.8
819.'t
835.1
7,423.0
146.24
105.91
106.46
s56.18
191
't90
192
1,720
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generatedl. 04 / 721 23 09 :59
G P043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 155 of 278
Average Data - Low Flow Run 6
Plant HUNTINGTON PIANT
lnterval: 1 Minute
Type: Block
Report Peri od: O4l 1 21 2023 09: 46 Throug h 04 I 1 Z 2023 09:54
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul1A23 09:46
UNIT,I
BAt<t t<Ess
(NHG)
co2
(PCr)(scFH)
S I KFL(Jvv
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(tulW)
23.558 9.8 36,073,070.3 06.93
O4l1U23 09:47 36.070.210.8 107.26
O41U23 09:€ 23.559
O4/12l23 09149 -----: 2355ti-
35,997,580.0 107.32
9.7 35,803,263.6 825.0 107.23 192
Ul12l23 O9:5O 23.558 s.7 35,912,091./t 827.4
UnA23 09:51 36,109,492.0 107.12
36,153,011.50411U23 09:52
Ul1A23 09:54 35,623,8tt!9.0
Awrage
Minimum
Maximum
Summation
lncludod Data
P^ihte
Total number of
nrtr P^lnle
23.559
23.558
23.559
212.027
35,954,023.1
35,623,839.6
36,153,01 1.5
323,586,208.'1
s.7
9.6
9.8
47.1
828.4
820.6
833.0
7,455.3
107.16
106.93
107.32
w.42
192
191
1U
1.727
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/L2/23 LO:Oo
G P043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 156 of 278
Average Data - Low Flow Run 7
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: 0411212023 09:56 Through 0/'11212023 10:04
Time Online Criteria: '1 minute(s)
Source
Parryneter
(Unit)
UnA23 09:56 23.s59 9.6 35,738,861.3 422_9
UNITl
tsAKI.KEJU
(INHG)
vgz
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UN]TLOAD
(tllW)
UnA23 09:57 35,702,135.7 u1.9 106.68 191
Ul12l23 09:58 23.559 35,631,252.9 106.51 190
0411u23 09:59 23.559 9.7 35.311.056.9 812.3
o4t12t23 23_559 35.253.102.2 810.9 106.25 190
ut1u23 '10:0'l 23.558 9.7 35.073.043.7 820.6
ut12123 10:O2 23.558 35,900,305.8 825.8 106.15 190
ut1u23 10:03 23.558 9.8 35,897,539.3 825.9
01t12123 23.557 35.985.474.8 828.2 106.50 191
A\rerage
Minimum
Marmum
Summation
lnduded Data
P^int.
Totd number ot
ndq hinla
23.558
23.557
23.559
212.026
9.7
9.6
9.8
87.3
820.9
810.9
s2s.2
7,388.s
106.42
106.15
106.81
957.77
190
189
191
1,713
35,677,641.4
35,253,102.2
35,985,474.8
321.@4.772.6
F = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated:. 04 / LZl 23 70:26
G P043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page t57 of 278
Average Data - Low Flow Run 8
PIant: HUNTINGTON PTANT
Interval: 1 Minute
Type: Block
Report Period: 0/'1121202310:06 Through 0411212023 10:14
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul1U23 10:06
UNITl
BARPRESS
(INHG)
co2
(PCT)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
ruw)
23.557 9.8 36,490,053 u0.4 106.91
Ul1U23 10:07 36,886,746.6
UI|UZS '10:08 30,367,517.3 837.9 107.06
04n423 10:09 23.556 36.342.881.4 837.9 107.44
MnA23 10:10 36,749,515.2 u7.5 107.U
UnA23 10:11 23.556 9.7 36.t(18.872.s 107.80
ul1a23 10'.12 35,927,229.0 108.10
UnA23 10:13 23.555 36,055,353.6 832.6
Ul1U23 10:14 36,265,436.8 837.2
Average
Minimum
Marmum
Summation
lncluded Data
P^inla
Total number of
nata P^inta
23.556
23.555
23.557
212.O03
9
9
36,391,5't 1.8
35,927,229.O
36,886,746.6
327.523.606.3
9.7
9.5
9.8
87.2
839.2
829.2
849.6
7.552.9
107.60
106.91
108.35
968.43
195
194
196
1,7y
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generate d: O4l L2 I 23 tO :27
G P043AS -02 27 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 158 of 278
Average Data - Low Flow Run 9
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 041121202310:16 Through 04112/2O23 10:24
Time Online Criteria: 1 minute(s)
Sourc€
Param€ter
(Unit)
04/1?J23 10:16
UN]T1
uAr(l,xE!5
/INHA\
v(J2
/D'T\
FLOWSCFH
/cnE!\
STKFLOW
/tacnEtA
litKtEMt
/ntr.:E\
UNITLOAD
/lflAr\
9.5 34,888,1 1 5.4
Ul12l23 10:17 23.554 34,790,790.6 80r.5 106.99
Ul1A23 10:18 u,741,972.7 EOo.2 106.86
o4l1a23 10:19 23.5*9.7 34,976,120.0 106_80
Ul12l23 10:20 35,063,877.1 807.6
Ul12l23 10:21 23.553 35,225,961.2 811.4
UnA23 10:22 35,521,697.3 106.77
Ul12l23 10:23 9.8 35.352.419.r
0U12123 10:24 35,345,075.6 813.6
Awrag6
Minimum
Madmum
Summation
lncluded Data
P^intc
Total number of
ndc P^intc
23.553
23.552
23.554
211.979
35,100,669.9
u,741,972.7
35,521,697.3
315,906,029.0
9.7
9.5
9.9
87.3
I
I
808.4
800.2
818.1
7,275.9
106.82
106.r14
107.30
961.41
I
9
190
189
192
1.710
F = Unit Offline
E = Erceedance
I = lnvalid
M = Maintenance
Report Generate d: O4l t2 / 23 t0:27
G P04 3AS -02 27 22-Rr - t298
C = Calibration
S = Substituted
T = Out Of Control
Page 159 of 278
Appendix B.1.2
High-Load Flow RATA
G P04 3AS - 0 22 7 22 -Rr - 1298 Page 160 of 278
Average Data - High Flow Run 1
P|ant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: o4.11312023 06:12 Through O4/13/2023 06:50
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
G{,l13l23 00:12
UNITl
tsAt(l,KE55
(rNHG)
vuz
(PCr)
I.L(,WUUFH
(scFH)
STKFLOW
(KSCFM)
STirEMP
(DEGF)
UNITLOAD
(t{W
I 1,833.4 108.26 1't4
o4,l13l2l 06:i3 78,700,230.0 1,43/..7 104.24 1U
Ul13l23 06:14 23.330 10.5 78,357,228.7 1,824.4 108.14
Ul13l23 06:15 23.330 78,159,127.4 1,422.9 108.20 494
04113123 06:16 23.3i:t0 't0.6 78,295,046.6 't,825.5 108.30
04113123 06:17 23.330 10.6 78,300,077.1 1,824.5 107.97 496
Ul13l23 06:18 23.330 78,395,250.5 1,825.9 107.70 498
Ul13l23 06:19 23.330 r0.6 78.017.055.1 1,830.6 107.56
Ul13l23 06:20 78.413.577.8 1.825.6 107.47 503
Uh3n3 06:21 23.331 10.6 77,714,529.O 1,810.4
04./13n9 08:22 77,214,114.e 1.799.4 't08.06 500
Ul13l23 06:23 23.333 10.6 77,301,128.6 1,800.5 107-77
Ul'13123 06:21 77,459,682.0 1,803.5 107.58 4%
Un3n3 06:25 23.3U 10.5 76,871,853.2 1,789.6 107.53 490
Ul13l23 06:20 23.333 10.5 76.414.527.1 1,779.5 107.6'l
Ut1g23 OOi27 10.5 76,863,454.9 1.789.5 107.56 /185
04113123 06:28 23.334 10.5 77 .231.807.A 1,798.1 107.56
01113123 06:29 77.986,010.9 1.815.2 107.41 482
Ul13l23 06:30 23.334 10.5 78,532,011.3 1,827.8 107.35 82
04113123 06:3'l 23.3U 10.6 78.2U.175.5 1,820.2 107.41
Un3n3 06:32 23.3U 10.6 78,011,089.0 1.815.3 107.27 .183
Ul13l23 06:33 23.3U 10.6 78,144,O0/.3 1,817.8 107.11
Ul13n3 06:3/+78,'t76,950.7 1,818.7 107.15 482
04l13ng 06:35 23.336 10.6 78,227,945.1 1,819.1 106.94 4t!9
Ul13l23 06:36 23.337 10.6 78,537,018.3 1,526.1
Ul13l23 06:37 23.338 10.7 78,573,290.6 1,827.1 106.98 498
o1,l1g23 06:38 23.338 10.7 77.844.310.6 1,810.8 107.15
Ul13l23 06:39 77,080,318.3 1.793.1 107.21 4%
Ul13l23 06:40 23.398 10.7 77 .159.737.7 1,793.8 108.85 492
O413l2S 06:4'l 77,584,994.1 1,803.9 106.90
Ul13l23 0A:42 23.338 10.7 77,638,8,4,4.2 1,806.2 107.26 .+88
o1.l13l23 06:43 10.7 77.414.251.7 1,801.0 107.42
o4,l13l23 00:44 23.338 10.8 77,423,773.2 1,801.9 107.18 4U
Ul13l23 06:45 23.338 10.8 77.4',t9.928.9 |,802.5 107.67
Ul13l23 06:46 23.338 10.8 77,426,784.3 1,802.7 107.68 499
Ul13n3 06:47 23.338 77,302,156.8 1,800.1 107.75
*t"t Fsunatoffliffdtt . _** _* 'o't "lt'*t'o - -- ''"t't " . 'o''* t*
0{,t't3t23 dSftCeedancez3.338 10.9 76,780,050.7 1,785.5 107.00 1e7
10.8
! = lnvalid
M = Maintenance
Report Generated: OalBl23 06:57
G P04 3AS - 0 2 2 7 22 -RT - L298
(; = galtDraflon
S = Substituted
T = Out Of Control
Page 161 of 278
Average Data - High Flow Run 1
Plant: HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: 0411312023 06:12 Through 0411312023 06:50
Time Online Criteria: 1 minute(s)
Ul13l23 06:50 23.338 ,0.9 76,398,756.5 1,777.4 107.27
Average 23.334
Minimum 23.330
Maximum 23.338
Summation 910.045
lncluded Data 39
P^intc
Total number of 39
nat.9^i^la
10.6 77,741,A92.7
10.5 76,398,756.5
10.9 78,700,230.0
1,809.8
1,777.4
1,8U.7
107.52
'106.85
108.30
4,193.09
493
481
503
19,2't4
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04/L3/23 O6:5t
G P04 3AS -0 2 27 22-RT - 1298
414.9 3,031,933,815.2 70.580.3
C = Calibration
S = Substituted
T = Out Of Control
39
39
39
39
39
39
39
39
39
39
Page 162 of 278
Average Data - High Flow Run 2
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1 31 2023 07: 06 Throu gh M I 1 31 2023 07 :26
Time Online Criteria: 1 minute(s)
Source
Paareter
(Unit)
Ul13l23 07:06
UNITl
tsAtil,xEtil,
(rNHG)
L;O2
(PCr)
FL(,WliuFT'
(scFH)
5t llt'LL,W
(KSCFM)
UIAIEM|-
(DEGF)
UNI I LI..,AU
(MW)
,n1.06.80 452
Mt13t23 07:O7 70,285,959.2 1,n3.2 106.78
Ul1U23 07:OB 23.339 t0.8 74325.107.O 1,774.3 106.80 496
oI,t13t23 07:09 23.338 10.9 70,826,496.5 1,786.1 106.87 157
Ul13l23 07:10 23.339 t0.9 70.520.364.9 1,778.7 106.79 499
Ul13l23 O7t11 74,624,211.7 1.781.1 108.77 498
Ul13l23 07112 23.338 10.9 77,003,626.2 1,790.3 106.88
Ul13l23 07:13 23.338 10.9 76,539,417.9 1,779.1 106.85 496
Ul13l23 O7:'t1 23.338 10.9 75,766,447.0 1,761.0 106.72
Ul13l23 07:'t5 23.338 10.8 75,570,522.1 1.756.5 144.72 490
Ul13l23 07:16 23.338 10.8 75,418,840.5 1,7il.O 107.05
0/,l13l23 O7i17 23.339 10.8 75,063,312.2 1,717.5 107.66 485
0/,t13n3 07:18 75,313,847.5 1,753.7 107.79
ut1u23 07:19 23.339 10.8 75.90't.437.9 t,706.9 107.U 486
01t1w23 O7:2O 23.vO 74,ofi,252.5 1.742.7 107.39 489
04t13123 23.340 76,694,793.3 'l,785.3 107.€t 491
utlu?3 07:22 23.U0 10.8 76.089,219.9 1,785.2 192
utlgn 07:23 23.U1 10.8 78,707,570.0 1,7U.5 107.29 493
0/.t13t23 07:24 23.U1 10.8 76,822,629.8 1,786.1 106.94
ut1u23 07:25 23.U1 t0.9 70,904,903.7 1,788.1 107.01 498
04t13123 23.U2 10.9 77,1go,e/',t.4 1,795.8 107.38 498
Awra0e
Minimum
Marimum
Summatlon
lndudod Deta
D^lht.
Total number of
nd. P.rint.
23.339
23.338
23.v2
/+90.125
10.8
't0.8
10.9
227.7
1,775.5
1 ,747.5
1,7S5.8
37,2U.5
107.11
104.72
107.79
2,249.36
493
/185
499
10,354
76,338,518.8
75,063,3'12.2
77,190,U1.4
r.603.r08,894.4
21
21
21
21
21
21
21
21
21
21
21
2',1
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 041 L3 / 23 07 :33
G P043AS-02 27 22-RT - L298
C = Galibration
S = Substltuted
T = Out Of Control
Page 163 of 278
Average Data - High Flow Run 3
Plant: HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: 0/,11312023 07:49 Through 04/13/2023 08:09
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul13l23 07:49
UNITl
BARPRESS
(rNHG)
co2
(PCr)
FLOWSCFH
(scFH)
It I K|-L(JW
(KSCFM)
5I KI EMP
(DEGF)
UNITLOAD
(Mw)
23.35'l 10.7 76,976.0.[1.9 789.9 191
Ut13l23 07:50 23.351 10.8 77,116,869.7 1,759.1 t06.95 493
Ul13l23 07:51 23.349 10.8 77.123.594.3 1.792.4 495
04113t23 07'.52 23.350 10.9 76,620,308.1 1,78'.t.4 107.14 494
04113123 07:53 23.349 't0.s 76,4*,421.5 r,778.3 107.39
UnA23 07:51 23.U5 10.9 76,363,751.8 1,776.4 107.46 4%
Ul13l23 07:55 10.9 76,548,210.9 1.780.8 107.53
Ul13l23 07:56 10.9 76,487,U4.7 1,780.4 107.80
Ul13l23 07:58 23.U5 10.9 76,O4.2A7.9 1.771.9 493
Ut1U23 07:59 23.U5 75,846,768.r 1,767.2 108.30 493
o1,113ff23 O8:m 10.9 75,644,825.1 1.762.0 108_15 494
Ul1U23 08:01 23.U6 76,100.W.2 1,771.8 107.88
O1113t23 08:02 23.y6 10.8 76,571,248.1 1.782.5 451
O4l1A23 08:03 /3.y6 76,363,979.3 1,778.O 't07.91 492
04113123 08:(X 10.8 76,080,716.6 1,77',t.4 107.91 452
04rl?23 08:05 23.U7 49210.8 70,520,899.8 1,781.3 'to7.81
Ul13l23 08:06 10.9 76,360,7,l{}.9 1.n7.5 107.74
04l1U23 08:07 23.U7 10.9 75,985,7l:}.5 1,768.5 107.70 495
Ul13l23 08:08 11.0 75,971,544.6 1.767.9 107.63 495
Ul1U23 08:09 23.U7 11.0 75,891,940.2 1,765.5 107.44 457
Avorago
Mlnlmum
Ma,dmum
Summation
lnduded Data
P^inla
Total number of
n.t. hlnle
23.348
23.W
23.351
4SO.298
76,362,S85.8
75,W,825.4
77,419,8A5.7
1,@3,622,702.9
1,777.1
1,762.0
1,799.1
37,319.6
'to7.67
106.93
108.32
2,261.12
r0.9
10.7
11.0
228.2
493
491
457
10.363
21
21
21
21
21
21
21
21
21
2'.1
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generatedt 041L3123 O8:Ll
GP043AS-0227 22-RT -L298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 164 of 278
Average Data - High Flow Run 4
P|ant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ul13l2O23 08:26 Through 0411312023 08:46
Time Online Criteria: 1 minute(s)
Sourca
P*amet€r
(Unit)
Ul1A23 08:26
UNITl
t'AI(lJKE55
(INHG)
voz
(PCr)
FL(,W5UI.H
(scFH)
titKI-LUW
(KSCFM)
5I KI EMP
(DEGF)
UNII LOAU
(tfW)
23.U4 10.9 77.181.407 1,798.9 108.44
Ul13n3 08:27 23.U6 76,752,151.2 1,788.6 l08.rtl
Ul13l23 08:28 23.v5 10.9 74,278,787.5 't,n7.8 't08.43 497
An13n3 08:29 23.U3 76,172,282.1 1,774.0 108.62 498
04113123 08:30 23.34{t 10.9 76,460,951.7 't,782.0 108.38 496
Ul13l23 08:31 2?.U3 74,4$4,448.1 1,781.3 108.13
Ul13l23 08:32 2X.344 to.0 76,202,113.7 1,776.3 108.5'l /189
Ul13l23 08:33 23.U3 10.9 74,175,778.3 't,777.1 108.93 .188
Ul13li23 08:34 76,125,7$.6 't,783.0
Ul13l23 08:35 23.U4 10.9 70,934,957.0 1,7%3 108.82 495
Ul13l23 08:36 23.U5 76,587,0€8.5 't,787.3 109.19 503
041?,23 08:37 23.v5 11.0 n,o23,o8/'9 1,7Xt.7 108.95 509
Ul13l23 08i38 ?3.348 11.0 76,349,518.5 1,781.1 109.03 508
o41A23 08:39 23.346 11.0 75.692,411.9 1,787.1 109.42 504
Mt13fr23 08:40 B.U7 11.0 75,30rt,9.t'1.6 1,75A.1 ,l09./ttt 499
04113123 08:41 ?3.348 I1.0 75,581,940.0 't,7u.o 109.33
O4l1U23 08:42 z.J.U9 10.9 75,854,049.3 1,Tfo.3 109.32 488
Ul13l23 08:43 23.U9 10.9 76.104.834.0 1.775.6 109.15 €9
Ul13l23 08:44 23.348 76,029,rO9.0 1,773.6
Un3n3 08:45 2?.Us 10.9 75,938,774.9 1 ,771.4 109.02 4,97
Ul13n3 08:46 76,086,829.8 1,n4.4
A\,6ra0e
Minimum
Marimum
Summation
lnduded Data
Bdi6le
Total number of
nd. O^lnl.
23.346
23.U3
23.99
/+90.25S
76,266,939.2
75,304,941.6
77,181,407.6
1,601,605,723.0
1,778.8
1,758.1
1,798.9
37,31+.9
108.88
108.13
109.46
2,786.42
10.9
10.9
11.0
229.1
496
/188
509
10,411
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Erceedance
I = lnvalid
M = Maintenance
Report Generated:. 04 | t3 I 23 08:48
G P043AS-0 227 22-RT - t298
C = Calibration
S = Substituted
T = Out Of Contro!
Page 165 of 278
Average Data - High Flow Run 5
P|ant: HUNTINGTON PLANT
Interval: 1 Minute
Type: Block
Report Period: 0411312023 09:02 Through 04/1312023 09:22
Time Online Criteria: 1 minute(s)
Source
Pararnet€r
(Unit)
Ul1A23 09:02
UNlT1
BARPRESS
(NHG)
c02
(Pcr)
FL(JWUUFH
(scFH)
U I ITFLIJW
(KSCFM)
5t Kt EMt
(DEGF)
UNII LUAU
(lulW)
23.U7 10.9 76.457.768.0
4{,/13t23 09:03 10.9 76,590,864.9 1,783.7 108.04 492
ul13t23 09:()4 23.W 10.8 70,65€,92'1.8 '1,784.E 107.91
ut13t23 09:05 23.W 10.8 70,570,756.9 1,782.3 107.71 492
04/13n3 0g:06 23.W 10.8 76,246,217.3 1,775.4 107.66 tl89
ul13t23 09:07 23.346 10.8 76,2&,0W.7 1,774.0 107.50 488
ut1a23 09:08 23.346 10.8 76.779.757.2 t,786.5 107.54 ,189
ut1a23 09:09 23.U7 10.8 77,1*j17 .5 1,795.8 107.71 492
Ul13l23 09:10 23.U7 10.8 76.951.677.8 |,790.7 107.62 497
Ul13l23 09:'11 23.346 10.9 76,907,685.4 1,789.6 107.58 502
Ul13t23 09:12 23.U6 11.0 77.322.27A.1 1,799.8 107.71 504
Ul13l23 09:13 23.3,[5 11.0 77,175,185.2 1,79$.7 107.7A 504
ut13t23 08:14 23.U5 11.0 70,008,083.'t 1,770.0 107.95
04113123 09:15 23.v 50111.1 75,537,467.9 1,759.4 108.06
o4t13l'i23 I1.0 75,723,181.2 1,763.5 107.98 499
0413r/23 09:17 23.W 11.0 75.813.019.6 1.765.4 107.91 498
0411u23 09:18 B.U4 11.0 75,828,561.0 1,745.2 to7.7a 496
Mt13t2t 23.{5 11.0 75.857,565.2 1.766.1 107.83
04t13t2X 09:20 23.345 75,447,575.3 1,755.7 t07.88 452
ut13t23 23.345 10.9 75.20A.261.2 1.751.0 107.88 488
04,t13t23 Ogi22 23.45 75,lag,086.7 't,757.7 107.89 486
AvBrage
Minimum
Maximum
Summation
lndud€d Deta
f^lnl.
Total nunrber of
n.tr Daihta
23.346
23.W
23.U7
4SO.256
74,2U,510.5
75,206,261.2
77,322,276.1
1,601,574,729.1
1,775.9
1,751.0
1,799.8
37,293.5
107.81
107.50
108.06
2,2A?.51
10.9
10.8
11.1
225.1
495
486
5(N
't0,389
21
21
21
21
21
21
?'l
21
2'.1
21
21
21
F = Unit Offline
E = Erceedance
I = lnvalid
M = Maintenance
Report Generated: 041 L3 123 O9:24
G P04 3AS -02 27 22-RT - t29 I
C = Galibration
S = Substituted
T = Out Of Control
Page 166 of 278
Average Data - High Flow Run 6
P|ant: HUNTINGTON PI.ANT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1312023 09: 59 Through A4l 1312023'10:19
Time Online Criteria: 1 minute(s)
Source
Paran€ter
(Unit)
Ul13l23 09:59 10.9 76,771,U1.4 1,78.7 108.06 493
UNITl
tsARPItESS
(NHG)
co2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(lvlW)
Ul13l23 10:00 23.337 10.9 76.804.064.0 1.789.7 108.15
Ul13n3 10:01 23.337 76,404,701.3 1,781.3
Ml13l23 10:02 23.336 10.8 78,720,814.3 1,788.3 108.29 49r
04.,11?123 10:03 23.336 76,365,776.3 1,780.8
Ml13l23 10:04 23.336 49110.8 76.68/.3?2..7 1,788.8 108.73
Un3n3 10:05 23.336 10.7 76,675,181.4 1.788.6 108.70
Un3n3 10:OG 10.8 76,875,128.1 1,791.6 't08.18 452
Ut1u23 10:07 23.336 10.8 77,158,766.0 1.797.0 107.82
Ul13l2l 10:08 77,045,068.8 1,795.5 108.18 1U
Ul13l23 l0:0O 23.336 10.8 77,033,371.4 1,795.8 10€.34 4U
Ul13l23 10:10 23.336 7t,345,183.9 1,803.0 108.33 152
Ul13l23 10:11 23.335 10.7 77.158.923.0 1,799.5 108.59 491
04113123 10:12 23.334 10.7 2,500,088.6 1,807.8 108.65 192
O1l13l2t lo:13 10.7 78,305,226.5 1,825.0 108.14 1U
0411A23 10:14 23.332 10.7 78,338,1r[5.7 1,825.3 108.00
Ul13l23 10:15 r/,813,307.6 1,8't3.6 108.14 4U
Ulllti 10:16 23.332 10.7 77.354.00S.1 1,803.0 108.20 493
UIIAA 10:17 23.332 10.7 77,403,703.5 1,80[.4 108.23
4413123 10:18 10.7 77,850,733.8 1,815.5 108.114 490
Ul13l23 10:19 23.331 t0.6 77.768.9{,8.4 1,814.0 108.50 488
Awra0€
Minimum
Modmum
Summaiion
lnduded Data
P^lnla
Total numbcr of
n.h g^ihta
23.335
23.331
23.337
&o.o27
77 ,208,757.6
76,305,776.3
78,338,145.7
r,62r,383,908.8
1,799.9
1,780.8
1,825.3
37 ,797.2
108.32
't07.82
108.73
2.274.65
10.8
10.6
10.9
225.9
492
/l88
,[94
10,335
2',1
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4lt3l23 L0:23
GP043AS-0227 22-Rr - L298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page L67 of 278
Average Data - High Flow Run 7
P|ant: HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 04,1131202311:15 Through Ml13l2O23 11:35
Time Online Criteria: 1 minute(s)
Source
Per*Yret€r
(Unit)
Ul13n3 11:15
UNITl
tiAF(l.xEl'U
(NHG)
wz
(Pcr)
t-L(Jvv5gt-tl
(scFH)
5I AFLUW
(KSCFM)
!i I KI EMP
(DECF)
UNII L(JAU
(tfW)
77,9U,O51.7 t08.30
Ul1A23 l1:'16 77.880.804.0 1,815.9
04113123 11:17 77,955,912.3 1,818.1
UnA23 11:r8 t0.6 77,242,3%.8
04t't3t23 t't:19 76,736,950.8 108.58
04t1?123 ',t1:20 10.6 77,U1,294'3
04,l'1U23 11i21 77,947,207.8 108.90
ul13t23 11'.22 77,U4,212.8 1,817.5
Ul13l23 11:23 77,150,176.5 108.94
Ul1U23 11:21 77,406,255.2 1,805.7
04,l'13123 11:25 77,393,056.7 1 08.1 1
Ul13l23 11:2A n,000,9it3.7
Ul1U23 11:27 70,559,136.9
Oq13n3 11:28 76,756,600.7
0il13/23 11:29 76,846,234.S 1,751.2
Oll13l23 11:30 78,127,S3/.J 1,775.5 108.37
04t1u23 11:31 8.325 78,256,1't3.0 1,778.3 108.27
0,,l13l23 1'l:32 76.853.905.0 1,791.9 108.16
o{,l13l23 11:33 ?3.323 74,8415,582.4 '1,793.2 108.61
04113123 11:U 77,755,572.1 t,814.1
0q1gn 1l:35 77,377,&7.8 1,804.5
A\rerage
Minimum
Maximum
Summation
lnduded Data
P^lnla
Total numbor of
ndr D^lnla
23.327
23.323
23.331
489.871
77,212,255.2
76,'127,9y.0
77,955,912.3
1,421,457,559.2
1,800.8
1,775.5
1,819.4
37,E17.5
108.41
108.01
109.07
z.2ta.as
21
21
10.8
10.5
10.6
222.O
485
480
494
10,182
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4l L3 I 23 7L:43
GP043AS-0227 22-RT -1298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 168 of 278
Average Data - High Flow Run 8
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period: O4l 1312023 1 1 : 50 Through A4l 1A2023 12: 10
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul1U23 11:50
UNITl
BARPRESS
(NHG)
co2
(PCr)
FL(JWSUrn
(scFH)
5t K!-L(JYV
(KSCFM)
UI KI EMI'
(DEGF)
UNI I LgAL'
(?,w
23.320 .5 1,812.7 107.71 491
ul13t23 11:51 10.6 77,8il.?57.4 1,4fi.4 't07.80
Mt1il23 11:52 23.320 10.6 77.685.520.5 1,811.4 490
0/,t't3t23 I l:53 10.6 77,227,259.7 1,801.1 108.22
ul13t23 ,l:54 23.319 10.6 76,705,172.O 1,788.9 108.13 87
Un3n3 11:55 23.319 r0.5 76,587,820.7 1,794.0 107.71 486
Ul13l23 11:56 23.319 10.5 77,360,892.7 1,802.9 107.74 /Ant
04/l3t2X 11:57 23.319 77,545,196.0 1,808.6 108.20 4U
041'13123 11:58 23.321 10.6 77,756,080.1 1.813.6 4U
Ul'13123 11:59 23.321 77,&13,891.8 1,815.0 108.17 485
ut13123 23.320 t0.6 77.656.775.5 1.809.1 107.58
Ul13l23 12:01 23.320 79,o27,028.3 1,818.0 107.67 $7
Ul13l23 12:02 23.320 t0.6 77,571,555.1 1,816.3 107.55
O4l13nB 12:03 zj.321 10.6 77,910,029.9 1,815.6 107.74 490
04113123 12tU 23.320 77,530,212.6 1,807.0 107.86 490
o4t1u23 12:Os 23.319 10.8 77.514.500.8 1,807.1 107.96 490
04113t23 12:OA 23.320 10.6 77,8a7,60'1.4 't,816.4 108.18 489
04t'13t23 12:O7 10.5 77,8U,751.3 1,814.9 108.30 489
ul13t23 12:08 23.319 10.5 77,582,894.6 1,809.7
04113123 12:Og 23.3r8 77,20/.,U3.1 1,WO.7 108.19 tas
0/,t13t23 23.317 10.4 77,1 18,630.5 1,798.4 108.07
A\,6rage
Minimum
Maximum
Sunxmation
lncludad Data
9^16t.
Total number of
l1il. P.l^la
23.320
23.317
23.321
4€,5.714
77,509,671.0
74,705,172.0
74,027,028.3
1,628,963,091.5
1,808.4
1,788.9
1,818.0
37,975.8
107.57
107.55
'108.30
2,267.44
10.6
,10.4
10.6
221.8
87
4U
491
10,237
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4lL3/23 l2:3O
G P04 3AS -0 2 27 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 169 of 278
Average Data - High Flow Run 9
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0411412023 06: 12 Through 0411412023 06:32
Time Online Criteria: 1 minute(s)
Source
Param€ter
(Unit)
Ul'14123 06:12 78,498,72
UNTTl
BARPRESS
(rNHG)
co2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW)
23.397 t0.7 ,814.103.71
Ul11l23 06:13 79,001,ofi.7 1,422.4 103.89
A n4/23 06:14 23.397 to.7 79,172,140.7 1.825.9 103.76 492
MlllDg 06:15 79.030.408.0 1,821.7 103.50 452
Ul14l23 06:16 23.397 t0.7 78,799,308.2 1.816.8 103.62 492
Ml1lng 06:17 78,500,456.2 1,8'.t1.2 104.01 452
o4114123 06:18 23.397 to.7 78,250,700.3 1.805.6 't04.07
Ml'l4l2l 06:19 23.397 78,047,008.9 1,800.3 103.88 489
04114123 06:20 23.397 10.7 78,105,890.8 1.802.1 104.03 486
0,,114,i23 06:21 23.397 78,384,953.4 1,809.3 r04.25 486
Ul14l23 08:22 23.397 10.6 78,812,720.3 1,819.6 104.36 87
Ul14l23 06:23 23.397 10.7 78,739,485.'1 1,817.5 104..24 /Ag
Ul11t23 08:21 23.397 10.7 78,521,825.4 1,821.9 10{,.32 492
04t14123 06:25 23.397 10.7 79,263,981.3 1,830.9 496
04t14123 06:26 23.397 10.7 75,140.524.4 1,829.5 105.10 498
Ul14t23 6:27 23.398 10.7 78,627,996.0 1,817.2
0411123 06:28 10.7 78,2/18,0/18.6 1,808.6 105.04 496
Vl14l23 06:29 23.398 10.7 78,273,583.3 1,809.0 105.17
Ml11l23 06:30 10.6 78,443,828.7 1,813.7 105.09 493
Ul14l23 06:31 23.399 10.6 78,423j92.7 I,811.9
Oll14l23 06:32 77,773,955.9 1,795.7 104.45 493
Average
Minimum
Marmum
Summation
lnduded Date
P.i6tr
Tot6l number of
nd. hl^le
23.357
23.397
23.399
491.346
10.7
10.6
'10.7
224.2
192
486
498
'10,332
78,603,840.5
77,773,959.9
79,263,981.3
1.650.080.650.1
1,814.6
1,755.7
1,830.9
38,106.2
r04.33
r03.50
105.17
2.190.98
21
21
21
21
21
21
21
21
21
2'.1
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated : O4l t4l 23 06:35
G P043AS-0227 22-RT -L298
G = Calibration
S = Substituted
T = Out Clf Control
Page t7O of 278
Appendix 8.1.3
Gas RATAs
G P04 3AS -0 2 2 7 22-RT - L29 I Page L7L of 278
Average Data - Gases Run I
PIat HUNNNGTON PLANT
lntav*'1 Minut!
Tvlc Blo*
H
4ts ctt
't3u?Gr
U.3trtup
i.F! cili.* oalt!/2!
GP043AS-022722-RT- 1298
I
Page 172 ol 278
Average Data - Gases Run 1
Plant: HUNTINGTON PTANT
lnteryal: 1 Minute
Type: Bl6k
Report Period: 04/l 3/2023 06:1 2 Th rcug h 04/1 3 12023 06:50
fime Online Cdt€ria: 1 minute(s)
br.:co rblhrEceror.tr usi[h.t ieut.d @ tb/m&u
As@ U5 0.16 106 14.9 LOS.7 O.% 'fi.3 A.6 0.6 &.9 & 4594.6Mho 27.a O.G 1O,s 5.1 gi6i Ot$ 1@3 2t1,2 0.6 l!.8 dt 4459.33.S,6 O.m 10.9 e7.4 1,175.2 OA 12tO A.! O.B Z.g S 4670.7sffin a,B7! 7.14 a149 5.@.9 {,31a3 6.in a,yt.1 !0,a9 2N !15.5 1a,214 1791EE
l,fudtuhtuh T $ s s s s s € s 39 $ s
Tdndrd&€S9$a9SSS3o$os
F = Unit Off,ine
E = Erceedlnce
C = Ctllbntlon
S = SubJtltutcd
M = Mdntcnmce
T = Out Of Control
' = Sutpcct
L, = Stt.tup
8.Frt 6.nmtd: q/13/23
GPO43 AS - 0227 22-RT- 1298 Page 173 of 278
i
i
I
Average Data - Gases Run 2
PIAI HUNTINGTON PI.ANT
lnt.nd: I iilin$.
TylC gock
R.gort P.lod: 0a/13rr023 07:0t Tlmuoh 04t13/2023 07r2C'lln Onh. cllJh: I mhriccl
Uti
ffio0I
i
I
b@ryL.!*,d*Mryd@5/ffi
Aq. lg7.a
5fu {47
Euem
ffi art!
ll*rm n
rddlb i
@
6
w
G
ts
tql
ts
fr.,
![t
us
r!7,
i
^
0'
n7
@
0tqt
a
A
IE
qt!
@
(fl
4
2l
s
da
t@
2U
a
a
au
a?
tar
n
n
oq
oa
6
trg
71t
ot
u
{.4
4ru
4&a
&Q
tEr
a
1
-s-
tog
A
a
d
n
x
x
x
x
7l
il
F. Unftqiln
I r luibno
Cr Crlbtand
3 rsltdtllt.d
t ! tlalrtaafrct
T t Out Ol Cfftrel
. ! so?aat
U tSlftrD
isrffiod[n!
GP043 t!s.0227 22-RT-1298 Page 174 ol 278
l
Average Data - Gases Run 3
PISi: HUT.ITINGTON PLANT
lnisrd: l Mindc
TDo: Block
Ropott Pniod: O,a/13/2023 07:40 Timuoh O/U13r2023 0E:09
Tlmc Onina Cdt€da: I mhdr(s)
se
Ufl
B!% @:l
Bi
rq -awtg oE
wt% 05 irai
qt# of 14.0 @
-t ru
4t& 6fi r4t xat -
-o@re
hE nU
i|lfu4U
h 9.!
ffi la.t
qtx
W
w
wa
la
IG?
fi!
N
tpi
fau
t&a
z,w
21
4
G.7
&7
9U
1a,w
z
a
qls
qtr
@
111f
al
s
t@
2.@O
21
21
4.,
*7
nrt
t,a7
21
2l
@
oq
qo
t.tg
u
74.7
21,4
€.1
aff@
am
am
a.G
i
A
€
g
0
10,3
71
lt
21
4
n
n
21
21
d
a
a
2l
F.Unilffilm
E.tuaadro
Cr ctllb[dd
3 ' Sr&3tlEr.d
,{3tdm$rm
T E Oot Ol Contret
t . Sutpct
U r $f,tup
rFrffisns/ts
Gn 43 AS - O2Z7 22-RT- 1 298 P.qe L75 ot 278
il
i
i
L
\
i
A\rerage Data - Gases Run 4
Pht HUMNNqION PIAiTT
lnhn d: 1 Mh!{.
T)r.: Bck
R.pod Pilod: 04flt 2O13 0E:8Iirugh 0/Ut3/2023 0t:0
TInc Onh. Crt{h: 'l nilruh(.)
h
ffi ln
8S@
ri
i
I
,q. l.O
f,furu
ffiaE
ffi
^11.7
lffrs n
Td*dE n
EO
IrG
re
m
tu
tu
tl,
La
&
lw
GI
q67.7
21
21
ma
&a
nat
1..al
21
2l
0.!o
qt6
q0
re
I
E?
s
a6t
A
A
fr,
&l
ru
qd17
a
n
6
o&
@
l.1D
u
!s
1A
Q.7
c
&
o
4iil
4g
4il.o
o,fr2
n
a
A
,t
A
2l
2l
x
2t
n
d
21
2t
21
I
F. UntOtltr.
E.gcaadrro
c.Srdot
I rsrictho.l
X.lkmnca
T'oin OtOrld
{ . t0iact
UtSEttiFturr.A q/!/2r
GPO{3 rS - 0227 22-RT- 1 298 P.ge 176 oJ 278
Average Data - Gases Run 5
FIri: HUNNNGTON PI.ANTlnt{v* 'l Minuio
Typ.: Blod(
R.pqt Psbd; 0,U13r1023 0e:02nrelsh 0irl3/202$0e22
Tlr. Onll. qlbrL: I mhutcol
M
Urt
trtEr !0
I
l
I
,
I
i
Irl
I
I
ha. t.m
IhnS
m' t$,t
ffi,q's
tffmn. a
rdl*ch a
@
qt!
E
.D
l&t
fis
a
UI
2l
a
&7
&
att
lis
21
2t
qtr
GtlT
@
4m
g
Ers
2.n7
4
A
4t
N
I
r$47
d
n
q&
u
6
1A
!qt
t7t
2tt
s
5
d
ry
t0,
aga
ffit
a,w
,s
n
x
to
ts
t!.t
A1
i
!
l
4
d
2l
A
I
n
n
i
a
^
a
a
F . Unlt Otln
I r lluadaro
Ct CrlEndon
3r$lrrlnlt.il
t. tihhLraio
T r Out O, Cort ol
r r irpact
U r ttmupislaffig/1tru
GP0,{|3AA-O227?2-RT-1298 P.ge 177 ot 278
r
i
L
Average Data - Gases Run 6
P|f* HUNflNTTOT PI.ANT
lntlvd:1Mln .
TtDc Bct
R€pqt Pqlod: 0,ilitf2023 00:te ihlul0h OtflU|m23 l0:ieItr. orrlr! Cdtdi: t m[ruta(8)
P.rridr(m
(ts m
i
h:6t&ff&ldol4hrlBd6m
qr @ ls w2 qg !u a 4r(o
lruq00tn70@l7t-ffi,
ruMrtGtnu6r.rg(a
rx& I 1rG alxi t.t! ffi {s tm
4121444n21
142liiaa21
!.@ @ tct
&6tts
tsa @ lot
a@€N
21 ilA
21 11
IG?
ar.l
s
l{rt
a
frldfficr
P.gc 178 of 278
F. UnftOftlrl.
I'h.dxo
C'm[doi
3t$Dadurd
1r.tlffi0m
T E O[t Ol Cotrtrel
. r SutDaci
U r$.nup
i#ffiqayll
GP043AS-022722-RT- 1298
li
I
I
DIVISION OF AIR OUALITY
I
l
I
I
Average Data - Gases Run 7
Ph: HUT{TINGTON PIAI{T
lnbnd: I Uhub
Typc: Ed(
R.ooil P.dod: 0lul911023 ll:l51hreWh 0fi3rf23 tl:!5
11m. Onh. Cil.d.: I mlruic6)
h
h,raaatd
mE ttda
AeG
ht&
hi6,
.d &
@
@
GTT
t-t
ru
tu
tU
ru
&
tu
1211
r.s,l
A
a
gt
14t
a,t
1XD.'
i
n
w
w
6t€
tw
t7
iN
1r&
4
i
A7
m5
ru
aru
4
2t
M
6
6
t.t{
21
,t
l1!
!7'
ru
o
C
5
d
ro,i&
a,g7
4,4
4&7
la
A
2t
ffirb
tdfrr&
d
A
a
!
{
2t
tt
a
a
i
x
2l
F r Unlt Ollfln
lrlHdno
C. G.Xlradoug.nlDdubd
x.,JhianE
TtolndOilnl
. ' sulDacl
U.ltr,nl'irytgn.ruq/!|/8
GP043AS-022722-RT-1298
li
li
Pagc L79 ol 278
t.lir
I
I
I
l
1,
tl
l
ill
Average Data - Gases Run 8
Phi: HUiITINGTO.I PUI{T
lntrva; I Miiln
TyIa: Eck
Roqt Pqlod: Ou1s/:lmt 1150 1ltreucn oi#l?ninj2l 12t10
Tlnc On}|a gtaL: t mlnutGlr)
i i|!*riut
116 rrn
i
I
I
i
kf s7
f,fuE
rma,
ffiim
@
@
q!6
t.o
tu
iu
lu
a,
s
t72
fis
1.ts
a
n
g,
E'
u
20,iaJ
2t
2l
ut
@
€r!
tu
lo.!
tg
1!Oa
a
2l
Ii
xo
&
wt
4
i
m
G
E
t.rd
til
rlt
a7
q7,a
61'
.&
4io
re
A
n
&
g
5
tofr
| *-*
Hlrtrb
n
fl
A
a
a
a
a
2t
2l
i
21
21
71
n
F. Unltqilm
I t llcadro
Cr C.llbdbn
3t$brltubd
m r il.lntnrrra
?. Ot t Ot Oontrcl
. r so{nal
U t Strtup
i.FtCnG4 g/rY!
GPO 43 AS- 0227 22-RT- 1 298 Pagc 180 ot 278
l
Average Data - Gases Run 9
PIfit HUI{TINGTON PI.Ai.IT
lntm/d: 'l Mlnuta
Tn : Block
RGoql P..lod: O{1/U2023 00:t2 lho{Oh 0iU1lU2023 0C:3ll
Ttm Onflr cltdla: I dnutc(a)
M
H
ula *12
,1
I
I
I
Ma. ,€
h A.7
5hW
.l'fi &l
lldd&S 4
l{ftcu x
u
@
6
B
tct
u
t07
ru
o,
ia,
G,7
E!
GP
GO
1,@/
4,e2
n
2l
ut
ON
ula
&
tH
rGl
tu
25'
a
a
GI
m
q
BI
a
2t
N
m
w
tT
&
zl
ru
&
g
g
10&
4&
4S
{xll
,.&
2l
2t
I
I
,i
n
4
A
21
21
21
4
n
A
2l
d
A
21
a
F.Unldh
E.arcaadro
C.OIE.doo
3=sladlnlbd
IrEnlaim
T.OnOtOdd
t . Sorpact
U rStftuE
rwt8n .a* oabal2!
GP043AS-022722-RT-1298 Pag€ 181 of 278
Appendix 8.2
Unit 2
G P043AS -02 27 22-RT - t29A Page L82 of 278
Appendix B.2.1
Low-Load Flow RATA
G P04 3AS-02 27 22-RT - L298 Page 183 of 278
Average Data - Low Flow Run 1
Plant: HUNTINGTON PLANT
Interval: 1 Minute
Type: Block
Report Period : Ul 1 31 2023 1 4: 29 Throug h O4l 1 31 2023 1 4:34
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
ul13t23 11'.29
UNIT2
t,AKI-KEli5
(NHG)
v92
(PCT)
FLUWUUFII
(scFH)
t'I KFLUW
(KSCFM)
t'I KI EMP
(DEGF)
UNII LgAU
(MW)
9.4 37 36
Ul1g23 14:30 37,388,305.4 w.7 187
Ul13l23 14:3'l 37,460,'t69.4
Ul13l23 14:32 37,685,254.8 871.4 187
04113123 14:33 37.945.845.6 477 _8
O!.l13l23 11:g 38,O52,112.2
Awrage
Minimum
Mardmum
Sumination
lnduded Data
P.!inlc
Totd number of
ndc Brinta
23.320
23.318
23.321
139.918
37,670,175.9
37,388,305.4
*,o52,112.2
224,021,O55.1
9.4
9.4
9.4
56.4
871.2
844.7
880.2
5.227.1
103.44
103.36
103.55
620.63
188
187
188
1.125
F = Unit Offline
E = Exceedance
I = lnvalid
M = Malntenance
Report Generated: 04/ 13 I 23 t4:54
G P043AS-0227 22-RT - t298
C = Calibration
S = Substituted
T = Out Of Contrc!
Page 184 of 278
Average Data - Low Flow Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od: 041 1 31 2023 1 4: 37 Throu g h Ml 1 31 2023 1 4: 43
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul13l23 14:37
UNIT2
(NHG)
co2
(Pcr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNI I LgAU
(MW
9.3 37,601,278.1 869.2 103.27
Ul13l23 14:38 37,680,109.4 103.24
Ul13l23 '14:39 23.321 37,849,781.1
04113123 '14:40 37.868.644.8 103.23
Oll13l23 11:41 23.319 37.647.386.4 '103.22
ul13l23 14..12 23.319 37.740.@7.1 872.5
877.O
103.25
103.3923.319 37.924.559.6Ul13l23 14:43
Average
Minimum
Milimum
Summation
lncluded Data
P6int.
Total number of
n.tr P^iht.
23.320
23.319
23.322
163.241
37,758,909.5
37,601,274.1
37,924,559.6
264,312,366.5
9.3
9.3
9.3
65.1
872.9
869.2
877.0
6,'t 10.4
103.26
103.21
103.39
722.81
189
188
189
|,321
7
7
F = Unit Offline
E = Exceedance
I = lnvalld
M = Maintenance
Report Generated: O4l13l23 t4:55
GP043AS-0227 22-RT -t298
C = Galibration
S = Substituted
T = Out Of Contrcl
Page 185 of 278
Average Data - Low Flow Run 3
Plant: HUNTINGTON PLANT
Interval: 1 Minute
Type: Block
Report Period: 0/,1131202314:45 Through 0411312023 14:51
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ml13l23 11:15
UN]T2
BARPRESS
(NHG)
G02
(Pcr)
TL(,Wl'UFT'
(scFH)
!' I KFL(JW
(KSCFM)
l'IKIEMP
(DEGF)
UNII LUAU
(trfw)
37,r14'l,948.0 188
Ul1U23 14:46 23.3't8 37,53't.685.1 867.9 188
Ul13l23 11:47 37,634,412.7 103.16 188
Ul13l23 '14:48 37.533.432.2 867.8 188
Ul13l23 '14:49 37,343,785.8 103.30 189
04113123 14:50 23.317 37,447,708.4 866.1 189
01113123 14:51 37,535,162.3 189
A\r€rage
Minlmum
Maximum
Summation
lnduded Data
Pai^h
Total number of
ndr hi6tc
23.318
23.317
23.319
163.225
37,495,504.9
37,343,785.8
37,63,4.,412.7
262.468.534.5
9.3
9.3
9.4
65.3
867.1
863.6
870.0
6,069.4
103.32
103.16
103.44
723_28
188
188
189
1,319
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4lt3/23 14:55
GP043AS-0227 22-RT - 1298
G = Calibration
S = Substituted
T = Out Of Conttol
Page 186 of 278
Source
Parameter
(Unit)
04113t23 15:15
Average Data - Low Flow Run 4
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: Ml 1312023 1 5: 1 5 Through O4l 1312023 15:21
Time Online Criteria: 1 minute(s)
,520,820.0
UNIT2
UAT{IJ'{ESt'
(rNHG)
coz
(Pcr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW
9.2 37 887 't03.32
04113123 15:16 37.514,272.5 w7.4 'ls7
Ul13l23 15:17 23.319 37.578.723.3
Ul13l23 15:18 23.319 9.3 37,503,346.8 867.5 103.52 187
Ul13l23 15:19 23.319 37.548.438.2
Ul13l23 15:20 23.319 9.3 37,605,596.4 103.55
Ul13l23 15:21 23.319 37.639.056.6
A\rerage
Minimum
Maximum
Summation
lncluded Data
P^lnla
Total numbor of
nala P^ihte
23.319
23.319
23.320
163.2U
37,558,607.7
37,503,3/10.8
37,639,056.6
262,910,253.8
9.3
9.2
9.3
65.0
868.7
867.4
870.7
6,080.9
103.48
103.30
103.56
721.33
187
't88
188
't,308
F = Unit Offline
E = Exceedance
I = lnvalid
M = Malntenance
Report Generated: 04 / 73 I 23 16 :O3
G P043AS-0227 22-R'r - L298
C = Calibration
S = Substituted
T = Out Of Control
Page t87 of 278
Average Data - Low Flow Run 5
P|ant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0/,1131202315:23 Through 0411312023 15:29
Time Online Criteria: 1 minute(s)
Source
Pardneter
(Unit)
0/.l13l23 15:23
UNIT2
tsAKTKEUU
flNHG)
vuz
(PCT)
FL(JWSUFII
(scFH)
ij I KFLUW
(KSCFM)
5I KI EMP
(DEGF)
UNI I LgAU
ruw)
471.2 103.49 187
04113123 15:24 23.320 37,601,216.7 869.8 103.58
Ul13l23 15:25 37.67A.420.4
Ml13l23 15:26 23314 37,243,8,{.5.9 861.7 103.62 189
Ul13l23 15:27 35,517,9'16.1 101.20 '189
Mt13l23 15'.2A 23.317 36,599,915.5 8/l.1 99.79 '189
Ul13l23 15:29 23.3't6 37.242.672.2 't88
Av€rage
Minimum
Madmum
Summalion
lnduded Data
P6inl(
Total number of
n.t. D^i^tG
23.318
23.316
23.320
163.227
9.3
s.2
9.3
64.8
37,096,744.7
35,517,916.1
37,793,225.5
259,677,212.7
856.0
818.2
874.2
5.9S1.9
102.10
99.23
103.77
714.68
188
187
189
1,319
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4113123 76:04
GP043AS-0227 22-Rr - L298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 188 of 278
Average Data - Low Flow Run 6
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : Ul 1 31 2023 1 5: 3 1 Throu gh Mh 312023 1 5:37
Time Online Criteria: 1 minute(s)
Source
Pararfleter
(Unit)
04113n3 15:31
UNIT2
6A}<PKESt'
(rNHG)
ao2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW)
37,'176,848.6 186
01,/13123 15:32 23.315 9.2 37.038.297.0 r86
04113123 15:33 37,120,549.2 186
Ml13l23 15:34 9.3 37,395,860.0 98.92 186
Ul13l23 15:35 37,361,335.1 186
011'13123 15:36 37,520,376.8 859.9 98.24 187
-**-"i
B?Ul13l23 15:37 37,679,215.4 s7 _74
A\rerago
Minimum
Marimum
Summalion
lncluded Data
D^i^le
Total numbar of
nat. P^inlc
23.315
23.314
23.3't6
163.206
9.3
9.2
9.3
64.8
37,327,503.2
37,038,297.0
37,479,215.4
261,292,522.1
855.8
a,,s.2
862.8
5,990.6
98.47
97.78
98.92
689.27
186
186
187
1,304
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: 04 h3 / 23 16 :O4
GP043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 189 of 278
Average Data - Low Flow Run 7
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period : 04 I 1 31 2023 1 5: 39 Throu gh Ml 1 31 2023 1 5:45
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul13l23 15:39
UN]T2
BARPRESS
(INHG)
co2
(PCT)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(oEGF)
UNI I L(JAU
(Mv9
37,702,033.3 s7.4
Ul13l23 15:40 23.317 38.079.505.9 97.95
Ul13l23 15:41 23.316 38,644,989.6
Ul13l23 15:42 23.317 39.133.842.8
Ml13l23 15:4il 23.3't7 38,338,204.7 101.57
Ul13l23 15:44 23.317 37.986.379.8 102.13
04113123 15:4"5 37,763,7a2.3
Awrage
Minimum
Marmum
Summation
lncluded Data
P^inla
Total number of
n.la B^inte
23.317
23.316
23.317
163.218
38,235,542.6
37,702,033.3
39,133,842.8
287,6/.8,798.4
9.4
9.4
9.4
65.8
7
7
879.2
862.8
900./t
6,154.4
100.14
97.48
't02.59
700.99
190
'189
'191
1.330
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generate* 041t3123 16:05
G P043AS-0227 22-Rr - L298
G = Calibration
S = Substituted
T = Out Of Control
Page 190 of 278
Average Data - Low Flow Run 8
Plant: HUNTINGTON PISNT
lnterval: 1 Minute
Type: Block
Report Period: 041131202315:47 Through 0411312023 15:53
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
04.113123 15:17
UN]T2
tsARP'{ESs
(rNHG)
v(J2
(Pcr)
FL(JWSUT-H
(scFH)
\itK|-LUW
(KSCFM)
lit Kt EMt
(DEGF)
UNII LUAU
(MVv)
23.318 9.3 138.8
ut13t23 15:la 23.317 37,785,495.4 873.2 102.93
04113123 15:49 23.318 37.819.155.4 102.89
Ul13l23 15:50 23.318 37,512,846.4 102.93
04113123 15:51 37.222.557.1 103.17
04113123 15:52 37,334.825.9
Ul13l23 15:53 23.319 37,51 3,1 00.2
A\r€rage
Minimum
Marmum
Summation
lncluded Data
f.i^la
Toial number of
n2ta 9^iht.
23.319
23.317
23.320
163.230
37.535,359.9
37,222,557.1
37,819,155.4
262.747.519.2
s.2
9.2
9.3
64.5
867.5
860.4
873.8
6,O72.2
7
7
103.02
'102.76
103.29
721.17
189
188
190
1,323
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4l L3 /23 16:05
GP043AS-0227 22-Rr - t298
G = Calibration
S = Substituted
T = Out Of Control
Page L9L of 278
Average Data - Low Flow Run 9
Plant HUNTINGTON PIANT
lnterval: 1 Minute
Type: Block
Report Period: Ul 1 31 2023 1 5: 55 Throu gh O4l 1 31 2023 1 6:0'l
Time Online Criteria: 1 minute(s)
Source
Paraneter
(Unit)
Ul1U23 15:55
UNtT2
BARPRESS
(lNHG)
c(Jz
(PCr)
FLOWS(;FH
(scFH)
s tKI-LOW
(KSCFM)
STKTEMP
(DEGF)
UN]TLOAD
(trrw)
37,422,89.A 103.'t 1
Ul1g23 15:56 37,440,791.0 103.10
Ul1A23 15:57 37,427,124.7
Ml1A23 15:58 37.309.591.9 462.2
Ul1!23 15:59 37,215,213.5
04.113123 16:00 7.6 I 37,542,020.9 *7.7 103.12
Ul1g23 16:01 6.5 I 37,600,943.9
AvBrage
Minimum
Malimum
Suffination
lnduded Data
P.rinte
Total number of
nd. P^int.
23.320
23.318
23.322
r63.239
7
7
9.3
9.2
9.3
.16.3
5
7
37,431,168.0
37,2'.t5.213.5
37,660,9rt3.9
262,018,175.9
865.1
860.0
870.6
6.055.9
103.10
103.02
103.28
721.73
188
187
188
1,313
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4l 13 / 23 L6 :O6
G P04 3AS -0 2 27 22-RT - t29a
C = Calibration
S = Substituted
T = Out Of Contro!
Page L92 ot 278
Appendix 8.2.2
High-Load Flow RATA
G P04 3AS -0227 22-RT - t298 Page 193 of 278
Average Data - High Flow Run 1
P|ant: HUNTINGTON PI.ANT
lnterval: 1 Minute
Type: Block
Report Period: Uh42O23 09:08 Through 04f1412023 09:46
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul'11123 09:08 478
UNIT2
BARPRESS
(rNHG)
co2
(PCr)
TLUWliUFN
(scFH)
SIKI.LUW
(KSCFM)
UI KI tsMP
(DEGF)
UNITLOAD
(MW)
23.436 10.6 82.875.839.101.30
U|14123 09:09 23.436 10.6 82,1188,133.6 1,892.2 101.68 476
Ul14l23 09:10 10.5 82,2M,977.5 1,890.2 103.0rt 176
Ul14l23 09:11 23.437 10.5 81,741,818.0 1,881.2 103.53 478
Ul14l23 Og:12 10.5 81,975,591.9 'r,887.0 103.68 478
Ul1U23 09:13 23.139 10.s 82.178.430.9 1,8S2.8 104.05 179
Ul'14t23 09:14 10.5 a2,473,537.O 1.899.3 41
Ul14l23 09:15 23.439 10.5 82,,47,951.8 1,897.3 103.63 /181
Ul14l23 09:'16 23.439 81,913,459.1 1,884.8
04111123 09:17 23.t139 10.5 8r,778,081.5 1,8a1.4 103.4'l 479
Ul14l23 09:18 23.440 82,147,523.3 1,889.1 103.19
0,,,1141123 09:19 10.5 81,892,008.6 1,882.6 103.04 ,180
Ul1M23 09:20 23.412 r0.5 81,757 ,879.1 I,880.7 103.19
Ul14n3 09:21 23.44.2 10.5 81,438,921.3 1,873.4 103.41 479
Ul14l23 09:22 23.42 81,406,1 16.1 1,872.2 103.30
Ul14l23 09:23 10.5 82,005,517.6 1,885.1 103.02 €0
Ul14l23 09.24 23.443 '10.5 82,678,821.3 t,90't.6 103.34
o4,114fr23 09:25 10.5 82,052,834.6 I,900.5 103.22 82
Ul14n3 09:26 23.445 10.6 82,565,700.7 1,898.0 103.10 42
a5Ul14l23 09:27 10.6 82,709.399.8 1,901.1 103.03
Ul14l23 09:28 23.444 82,908,405.4 1,905.7 103.04
Ul14l23 09:29 10.6 82,522,U2.8 1,896.7 103.03 .fSs
Ul14l23 09:30 23.445 10.7 82,140,320.4 1,894.8
Ul14l23 09:31 10.7 82.576.597.7 1,897.7 102.93 486
Ul14l23 09:32 23.45 10.6 82,553,r|{}0.1 1,896.9 102.85
Ul14l23 09:33 23.445 10.7 82.314.321.2 1,891.4 102.87 $7
01114123 09:3{23.44 r0.8 81,997,617.0 1,884.8 103.07 488
04114123 09:35 23.445 82,068,225.7 1.887.1 87
04t1423 09:37 23.47 8:r,061,677./t '103.09 rl83
04.114/23 00:38 23.447 82,555,774.1
Ul14n3 09:39 23.147 10.6
Ul14l23 09:40 23.47 82,507,286.6 1.897.2 475
Ul14l23 09:41 10.5 82,192,593.0 1,890.rt 101.14 47A
Ul14l23 O9:12 10.5 82,'170,087.6 1,889.6
o4t14t23 ts#unit offli?f#8 43,2@,711.2 1,913.6 103.0110.5
1.919.6 101.89ut1u23 P$ficeedance23..[s0 83,701,98r.6 181
I = lnvalid
M = Maintenance
Report Generated: o4/t4/23 09:48
GP043AS-0227 22-R-r - L298
(j = r,allDfall0n
S = Substituted
T = Out Of Control
Page L94 of 278
Average Data - High Flow Run 1
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0411412023 09:08 Through 0411412023 09:46
Time Online Criteria: 1 minute(s)
ut14t23 09:46 23.45'1 10.6 82.869.515.3 1,899.2 101.52
Average 23.443
Minimum 23.436
Maximum 23.451
Summalion 914.288
lncluded Data 39
P^inta
Total number of 39
n.b 9^i^ta
10.6 82,390,103.3
10.5 8'l,406,116.'l
10.7 83,701 ,98't.6
I,894.0
1,872.2
1.919.6
103.08
101.30
104.05
481
476
4ti8
I 8,767
39
39
411 .7 3,213,214,027.2 73,867.6 4,020.29
C = Calibration
S = Substituted
T = Out Of Control
39
39
39
39
39
39
39
39
F = Unit Offline
E = Exceedance
I = !nvalid
M = Maintenance
Report Generated: 04/ L4/ 23 09:48
G P04 3AS-02 27 22 -RT -1298 Page 195 of 278
Average Data - High Flow Run 2
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Peri od : Ul 1 41 2023 1 0: 00 Through O4l 1 41 2023 1 O:20
Time Online Criteria: 1 minute(s)
Sotrrce
Param€ter
(Unit)
Ul11123 10:U)
UNIT2
BARPRESS
(rNHG)
co2
(PCT)
FLOWSGFH
(scFH)
5t K!-LUvv
(KSCFM)
s'I KI EMP
(DEGF)
UNITLOAD
(Mw)
23.45!I 10.6 81,825,81 142
Un4n3 10:01 23.453 10.5 82,124,110.2 1,885.0 100.38 482
An1q23 10:02 82,404,309.5 1,883.7 100.15
Ut14l23 10:03 23.453 10.6 81,607,856.7 1,866.8 100.54 82
Ul14l23 10:04 81,969,6Ar.5 1,875.8 1co.74
Ul14l23 10:05 23.1il 10.6 82,437,521.2 1,886.4 100.74 ,t81
Ul14l23 10:06 23.455 82,389,267.7 1,884.6 100.58
Ul14l23 10:07 23.49 10.5 81,896,18t!.5 1,O72.9 1@.42 475
Ul14l23 10:08 2t.155 81,587 ,174.8 1,872.2
Ml11n3 10:09 23.455 10.5 82,155,257.1 1,879.3 100.33 478
Ul14l23 10:10 23.455 81,737,140.9 1,869.2 100.42
Ul11l23 l0:'ll 23.4et 10.5 82,032,1€.2.4 1,878.1 101.11 477
Ul14l23 10:12 23.458 10.5 82,663,786.9 t,896.8 102.39
O1t14li23 l0:13 10.5 82,503,509.8 1,894.7 102.87 477
04114123 10:11 10.5 82,534.,227.O r,895.1 102.82 477
04114123 10:15
O4t11l2S 10:16 23.458 10.5 81,826,493.6 1,879.8
o4114123 10:17 23.,+58 10.5 82,318,4/.8.2 1.890.6
04/14123 '10:18 23./+59 10.5 82.805.78€..2 1,901.8 102.92 480
Ul14l23 10:19 23.458 10.5 82,659,630.9 r.899.1 480
Ul14l23 10:20 23.1159 10.5 82.078.722.4 1,886.0 103.20 482
Avera0e
Minimum
Ma)(imum
Surmation
lnclud€d Data
P.J6te
Total number of
n.t. hl^ra
23.456
23.452
23.460
192.576
10.5
10.5
10.6
221.1
82,2U,033.3
81,607,856.7
82,805,788.2
1,726,284,699.0
1,883.0
1,868.8
1,901.8
39,556.3
101.56
100.15
103.20
2.132.77
480
477
484
10,071
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4/14/23 LO:22
G P043AS-0227 22-RT - L298
G = Calibration
S = Substituted
T = Out Of Control
Page 196 of 278
Average Data - High Flow Run 3
Plant: HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: 0411412023 10:36 Through M11412023 10:56
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul14n3 10:36
UNIT2
BARPRESS
(rNHG)
v9z
(Pcr)
FL|r,WsUFII
(scFH)
STKFLQW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAO
(MW)
42,1
Ul'11123 10:37 23.M 10.6 82,135,975.?1,879.3
Ul14l23 10:38 23.&t0.6 82.154.578.6 1,878.5 100.57 M
Ml11l23 10:39 82,248,*t9.7 1,878.8 100.o3
Ml14l23 10:rO 23.$6 10.0 81,919,735.1 1,870.3 483
Ul14l23 10:41 23.$7 81,844,060.6 1,869..1 r00.02 ,+83
Ul14l23 10:42 23.47 10.6 81,870,334.6 1,871.8 100.52 M
Ul14l23 10:43 23.166 10.7 80,928,969.5 1,854.0 101.70 485
0,{.1141123 10:44 23.&10.7 81,703,159.8 1,871.1
Ul14l23 10:45 23.55 10.6 82,159,559.5 r,886.5 102.95 rt85
Vl14l23 10:46 23.$3 10.0 82,235,O28.9 1,888.9 103.12
Ul11l23 '10.47 23.M 10.6 82,596,318.8 1,897.3 103.16 rt85
04114123 10:,18 23./+65 10.6 82,520,780.7 1,895.2
04114123 10:49 23.rt80 10.6 82,360,859.4 r,891.1 102.97 &
04111123 l0:5O 82,297,08/.4 1,889.8 103.00
04114123 10:51 23.466 '10.6 82.209.127.7 1,887.4 102.90 483
Ul14l23 10:52 23.466 10.7 81,818,614.2 1,878.3 102.U 481
Ul14ln 10:53 23.467 10.6 81,655,686.6 1,E75.3
o4.l't4/23 10:54 23.67 10.6 81.556.764.7 1,474.2 103.44 479
04.11423 10:55 81,449,056.s 1,871.3 't03.35 481
Ul14l23 10:56 23.1@ 10.7 81.738.088.8 1,477.4
AErage
Minimum
Marmum
Summation
lnclud€d Dste
9^idr
Total number of
n.lr P^l^la
23./t66
23.463
23.48
492.777
81,980,084.3
80,928,969.5
82,596,318.8
1.721.581.709.3
1,879.5
1,e54.0
't,897.3
39,/+69.7
102.10
95.77
103.4
2,144.07
10.6
10.6
10.7
223.2
/183
475
485
't0,147
21
21
21
21
21
2',1
2'.1
21
21
21
21
21
F = Unit Offline
E = Eceedance
| = lnvalid
M = Maintenance
Report Generated: O4h4l23 lO:59
G P04 3AS -0 227 22-Rr - t29 8
C = Calibration
S = Substituted
T = Out Of Control
Page L97 of 278
Average Data - High Flow Run 4
Plant HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: Ml14l2O23 1 1:12 Through 0411412023 11:32
Time Online Criteria: 1 minute(s)
Source
Parsneter
(Unit)
Ul14l23 11i12
UNIT2
UAXI'KEsU
(NHG)
cgz
(Pcr)
t-Lowsut-H
(scFH)
STKFLOW
(KSCFM)
STIiTEMP
(DEGF)
UNITLQAD
(Mv9
23.409 80.055.224 ,837 47
01t14t't23 1',t:1?23.468 11.0 80,077,9t2.0 1,838.7 103.01 47
04/11t23 1'l:'14 11.0 80,273,480.1 1,843.5 '103..l3 486
04t14t23 1'l:15 23.&1 1.0 79,858,398.4 1,834.1 103.17 €0
ut11t23 l'l:16 10.9 79,485,155.7 |,825.9 103.25 €5
ul14123 11:17 23.4t 8 10.9 79,576.410.9 1,824.1 103.2s
ut11t23 I 1:18 2?.464 79,616,628.9 1,828.9 103.26 /183
ut14n3 1l:19 23.ffi 10.9 79.427,6U3.5 1.824.3 100.19
04t14t23 11t20 23.408 79,579,094.8 1,827.7 103.16 483
Ml11l2l '11:2'l 23.$7 10.9 79,953,305.2 1,836.2 108.10
ut14l2x 11:22 23.&6 40,212,511.3 1,841.8 102.99 484
ut11n3 11:23 23.465 10.9 8t,.,+53.61 1.8 1,U7.8
od,t11li23 l1:24 23.465 10.9 80,51 1,91 3.6 1,850.2 103.40 ,t85
O1l1N23 11:25 23.$5 10.9 80,493,129.3 1,849.8
04114123 11''26 ?3.466 11.0 80,299,999.0 1,835.9 100.55 /AB
o4t14t23 11:27 11.0 40,227,457.5 1,8y.2 100.53
ut14123 11:28 23.466 11.0 80,1 10,138.8 1,831.7 100.60 490
un4n 11'.29 11.0 80.458.082.9 1.839.4
ul14t23 11:3O 23.484 11.0 80,586,412.1 1,U2.3 100_53 490
ut14t23 '11:31 t 1.o 79,996,659.3 1,825.4 100.70
ut14t23 11:32 23.87 t 1.0 79.905.444.3 1,829.5 100.98 €6
Av6rag€
Minimum
Marmum
Surwration
lndudod Dsta
Pri^la
Total number of
n.t. O^l^ta
23.467
23.465
23.445
492.805
80,058,020.7
79,427,AO3.5
80,586,412.1
I,681,218,434.0
1,8:i6.1
1,824.3
't,850.2
s8,557.3
102.33
r00.53
103.44
2,1/18.83
11.0
10.9
1',t.1
230.1
486
4trt
490
10.211
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
! = lnvalid
M = Maintenance
Report Generated:. 04/ t4l 23 L7.40
GP043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Contrcl
Page 198 of 278
Average Data - High Flow Run 5
P|ant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period : Ml 1 412023 1 1 : 48 Through O4l 1 41 2023 12:08
Time Online Criteria: 'l minute(s)
Source
Paremd6r
(Unit)
01111123 11:18 23.469 1 1.0 79,738,943.5 1,831 .7 103.31 4&t
UN]T2
BARPRESS
(rNHG)
c02
(PCr)
FLOWSGFH
(scFH)
STKFLOW
(KSCFM)
ST}CTEMP
(DEGF)
UNITLOAD
(MW)
ut14t23 11:49 23.449 11.0 80.053.396.8 1,839.4 103.113
Ml11t23 l'l:50 10.9 80,117,524.0 1,841.8 't03.71 /t&i
ul14t23 11:51 23.89 10.9 80,208,702.5 1,W.1 103.76 42
0414t23 11:52 80,'135,535.4 1,841.5 103.52 442
ut1u23 11:53 23.,169 r0.9 80.344.157.0 1,U6.4 103.52 tt83
ul1u23 1 1:54 80,738,088.5 1,855.4
04,t14123 11:55 23.468 t0.9 80.w)7.222.0 1,860.4 103.41 rl85
o4t1u23 1 1:56 23.468 80,791,101.8 1,856.4
ut14t23 11:57 23.$7 t0.9 80,451,131.2 1,848.6 103.42 rt86
04t14t23 1 1:58 23.157 80,411,289.0 1,848.3 103.58
o1111123 ll:59 23..+66 10.9 80,200,520.9 1,U4.3 1Gi.85 486
ut14t23 12:00 23.467 10.8 80,633,428.3 1,8*.7 103.96 i[86
ut11ti23 l2:01 81,096,194.6 1,865.1
ut11ti23 a.$7 10.8 41,M7,719.1 1,863.2 103.67 486
44t14t23 12:O3 n.&8 t0.8 81.134.788.3 1,865.2 103.65 '+86
o4t14123 81,182,447.3 1,866.9
ut11t23 12tO5 23.4A7 10.8 81,060.800.0 1,864.8 10'1.00 483
ut14123 12:OA 23.447 81,076,368.2 1,864.7 103.91 82
ut11123 12:O7 23.468 't0.8 80.1't 1.067.7 1,843.1 104.13 .t8O
Ul11l23 '12:08 23.488 10.8 80,313,965.8 1,847.8 104.08 479
Awraoe
Minimum
Marmum
Summalion
lnclud€d Data
D^inla
Total nufi$ar of
n.tr P^lnlc
23.448
23.466
23.469
152-421
10.9
10.8
I 1.0
224.2
1,852.1
1,831.7
1,866.9
38,893.4
103.69
103.31
104.13
2,177.57
&
479
$7
10,r63
80,562,616.2
79,738,948.5
a1J82,447 .3
1,691,814,940.2
21
21
21
21
21
21
21
?1
21
21
2',1
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Maintenance
Report Generated: O4lL4l23 l2:t0
GP043AS-0227 22-Rf - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 199 of 278
Average Data - High Flow Run 6
Plant HUNTINGTON PI-ANT
!nterval: 1 Minute
Type: Block
Report Period: 0/.l'1412023 12:22Through 0411412023 12:42
Time Online Criteria: 1 minute(s)
Sorrce
Ptrdneter
(Unit)
Ul14l23 12:22
UNIT2
t,AItPREl;S
(lNHG)
cQz
(PCr)
FLOWSUFTI
(scFH)
S I KFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(trrw)
23.471 0.8 t.443.652 1,472
ul'1423 23.471 10.8 80,890,817.8 1,861.4 10/..26 ,181
ul|1123 12:24 23.470 48110!..2710.8 80,7114,003.8 I,857.9
Ul14l23 12:25 10.8 81,032,812.5 1,863.8 104,.02 €0
04t14123 l2:24 23.470 10.8 81,168,781.5 1,866.3 103.83 475
ut11123 r0.712:27 23.469 80,901,917.8 1,860.7 103.S6 479
ut14t23 l2:28 23.4A7 10.7 81,029.538.4 |,863.7 103.96 o9
ut142?12:29 23.4dt 10.8 79,997,044.6 1,837.0 103.03 475
ut1u23 12:3O 23.469 10.8 79.477.636.4 1,821.1 101.95 479
Ul14l23 12:31 23.470 10.8 80,101,83t.1 1,834.8 10r.69 179
ul14n3 23.4@ 10.8 80.318,A27.2 1,839.1 1 01.rts 479
ut1u23 l2:33 23./168 '10.8 80,005,018.7 1,U4.4 10'1.0s
ut11n3 80,159,805.6 1,833.6 100.88 175
04114123 12i35 23.4e7 10.8 80.017.576.6 1,830.4
04t14t23 1234 23.87 80,046,836.5 1,831.6 101.04 477
o4t14t23 12i37 23..[88 10.8 80,030,589.0 1.830.1 100.71
o4t14t23 12:38 n.s7 80,005,8{xr.8 1,428.4 100.36 475
ut14t23 12:39 23.465 10.8 80,01 t,280.4 1.828.1 100.18
04,t14tz3 l2i4O 23.405 80,029,500.3 .Al1,828.4 100.14
ut11t23 12:41 23.405 10.9 79,909,998.7 r.826.9 100.5't 42
ut14t23 12i42 23.445 80,083,173.1 1,832.3 100.94 482
Awrage
Minimum
Ma)dmum
Summation
lnduded Data
9^idr
Total number of
nqtr 9^ihl.
23.468
23.$5
23.471
492.427
80,381,574.5
79,477,636.4
81,443,652.8
1,688,013,065.0
1,U2.5
1,421.4
1,872.9
3E,693.2
102.05
100.14
10/..27
2,143.10
10.8
10.7
10.9
228.9
479
475
82
10,064
21
21
21
21
21
21
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated: O4lt4l23 12:45
GP043AS-0227 22-Rr -L298
C = Calibration
S = Substituted
T = Out Of Control
Page 200 of 278
Average Data - High Flow Run 7
Plant: HUNTINGTON PLANT
lnterval: 1 Minute
Type: Block
Report Period: 0/,1141202312:59 Through 0411412023 13:19
Time Online Criteria: 1 minute(s)
Source
Parameter
(Unit)
Ul14l23 12i59
UNIT2
BARPRESS
(rNHG)
co2
(PCr)
FLOWSCFH
(scFH)
STKFLOW
(KSCFM)
STKTEMP
(DEGF)
UNITLOAD
(MW
1
Ul11l2t 13:00 79,737,302.5 1,835.5
04,11./23 13:01 10.7 79,8e1,047.3 1,838.7
Unlng 13:02 79,842,811.8 1,836.9
o4t't4l?3 13:03 79,757,795.8 r,834.2
Ul14l23 '13:04 79,856,060.2 1,836.8
Ul14l23 13:05 79.639.729.1 1,831.9
Ul14l2? 13:06 79,910,241.7 1,837.7 103.85
Unlng 13:07 80,247,040.6 1,845.3 103_82
Ul14l23 13:08 80,036,269.3 1,84{r.6
Ml14l23 13:09 80,104,064.0 1,842.3
Ul14l23 '13:10 80,370,882.1 1.8/.4.4 1m.91
01111123 l3:l'l 80,861,237.9 1,859.4
O1l14li23 13i12 10.8 80,20,651.3 1,858.2 104.14
0411423 13:13 80,385,542.9 1,850.1 104.38
o4111t23 13..11 80,3/+8,152.0 1,8118.6
04114123 13:15 80,740,318.8 t,856.8 103.99 481
ul11l23 13:16 81,345,824.3 1,870.9
Ul14l23 13:17 81.,189.'t 30.0 1,873.9 104.r0 479
Ul14lB 13:18 81.1143.068.4 r,873.3 10/..14
Ul1$lB 13:19 81,035,376.5 1,W.7
A\rera0e
Minimum
Maximum
Summation
lncludsd Data
P^inl.
Total number of
nd. P^inte
23.488
23.&
23.171
492.8i!6
21
21
10.8
10.7
10.8
226.1
21
21
80,358,714.7
79.639.729.1
81,409,130.0
1.687.533.638.1
1,848.5
1,83'r.9
1,873.9
38,819.0
21
2',1
104.06
103.82
'104.51
2,'.t85.26
179
475
&
10,060
21
21
21
21
I
F = Unit Offline
E = Exceedance
| = lnvalid
M = Maintenance
Report Generated: O411,4123 73:25
G P043AS-0227 22-RT - L298
C = Calibration
S = Substituted
T = Out Of Control
Page 201 of 278
Average Data - High Flow Run 8
PIanT HUNTINGTON PTANT
lnterval: 1 Minute
Type: Block
Report Period: 04,1141202313:32 Through 0411412023 13:52
Time Online Criteria: 1 minute(s)
Source
Paramder
(Unit)
Ul11l1l3 13:32
UN]T2
tsAKlJKE55
(NHG)
vQz
(PCr)
FL(,WUUTN
(scFH)
u I
^FLr.rw(KSCFM)
UIAIEMT
(DEGF)
UNI I L[,AU
(MW)
1 175
ut14t23 13:33 23.476 10.7 80,865,438.9 1,852.8 102.00 480
ut14t123 13:U 23.475 't0.8 80,981,656.4 1,855.4 101.98 481
04t14t't23 13:35 23.47e 10.8 81,365,953.6 1,863.7 r 0't.82
ut14t23 13:36 23.474 10.8 81,327 ,592.7 r,862.7 101.75 483
o1111t23 13:37 81,793,468.9 1,871.3 101.20
un4t23 13:38 23.474 /l8o10.8 81.241.786.4 1,858.8 101.09
ut11li23 13:39 80,928,126.9 1,851.4 101.13
ut14t23 13:40 23.477 10.8 81,008,630.2 1,8![.4 101.54 €5
ut11t23 13:41 80,454,260.9 1,U5.4 102.62
ut11/23 13:42 23.478 10.7 80,286,292.8 1,846.0 104.04 483
04t1423 '13:.13 81,(xt2,t19.0 1,865.3 1il.60
ut14t23 13:44 23.482 10.6 81.510.273.1 1,875.6 10{..;t lt80
o1t11ti23 13:45 81,737,358.3 '1,880.7 10/..19
041111i23 t3:46 23.42 10.6 81,363,786.7 1,872.2 104.54 477
o4t14t23 13:47 81,011,873.8 1,8n.3 '101.37
04t14t23 13:tl8 8.$1 10.6 81,568,918.5 '1,875.5 104.08 477
utl4tzi 13:49 23.80 10.7 80,'159,579.9 '1,w.5
04t11t23 l3:50 10.7 81,028,188.6 1,855.7 '10't.84 476
un4n3 13:51 23.lao 10.7 81,179,775.7 1,858.4 101..42 475
ut't4t23 13:52 10.8 81,134,860.8 1,856.5 10't.35 476
Av€rag6
Minimum
Mardmum
Summatlon
lnduded Data
P^iht.
Total nuflrber of
nih H^ta
23.47A
23.474
23.482
4S3.045
81,1r14,153.1
9o,28e,2s2.8
8r,793,468.9
1,7U,O27,215.2
1,861.0
't,84/1.5
1,880.7
39,080.6
102.@
101.09
104.60
2,1il.65
21
2',1
10.7
10.6
10.8
225.O
480
475
486
10,090
21
21
21
2'l
21
2',
21
21
21
21
F = Unit Offline
E = Exceedance
| = Invalid
M = Maintenance
Report Generated:- O4l 14123 L3:54
G P04 3AS -0 2 27 22-R1 - t29 I
C = Calibration
S = Substituted
T = Out Of Contro!
Page 202 of 278
Average Data - High Flow Run 9
Plant: HUNTINGTON PI-ANT
lnterval: 1 Minute
Type: Block
Report Period : Ml 1 41 2023 1 4: 07 Through 041 1 41 2023 1 4:27
Time Online Criteria: 1 minute(s)
Sorrce
Param€ter
(Unit)
04114123 14:Ol
UNTT2
BARPRESS
(INHG)
coz
(PCT)
FLIJWl'UF]1
(scFH)
st Kt-Lgw
(KScFM)
5I KI EMt'
(DEGF)
UNITLOAD
(MW)
25.188 10.7 81,351,654.6 1 485
04114123 14:08 80,992,609.0 1M.17
Ul'14123 14:09 81,045,373.4 1,8{t3.5 104.30
Uh4ng 14:10 10.7 81,115,rc3.4 1,865.0
Ul14l23 11:11 81,174,455.8 104.30
Ul14l23 14:'12 't0.7 80,853,800.5 1,859.0
04111123 14:13 80,768,092.7 1,857.3
ut11t23 11..11 10.7 80.866.828.9
Ul14l23 11:15 80,743,571.2 1,857.2
Ul11li23 '14:16 10.7 80.542.888.5
Ul1M23 14:17 80,660,805.0 1,855.1
Ul11n3 14:18 80.831.578.7 1,858.5 10/..22 171
An14n3 14:19 23.487 10.7 80,728,549.5
utfin3 1+20 10.7 80.8q!.903.4 1,858.5 175
0411123 '14:21 r0.7 80,8/t9.33'1.9 '1,858.6 10/..17
04t14123 11:22 10.7 80,398,475.2 1,W.2
Ul14l23 14:23 10.7 80,550,352.0 1,851.3 101.14
Ml14l23 14:24 10.7 81.243.664.9 1.866.6 103.97
04t14123 14i25 10.7 81,626,090.6 1,875.2
o4t14123 11..26 10.7 81,717,980.1
ut14l23 14:27 10.7 81,954,139.7
A\rerag€
Minimum
Maimum
Summation
lncludod Data
B^lnte
Total number of
nalr P^i^l.
23.489
23.87
23.493
193.211
1,&2.0
1,848.2
1,883.5
39,101.8
21
21
't0/..21
103.91
104.49
2,188.50
21
21
10.7
10.6
10.7
221.5
80.994.292.8
80,398,475.2
81,954,1 39.7
1,700,880,149.6
47A
474
485
10,048
2',1
2'.1
21
21
21
21
21
21
F = Unit Offline
E = Exceedance
I = lnvalid
M = Malntenance
Report Generate * 04 I L4/ 23 74t3O
G P043AS-0227 22-RT - L298
C = Calibration
S = Substltuted
T = Out Of C,ontrol
Page 203 of 278
Appendix 8.2.3
Gas RATAs
G P043AS -02 27 22 -RT - L298 Page 204 of 278
Average Data - Gas€s Run 1
PLntHINTiIGTONPI NTIt nd: I llili.
TtDc: RolREr F!.lod: ofi i{rlEl (,*m TtrTlr. or{m CrlEif, 1
Lr
H
M@ OS
I
i'ri
,i
il
i
ll
I
il
.\
i
I
riii
I
l
Itt
ll
rj
Page 205 of 278
3.sl&dnlnd
Mrtiihilt-
T.oilt OtG.ffil
. rtu?ad
U .3a.tt9
i.Ftffiq/l.A!
GP043 AS-O227 22- RT- 1 298
Average Data - Gases Run 1
Plant: HUNTINGTON PLANT
lnteMli 1 Minute
TyPe: Roll
Repod Perid 0ry142023 09:08 Throuqh 0411412023 09.46
Time Onlire Cateria: I minde(s)
29r 3
F = Unlt offline
E = Excacdenca
C = GllbEtion
S = Subsrituted
T = Out OI ContEl
U = St.frup
Repod Generat&: 04/14l23
GPO43 AS -0227 22-RT- 1298 Page 206 of 278
I
l
Average Data - Gases Run 2
PImt HUNTD,IGTON PI.T},IT
ht nf,l: I Mruir
Typ.: RoI
R.Oo.i Pdlo.r: O{r1@(An lC@ Tlrq5h 04n{/28 tO20
Tlrc OrliE Crlt..L l madtc{.)
H
BA toil i$: o@ to.a L)s.7 qo! d.!
17a |fra.l
k@s-!*ff&bdd@ffi
1E,,
d1
94.5
0.0t7
ao
il,i,rt0I
rJrr!
24@t
21
!14,
(aJ
tlel
21
21
21
{0.1
4ror
{&,
to.a7,,a
n
a
10,
!0,5
lol
o€a
0.62
q2G
!.62
o@o
o.sa
q6
lt-a
t.2
{t
F. Unli Oill&r
E. badana
C. otbr.do.r
S. Sui.tltftd
MriLlrmM
T. Od O, CottEl
. . &[pct
u.sffi4irytffis/la/rt
GP0,43 AS-0227 22-RT- 1298 Page 2O7 ol 278
1i
l
Average Data - Gases Run 3
Phil: HUNTtr{OTON PLTNTmml: t Mnut
Ret Pldod: Ogl42@
$D
ffi
W
r.!6,7 082 6 1.t%.2
M6 !0:4 d_a 6 48.!
4fi2i
a$@ &t
Ifu $2
hdi
ffi 4tu1
IMhM d
ld,rfudh 2r
o.@
o,@
o.o3
{a
rta
ilae
1,N
21
q&
qxe
oa
5.6
117t
10.1
16.4
tht
M,5
A
i
0B
tofr
ou
,r
ot
11J
@!
21
a1
G
{&a
1ff.4!
21
rqa
rot
462
F r Unli Ollllm
E. Enaadrro
C, c.ftodo
t.lcb.dnrd
m. ithbi.E
T.oln Of Cctul
..sutlact
U . Sbdupi@(ffiddA4/al
GPO 43 t!s.- 0227 22-RT- I 298 Page 208 of 278
rl
rl
rl
Average Data - Gases Run 4
PITnt IIUNTNGTON PI.A}.IThrnd: I Unlic
Typ.: Rol
Rrpo.t P..tod: Oilrl.t/Z@3 1 1:12 ThBDh Oarl/in(El, 11:3a
t minlc(.)
H
M@ t1l2
2(l o 4ar3t
ri
h@FEffiShryd@@
ks @2
tu la-2
kM 6.0
ffi lt&a
o071
ola6
1&!
1 t,0
10e
ti,l
&t
lllt
!at
tar!
2.gzt
l,@t.a
azl
h,47.1
oa2
o.&
o217
r@a
t6.t
Iil.1
1!aa
N.1
,,@9
N
u
@2
&
t0,2fi ru,*l
F.UntOmlm
E. Eroadano
C. oltr.do.r
3r3$.dttd
M.t.lnt um
T. oc olcon6l
. . sup.d
U.smp
isG..gdoa^a/rr
GP0,43 AS-0227 22- RT- 1 298 Page 209 of 278
il
t,
Average Data - Gases Run 5
Phnt: HUMtr{GToN Put{T
lnlcnd: 'l Minut
Typ.: Rol
Rrpo( Prrlod: olrliu:IE! 1t:ilSThroqrh O{r14i2023 l20t
Tlm dD clltih , mlillC.)
---EA---iini-
i
tot 1aa 6.1
rol 1,al t,@a o^a rru s.4 06 4,0 & 4&,4
roa rora r,Ma o.2rl iGo s0 qs ar a1a 4u,7
ri! ozt r,6r, o.22t llze &a @ N 4, 4s,0
7b2 !U3 MS afrt 2.3t3.7 6.740 tg 8t tqt6 i@t3.1
0a
0.1n
qad
Mq lprll
Ifu qi
ffi l.5al-7
l
ir
F .l&tt Omlm
E. Ee.d.m
C ' c.lbEillo
S. S{b.dmd
}l.lblltmo
t rOd OlGoffil
. . SurIact
U. SEtuD
ipn Gdd qhal23
GP043AS-022722-RT- 1298
l
1l
l
Page 210 of 278
I
Average Data - Gases Run 6
a.ilHUNTINGTONP! ilTlil.nd: 1 llnut
Typr: Rdl
R*o|l Pr.lod: Ot 1,l2lz, lz2,ftucnhm,!.al7,,z3 1242
Tkru Odlm Cdt ria 1 mlillc(.)
W
WM 12:2
re
-oE-
4a 4&1,e
7sJ qrs t0, \nt 1!D.1.u;i2i12:{__ffio,_-_.-.gn_-...ior.r
o.rro ror 1o.4 1,02,7 O.U 111.7 N,a 0.6 2tt a7a 4a6n
oa ro, aa,, t,m7 o21f t@o d.l oN 1a2 05 {70'
o,6a ro,a 1$., 1,14a O& 1!47 31!.r OSa 6t & @r
457 h@ 2Sa UtO.o a.@ 2,4a a1@2 is 472 tO,& to1,u46
N @\J
lfu82
5lE i,i$!
ffin 17,2U,7
21
21
A
d
x
aA
2121^A
71
n
21
^21
2121
a1
Page 211 of 278
F . Unlt Olrllm
E. ho.d.no
C. Oltodo.!
3.S{t irud
M.lihh.mo
T. Oe Ol ContEl.. Su.pd
U.$ep
iaonffids^4nl
GP04;AS-O22722-RT-1298
Average Data - Gases Run 7
Plrnt HUNTI{GITON PLAl.lYhtrd: I tiilnut
T!rc: Rol
Rlport P.dod: 01rl,U:IE3 1259 Tlm.nh Oar14il023 1 3 1 9
Tkm dF CdHr I mlnlIc(.)
W
w@ Lfr rlo.a
110.7 5&.1 0.M 2S U {61.'
@.2
-o7--- iiir--o.ffi-""' '--iil, - -''" --
o2fr r0r da r,@1J oa rr$ ii!! o@ aj fr {s.a
0.10 loJ r!1, t.Gr a6 110., &a 0.6 n7 45 474-2
0.4 toi o., ,,!1!J d& fi6. lir o@ 217 M 151.7
6.S A.1 \&7t b,^6 ltu 2,$.2 6.@a 1370 4t! lo,M idS.O
@ LAI'
h tu!
h 4.4
ffi Atdi
lffihM 21
idnr&dB 21
21
71
v
z21
A
21
a121
a1
,
21
a1
2121
21
a1
PaOe zLZ ol 278
F . Unlt Oflllm
E.M.no
C. c.Xhrd6
S. Suhted
M. ir.lrt mno
T . oln Of C.ntDl
t t Surp.d
U. Sbttpiqn6ffi6/142!
GW43 tts-0227 22-RT- 1298
I
I
Average Data - Gases Run I
Plut HUNThIGTON Pll lT[rt{d: I tlnut!
TyD.: Roll
R.Fo.l Pdod: OdrliarIES 13:32 Tt{qr0h 01/1{/2023 1*52
?lmOdlBCdbria I minit (.)
Uil
M@ llro l,@r.e 0217 io t7d t,to.l d,s 11a,r !11.2 o.G 6.t il a.iaat
1,17f .O 08 iO! * @ 2.1 & {t&!
1,@a oal f 40 mt od xt oa 4n2t
r,taa! 0aa1 ris ,raa o@ aa & 4s7t
23,aaa,a 40 16, a,&j !,8 d,9 loom $11a_6
1$.4
11.t
3J6L'
21
roa
Aw U,r Or&
tu @a ott!
h 1,2{a Oa
ltuhh 21
Tdlfudb 21
i 21
71
21
21
2t
2i
21
A /
Page 213 of 278
F. Unh Oflllm
E. Er6d.E
C- C.hidm
S. Sut tltrd
L'u.hr.E
Tr Ost OtCoffil
t r 3uPart
U.Sbfupisfr6dd6{Arnt
GPo,4irs-022722-RT-1298
Average Data - Gases Run 9
PLnt Ht i{TNGToN n cNInard: I tlnlia
TyD.:
R.p..t Pa.bd: 01rli9l@E NlffiL127
W
o.dt fi(1 4a q6 41 a?a 4t10i
0.d li2l ste 06 a-! 4a 47&n
o,1t firl $.6 @7t al a& L?1f,
4& a47,6 6,n0 rg 514 10!4 td,o1a.t
10, i&a t.tti3
lot itit t,&t
rq7 472 r,r4tl
ks 1.@.4 Od
il[fu li.a O,t{
blu l.&l [97
21
,1
i
21
d
n
d
21
i
a
A
Page 214 ol 278
F r Unlt Otlf,o.
E. BacdaE
C. c.ltidoi
3.srrbrdEd
UrhhEE
T.OdOtGfrl
. . $dpart
U.Snfupl?onffidsaa/la
GW43 AS - 0227 22-RT- 1 298
Appendix C
Quality Assurance/Quality Control
G P04 3AS - 0 2 27 22-RT - 1298 Page 2LS of 278
Appendix C.1
Units and Abbreviations
G P04 3AS -0 22 7 22 -RT - t298 Page 2L6 of 278
d!..i\ l+?.N,r+gp.E-
UNITS AND ABBREVIATIONS
@Xoh 02 corrected to X% oxygen (corrected for dilution air)
lCCl absolute value of the confidence coefficient
ldl absolute value of the mean differencesoC degrees CelsiusoF degrees FahrenheitoR degrees Rankine
" HzO inches of water column
13.6 specific gravity of mercury
AH pressure drop across orifice meter, inches H2O
AP velocity head of stack gas, inches H2O
0 total sampling time, minutespg microgram
9a density of acetone, mg/ml
Pw density of water, 0.9982 g/ml or 0.002201 lb/ml
acfm actual cubic feet of gas per minute at stack conditions
An cross-sectional area of nozzle, t(
As cross-sectional area of stack, square feet (ftz)
Btu British thermal unit
B*. proportion by volume of water vapor in gas stream
C" particulate matter concentration in stack gas, gr/acf
Cnvs average unadjusted gas concentration, ppmv
Cot, measured concentration of calibration gas, ppmv
cf or ft3 cubic feet
cfm cubic feet per minute
Ccr. 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
Crun 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
C, particulate matter concentration in stack gas, gr/dscf
CS calibration span, % or ppmv
Cs measured concentration of calibration gas, ppmv
Cv manufactured certified concentration of calibration gas, ppmv
D drift assessment, % of spandcf dry cubic feet
dcm dry cubic meters
Dn diameter of nozzle, inches
Ds diameter of stack, inches
dscf dry standard cubic feetdscftn dry standard cubic feet per minute
dscm dry standard cubic meters
Fd F-factor, dscf/MMBtu of heat input
frm feet per minute
fos feet per secondft feet( square feet
gram
gallonsgr grains (7000 grains per pound)gr/dscf grains per dry standard cubic feet
s
gal
hr
G P04 3AS -02 27 22- RT - t29 I Page 217 of 278
6/.l\ l*?.N,T+gLH
UNITS AND ABBREVIATIONS
I percent of isokinetic sampling
in inch
k kilo or thousand (metric units, multiply by 103;
K kelvin (temperature)I Ks conversion factor 0.0154 gr/mg
l& conversion factor 0.002668 ((in. Hgxftr)y((mlx'R))
kg kilogram
q pitot tube constant (85.49 fUsec)
kwscfh thousand wet standard cubic feet per hour
I liters
lb/hr pounds per houri lb/MMBtu pounds per million Btu
lpm liters per minute
m meter or milli
M thousand (English units) or mega (million, metric units)
m3 cubic meters
ma mass of residue of acetone after evaporation, mg
Md molecular weight of stack gas; dry basis, lb/lb-mole
meq milliequivalent
mg milligram
Mg megagram (106 grams)
min minute
ml or mL milliliter
mm millimeter
MM million (English units)
MMBtu/hr million Btu per hour
mn total amount of particulate matter collected, mg
mol mole
mol. wt. or MW molecularweight
Ms molecular weight of stack gas; wet basis, lb/lb-mole
MW molecular weight or megawatt
n number of data points
ng nanogram
nm nanometer
Po", barometric pressure, inches Hg
pg picogram
Ps stack static pressure, inches H2O
Pm 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 basis
Ps absolute stack gas pressure, inches Hg
psi pounds per square inchpsia pounds per square inch absolutepsig pounds per square inch gauge
Psto standard absolute pressure, 29.92 inches Hg
Q" volumetric flow rate, actual conditions, acfin
Q" volumetric flow rate, standard conditions, scfin
Qsto volumetric flow rate, dry standard conditions, dscfrn
R ideal gas constant 21.85 ((in. Hg) (ft3)y("R) (tbmote))
G P04 3AS -02 27 22-RT - L298 Page 218 of 278
64\ f,l?.N,T+gp.E
UNITS AND ABBREVIATIONS
SBnna post-run system bias check, % of span
SBi pre-run system bias check, % ofspan
scf standard cubic feetscft standard cubic feet per hourscfin standard cubic feet per minutescm standard cubic metersscmh standard cubic meters per hoursec second
sf, sq. ft., ord square feet
std standardt metric ton (1000 kg)
T o.szs t-value
Ta absolute average ambient temperature, "R (+459.67 for English)
Tm absolute average dry gas meter temperature, oR (+459.67 for English)
ton ort ton = 2000 pounds
tph ortons/hr tons per hour
tpy or tons/yr tons per year
T. absolute average stack gas meter temperature, oR (+459.67 for English)
T",o absolute temperature at standard conditions
V volt
% volume of acetone blank, ml
Vaw volume of acetone used in wash, ml
V" total volume HrO collected in impingers and silica gel, grams
Vm volume of gas sampled through dry gas meter, ft'
Vm(std) volume of gas measured by the dry gas meter, corrected to standard conditions, dscfVm stack gas volume sampled, acf
V" volume collected at stack conditions through nozzle, acf
% average stack gas velocig, feet per second
Vwqstol volume of water vapor condensed, corrected to standard conditions, scf
V*i("to) volume of water vapor in gas sampled from impingers, scf
Vwsslstol volume of water vapor in gas sampled from silica gel, scf
W watt
Wa weight of residue in acetone wash, mg
W,p total weight of impingers, grams
Wss total weight of silica gel, grams
Y dry gas meter calibration factor, dimensionless
G P043AS-0 2 2 7 22-Rr - L29 I Page 219 of 278
64\ lY"{?N,I+gp.H
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
cro
CVAAS
De
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
atom ic absorption spectroscopy
air contaminant discharge permit
analyzer calibration error, percent of span
absolute difference
above detection limit
Air Emissions Testing Body
applicable standard (emission limit)
American Society For Testing And Materials
best achievable control technology
below detection limit
brake horsepower
boiler and industrial furnace
black liquor solids
confidence coefficient
calibration drift
calibration error
continuous emissions monitor
continuous 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-pdioxins (pcdd's)
detection level limited
dilute non-condensable gas
electron capture detector
Engineer ln Training
electoconductivity detector (hall detector)
estimated maxim um possible concentration
US Environmental Protection Agency
Electric Power Research lnstitute
emission standard (applicable limit)
electrostatic precipitator
emission unit
fluid catalytic cracking unit
flue gas desulfurization
flame ionization
fl ame ionization analyzer
flame ionization detector
fl ame photometric detector
fi lterable particulate matter
Fourier-transform infrared spectroscopy
fleld train proof blank
field train recovery blank
polychlorinated dibenzofurans (pcdfs)
gas chromatography
G P04 3AS -0 2 27 22 -RT - 7298 Page 220 of 278
A/i\ MONTROSE
v .t At R quALtTY SERVtCES
ACRONYMS
GC/MS gas chromatography/mass spectroscopyGFAAS graphite furnace atomic absorption spectroscopyGFC gas filter correlationGHG greenhouse gas
HAP hazardous air pollutant
HC hydrocarbonsHHV higher heating valueHPLC high performance liquid chromatographyHRGC/HRMS high-resolution gas chromatography/high-resolution mass spectroscopyHRSG heat recovery steam generator
lC ion chromatographyICAP inductively-coupled argon plasmographyICPCR ion chromatography with a post-column reactorICP-MS inductively coupled plasma-mass spectroscopylR infrared radiationISO lnternational Standards OrganizationkW kilowattsLFG landfill gas
LHV lower heating valueLPG liquified petroleum gasMACT 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 ForAirAnd Steam lmprovementNCG non-condensable gases
ND not detectedNDIR non-dispersive infraredNESHAP National Emissions Standards For Hazardous Air PollutantsNG natural gas
NIOSH 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 hydrocarlconsPCB polychlorinated biphenyl compoundsPCWP plywood and composite wood products
PE Professional EngineerPFAS per- and polyfluoroalkyl substances (PFAS)Pl photoionization
PID photoionization detectorPM particulate matter
PMro 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
G P04 3AS -0 22 7 22-Rr - L298 Page 22L of 278
64\ lt?N,I+gp.H
ACRONYMS
QA/QC quality assurance and quality control
Ql Qualified lndividual
QSTI Qualified Source Testing lndividual
RA relative accuracy
RAA relative accuracy audit
RACT reasonably available control technology
RATA relative accuracy test audit
RCTO rotary concentrator thermal oxidizer
RICE stationary reciprocating intemal combustion engine
RM reference method
RTO regenerative thermal oxidizer
SAM sulfuric acid mist
SCD sulfur chemiluminescent detector
SCR selective catalytic reduction system
SD standard deviation
Semi-VOST semivolatile organic compounds sample train
SRM standard reference material
TAP toxic air pollutant
TBD to be determined
TCA thermal conductivity analyzerTCD thermal conductivity detector
TGNENMOC total gaseous non-ethane non-methane organic compoundsTGNMOC total gaseous non-methane organic compoundsTGOC total gaseous organic compoundsTHC total hydrocarbons
TIC tentatively identified compoundTO thermal oxidizerTO toxic organic (as in EPA Method TO-15)TPM total particulate matter
TSP total suspended particulate matter
TTE temporary total enclosure
ULSD ultra-low sulfur diesel
UV ultraviolet radiation rangeVE visible emisslons
VOC volatile organic compoundsVOST volatile organic sample trainWC water column
\M /TP waste water treatment plant
G P04 3AS -02 27 22-Rr - L29 I Page 222 of 278
Se
Soz
Soe
SO,
TCDD
TCDF
TGOC
THC
TI
TRS
Zn
Ag
As
Ba
Be
c
CI:
clo2
co
Co
Coz
Cr
Cu
H2
Hzo
N2
NH.
Ni
NO
Noz
NO,
o2
6 l,l?N,I+p"p.H
silver
arsenic
barium
beryllium
carbon
Cd cadmium
CdS cadmium sulfide
CH2O formaldehyde
CH3CHO acetaldehyde
CH3OH methanol
CHr methane
C2H4O ethylene oxide
CzHs ethane
CaH4O acrolein
CaH6O propionaldehyde
CgHs propane
CoHsOH phenol
chlorine
chlorine dioxide
carbon monoxide
cobalt
carbon dioxide
chromium
copper
EtO ethylene oxide
EIOH ethyl alcohol (ethanol)
hydrogen
\i/ater
Hzoz hydrogen peroxide
HzS hydrogen sulfide
H2SO4 sulfuric acid
HCI hydrogen chlorideHg mercuryIPA isopropyl alcoholMDI methylene diphyenyl diisocyanate
MeCl2 methylene chloride
MEK methyl ethyl ketone
MeOH methanolMn manganese
nitrogen
ammonia
nickel
nitric oxide
nitrogen dioxide
nitrogen oxides
orygen
P phosphorus
Pb leadPCDD polychlorinated dibenzo-pdioxinsPCDF polychlorinated dibenzofurans
antimony
CHEMICAL NOMENCLATURE
selenium
sulfur dioxide
sulfur trioxide
sulfur oxides
tetrachlorodibenzodioxin
tetrachlorodibenzofu ran
total gaseous organic concentration
total hydrocarbons
thallium
total reduced sulfur compounds
zinc
G P043AS -02 27 22-RT - t298 Page 223 of 278
Appendix C.2
Manual Test Method QA/QC Data
G P04 3AS -02 27 22-RT - L29 I Page 224 of 278
Quality Sowce Sanpling Slstens & Accessoies
February 6,2023
Mr. Alex Webster
Montrose Air Quality Services, LLC'
990 West43d Avenue
Denver, CO 8021
Subject S/N S2G0117 Calibrated Type'S" Pitot
Dear Mr. Webster,
This report presents the results of a calibration performed on the Type S pitot (S/N S2G0117) on
February 6,2023, at Environmental Supply Company's wind tunnel in Durham, North Carolina. Attached
to this report are tables that present the measurement data and the probe coefficient. Also attached is
the latest EPA wind tunnel audit report. The calibration summary is presented in Table 1.
The calibration procedures and acceptance requirements were based on the specifications in Method 2G.
The Type S pitot was placed in the wind tunnel at 0' pitch with the impact port pointed directly into the
flow. Both the A side and B sade were calibrated. The pitot was calibratecl at nominalwind tunnel velocity
settings of 60 fr/sec and 90 fi/sec. Three repetitions were performed at each velocity setting. For each
repetition, a calibration coefficient (Cp) was calculated using the fullowing equation:
\Mrere:
cp=c.n 7*'-_ uF@il
I *r,,_
= TyPe S pitot coefficient,
= calibration Pitot tube coefftcient,
= velocity pressure form the calibration Pitot tube, and
= velocity pressure from the Type S Pitot.
Table l. Type S Pitot Galibration Reeults
Type S Pitot l.D.Galibration
Goefficient
Reference Scrlbe Line
Rotational Offset, ReLo
s2G0117 0.838 Side A - 1.20
s2G0117 0.824 Side B - 1.20
A yaw angle calibration procedure was also perbrmed in the wind tunnel to determine the rotational
position,oi the reference scribe line relative to the probe's yaw-null position. As prescribed in Method 2G,
the digital inclinometer was aligned and locked on the probe's reference scribe line. Positioned at the
Cp
cpr*l
APao
APpmm
708 E. Club Blvd., Durham, North Carolina 27704
GP043AS-0227 22-RT - L298
919-956-9688 EAX: 919-682-0333
Page 225 of 278
www.e,nvironsupply.com
fuality Soure Sonpling Slstens &Accessories
February 6,2023
Mr. Alex Webster
Montrose Air Quality Services, LLC
990 West 43d Avenue
Denver, CO 80211
Subject S/N S2G0133 Calibrated Type "S" Pitot
Dear Mr. Webster,
This report presents the results of a calibration performed on the Type S pitot (S/N S2G0133) on
February 6,2023, at EnvironmentalSupply Company'swind tunnelin Durham, North Carolina. Attached
to this report are tables that present the measurement data and the probe coefficient. Also attached is
the latest EPA wind tunnel audit report. The calibration summary is presented in Table 1.
The calibration procedures and acceptance requirements were based on the specifications in Method 2G.
The Type S pitot was placed in the wind tunnel at 0' pitch with the impact port pointed directly into the
flow. Both the A side and B side were calibrated. The pitot was calibrated at nominal wind tunnel velocity
settings of 60 fUsec and g0 ft/sec. Three repetitions were performed at each velocity setting. For each
repetition, a calibration coefficient (Cp) was calculated using the following equation:
\Mtere:
9p
Cpt*ot
APao
APpooe
Type S pitot coefficient,
calibration Pitot tube coefficient,
velocity pressure form the calibration Pitot tube, and
velocity pressure from the Type S Pitot.
Table 1. Type S Pitot Calibration Reeults
Type S Pitot l.D.Calibration
Coefficient
Reference Scrlbe Llne
Rotational Offset, Rsr-o
s2G0133 0.804 Side A - 3.30
s2G0133 0.816 Side B - 3.30
A yaw angle calibration procedure was also performed in the wind tunnel to determine the rotational
position of the reference scribe line relative to the probe's yaw-null position. As prescribed in Method 2G,
the digital inclinometer was aligned and locked on the probe's reference scribe line. Positioned at the
708 E. Club Blvd", Drhao, North Camlina 27704
G P04 3AS -0 2 2 7 22 -RT - L29 I
919-956-9688 EAX: 919{824333
Page 226 of 278
www.environzupply.com
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice,
Leak Check, and Thermocouple Calibration Check
English Meter Box Units, English K' Factor
(dz 0.9783
AH@:'t.820
Meter Box Orifice Calibration
IMPORTANT Forv.ld !n G6ub. tu tulv.dffi *uE b 1 b 2 an. Hg tr .brtun S. tuomtelCdtc.lV.cuum &M.&v6
IMPoRTANT tu ctulotu Co.ffd.( K. Nh.ruGd n EnCish un6. (frf3'(d.g R)t.t((in.H9)'(dn)).
- SNPLE ME - - DRYGAS METER -
-
ORIFICE- - ORYGAS METER-
INDICATEDVS,ACTUA VOLUME VOLUME VOLUME CfuEMNON FACTOR
CORRECTED CORRECED NOMINA Yd
For C.libmbn F.6r Y. S. n& of h r..din0 oth. c.libnton dbr b h. dry g.! mbr.
.€pb* Mnnd of idivito.lv.ls.toh ft. rv.mg. i. +rc.02.
For Otr6 C.lih&n F.tur AHO tu odfo dftDffil pr.ero in inch.. of H20 S.t .qu.bs b 0.75 fr ot .[
ilA F.d A.P hd.r of Hg, .opbbb d.Erc. of individu.lv.lu.! tum 6..v.ES i! +rc.2.
ta 5ao
tuIy op.n, fin. Bdjudtufly do$d, sel. inl.t dw.d
b 2610 (mu di.ldH.b 1 minub)
Metor Box Prersure Leak Check Meter Box Vacuum Leak Check
ileter Box Thormocouplo Readout Calibration Check
'R..ding vilu.. md b 6in 1.5% of Etolrc tummb val63 (&{d on abdd b@E!6 dh)br dlbEton b h.e.phbb
hpd High
120
ll
12 334 62
sc 20 aao 920
Th.mo6upl..hqhto,
GP043E 022722 RT 1298
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice: PostTest,
English Meter Box Units, English K' Factor
Current Cal. Yd: 0.9783
Post-test Yd:0.9701
Post-test Result:PASS
Meter Box Orifice Calibration
IMPORTANT Forvalid tosi resulis, the Adu6l V.cuum should bo 1 lo2 in. H9 grod6rSen h€ Th6or6tical Cdtical Vacuum shwn abov€
IMPORTANT Tho Criical Orifice Coeffcient, K', musi bo .nl6r6d in English unfrs, (n)^3'(d6g Rf0.5((in.H9)'(min)).
For C.libdion Fador Y, ba relio otSo r.ading ofhe calibEton met€r to th6 dry 9a! metsr,
acc6pbbl6tobranco otindtoidu.l valus! tom S€ aveBge is +rc.02.
ForOdiceCalibr.tonFadorAH@ th.otrc.dftrentalprcssuroininche.ofH20thatequatesto0.T5chotai
rt68 F and 8.92 inchos olH9, accopt.bletobEnce otindMidu.l v.lu6s fom h. rveEge is +rc.2.
Meter Box Vacuum Leak Check
Coarse adjusl vev6 fully opcn, fin. adjust tully clos.d, iamplc inld ptrgged
IVust bezero (motordial stablo br 1 minde)
Meter box posllesl calibra{on fom (oriic6) R3
GPg3S-O22722-RT-1298
,\{()N ll(()\l
EPA Method 5
Meter Box Calibration by Calibrated Critical Orifice,
Leak Check, and Thermocouple Calibration Check
English Meter Box Units, English K Factor
Yd:0.9995
AH@:1.721
tt.61 in. Hg
Metor Box Orifice Celibration
IMPORTANT For vllld t.d n.uli, lh. Adul Va@um .hu6 & 1 to 2 h. Ht Cr.li.rfr.n h. fteor.iial Cdidl V.cuum.hown.bov.
IMPORTANT Th. C.nid onfra Co.&nl K. mB b.nl.,.d in Engil$ uh[., (n)rl(d.g R)t.5/((in.Bg).(mln)).
4.322
For C{lb[ilon frdor Y, lh. 6lio ot th. Erdlry of h. olllbdbn m.t r lo the dry F. m.t.r,
.@pi.!. lobEnc. ollndtoidu.lv.lu.6 lbm th..v.6g. l. +/{.02.
For Onfr@ C.libdbn F.dorAH@, th. odfic. dltr r.nii.l F..&E h inch..orHAhrt.qutc.to o.75ch or.r
.l 66 F rnd 29.Y hchiiorHg, ldpl.bh tol.En6 olindtrldurlv.lu..tumttu.vcng. i. +rc.2.
d
oa 64.0 &
63,0 s.0 701 9 17_0
250 TO
Moter Box Pressure Leak Check Meter Box Vacuum Leak Check
..i u., nn n'u,hnt:b. z.ro (mrnom.l.r l.v.l sabh br I Fnur.)
24 E &iud v.h. tui, oFh. fin. .diud tuty do*d. smpL inl.t pl{O.d
hz.ro (m.l.r did drm tur I mind.)
Meter Box Thormocouplo Readout Galibration Check
rhlrudDL rhuhtd
' R..dlng v!|u.. mud & dhl. l.5A ol r.bnr th.mom.i.r v.lu.. (hsd on lholur. r.mp.rarur. Hh) lor crllbillbn lo [e-mail].
lnpd Hr9h
7
6a
11
/oa 7
TETHOD 5 CRMCAL ORIFEE CALIBRANOT
' cRnicALoEFrcdSArrn:@!
lT] ' f;-T-il
-
@l *l '',ol_J t I rr I rr I lrr. l LI0!r1_LIlr.d.-zro
l;l'l '-l-"-l , , [,",.*.l-*l .'.'
l_J ! I r3 I i. ll4J l,lo.rulrrrr0 Ic!.t
L;l ,T;-ril _ @l-i*"l ,,,.
l_J r I 16 | $ lllLl lrrrrul[t.r.!lt"!rr
l;l ' fTfrll - IluETE-i,IT .,..
t-J t I r! | r! r rzrrl lffiiTffi-l rru
ttmllcclElmla.I tnmnmC&l-4.ffi hd-f-h$bo(Idbrld.fir.jdcht 0(l*lore, Y,'if, [refr hlJ8PA[U6.ttr ruOr...q&alq,dan Fdrarffi ndtfr aao
aora
aLa
!o.0t
a0.,at
,1,,
70rc
,0,ta
TUat
,!.c0
TUta
0rl0'0.t !t 4.7!tE{a
0,aaA,0t tir l,rarE{4
0.ll'O 0.240t 2.t0lE{a
lc . ffildilloolllcbltt,
t(rtf$9tfi(,LHcxmln.lt - EnslLh unlb
I0nmlcK)ull,t(mm Hcxmh.)t - t nb{tbl! unnr
I(mt)fKltz}lr(mm Hel(mtn.lt . x.Hc Unll,
{rt
o0i
o0a
4,04
O0,l
arl
ora
{.ta
{.fi
o.ll
IT-'l , T--m-'l t-iililTi.*il-t e-[J , I r.Til-l l-ilsl FffiT6'rr-l rco
Envlfimu Sl.oty Co,, fE . ?u E cL eld, orLr!, IC 27roa
GPo 43 A5 -0227 22-RT.1 298
. el96C$l - fr.Gtonrrpply.d cGiz't.
Page 230 of 278
*'*[=l
a-t a,NJ i.,
la ac.r g ae-,c,
J.i
gft aa.t aa.t 0.t 1n2
aD ml tuu n! il
at ,0.1 mil ?G!mc
d-t mt nt ha ht
o_c t/,oa 19'.tqa
i
CI ru [! ha ,11
EI It at ,l aLa
Appendix C.3
Instrumental Test Method QA/QC Data
G P043AS-0227 22-RT - t298 Page 23L ot 278
Appendix C.3.1
Unit 1
G P04 3AS-0 227 22-RT - L298 Page 232 of 278
PROI-O22722
PacifiCorp
Huntington Unit 1
4lL3 - 411412023
Gas
Coz
co
Level
Low
Mid
High
Low
Mid
High
Low
Mid
High
Low
Mid
High
Soz
Calibration Error Tests System Calibration Error
Gas
Value
Analyzer Calibration
Error
0.0%
L.5/o
-o.2%
-0.2%
'0.3Yo
O.LYo
o.o%
o.9%
1.L%
0.2%
!.OYo
0.s%
Analyzer
Response
System
Cal Error
o.o%
o.0%
O.OYo
O.Oo/o
0.OYo
0.0%
0.0%
o.o%
0
8.93
t7.94
0
26.51
61.94
0
153.8
332.3
0
150.9
333.8
0
9.2
17.9
-0.1
26.3
62
0.1
L56.7
335.8
o.t
154.3
335.5
0
9.2
-0.1
26.3
0.1
t56.7
o.7
154.3
<5% or
t 0.5 ppm
G P04 3AS -0 2 2 7 22 - RT - 129 I Page 233 of 278
PROt422722
PaclflCorp
lluntlnSton unlt 1
4lL3 - 4lr4l2o2a
Level
Low
Mid
High
Low
Mid
High
Low
Mid
High
Low
Mid
High
Gas
Cor
NOr
Error
0.6%
o.4%
0.8%
0.o%
0.2%
0.9%
0.r%
0.7%
0.8%
0.3%
1.8%
o.l%
Gas Analyzer System
Value Resoonse Cal Errof
0 I 0 I-0.6%
8.93 1910.0%
0 I -1 lO.O/o
151 I155.9 I0.0%
GP043AS-0227 22-RT - t298 Page 234 of 278
Dridtrrr4 tp.-p'Ed.DdiE*
lnthl Pdol htd
olaE hm
iun @n
sls TiR
HLt hot td todd MId
Runhnjh
s@ TIn.
rntLl Md
t&
toibi& 2t
Page 235 of 278GP043 AS-O227 22-RT- 1 298
t
bTitu lqlt
ild I hilr hor hTd
GPO 43 AS - 0227 22-RT- 1298 Page 236 of 278
'l"ime
4/L3/23 5:32:37
4lL3l23 5:32:47
4/L3123 5:32:57
4h31235:33:07
4l13/23 5:33:t7
4/13123 5:33:27
4lL3l23 5:33:37
4lL3l23 5:33:47
4/13/23 5:33:57
4/13/23 s:34:07
4lt3/23 534:17
4/13/23 5:34:27
4/13123 5:34:37
4lt3/23 5:34:47
4/13123 5:34:57
4/13/23 5:35:07
4lL3l23 5:35:17
4113123 5:35:27
4lL3/23 5:35:37
4lr3l23 5:35:47
4l13/23 5:35:57
4/13/23 5:36:07
4h3/235:36:77
4/t3/23 5:36:27
4/L3/23 5:36:37
4/L3/23 5:36:47
4l13/23 5:36:57
4l13/23 5:37:0"1
4lL3/23 5:37:17
4/L3123 5:37127
4/L3/23 5:37:37
4lL3l23 5:37:47
4lL3l23 5:37:57
4/L3/23 5:38:O7
4l13/23 5:38:17
4/L3/23 s:38:27
4lL3l23 5:38:37
4lL3l23 5:38:47
4/L3123 5:38:57
4ll3l23 5:39:07
4/t3/23 5:39:17
4/13/23 5139:27
4/13123 5:39:37
4/13123 5:39:47
4/t3123 5:39:57
4lt3l23 5:40:07
4h3123 5:4O:L7
4/13123 5:40:27
4/13/23 5:40:37
4/L3123 5:40:47
4lL3l23 5:40:57
4lL3/23 5:4L:07
4/13/23 5:4L:L7
4/13/23 5:4L:27
4/L3/23 5:4L:37
4/L3/23 5:4L:47
4h3123 5:4L:57
4/L3/23 5:42:07
4h3/23 5:42:t7
4/13/23 5:42t27
4/L3123 5:42:37
4lL3/23 5:42:47
4lL3l23 5:42:57
4/L3/23 5:43:07
4lL3l23 5:43:77
4lL3l23 5:43:27
4lL3/23 5:43:37
4/13/23 5:43:47
4lL3l23 5143:57
4/13/23 5:44:07
4h31235:44:tl
4lt3/23 5:44:27
NOx
o.1 7.1
0.1 0.5
0.3 0.4
0.1 -0.4
0,1 -0.3
0.4 -0.3
0.4 0.7
0.3 1.8
0.2 2.2
0.7 1.6
1.1 L.2
0.7 0.9
0.6 0.3
0.5 0.5
0.4 0.9
0.8 0.8
0.8 -0.2
0.9 -0.5
0.7 -1.0
0.8 -0.s
0.6 0.3
0.5 0.6
0.4 0.2
0.4 0.5
0.4 0.2
0.5 -0.1
0.4 -0.9
0.6 -1.8
0.5 -2.3
0.3 -2.7
0.5 -2.8
0.5 -3.3
0.9 -3.6
0.8 -s.0
0.3 -4.8
0.8 -4.5
0.8 -4.0
0.5 -3.8
0.8 -3.6
0.8 -3.s
0.5 -3.4
o.4 -3.5
0.5 -3.3
1.0 -3.6
r.2 -3.4
0.9 -3.0
0.5 -2.9
0.3 -2.9
0.6 0.4
109.4 22.L
245.9 73.4
279.4 741.3
2a7.2 220.2
29r.0 269.4
294.7 293.4
319.8 300.3
337.6 301.1
332.1 300.9
329.3 307.7
333.1 302.2
331.8 302.8
331.4 302.8
334.5 302.8
334.8 305.6
335.1 334.0
335.0 333.8
335.3 334.2
335.3 334.7
335.7 334.8
336.1 335.r
336.6 335.0
336,6 335.6
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
-0.1
0.0
0.0
0.0
0.0
-0.1
0.0
0.0
0.0
0.0
0.0
-0.1
0.0
0.6
3.0
7.9
13.1
15.1
L7.4
17.9
18.0
18.0
18.1
18.1
17.9
17.9
17.9
t7.9
17.9
18.0
18.1
18.0
18.1
18.1
18.1
18.2
18.1
13.9
7.4
2.5
0.6
o.2
o.2
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
-0.1.
0.0
0.1
-0.1
-0.2
-0.2
0.0
-0.1
-0.1
-0.3
-0.1
0.0
-0.2
0.1
-0.2
-0.2
0.0
{.1
4.2
0.2
-0.1
-0.3
-o.2
-0.2
0.0
0.3
-0.1
-0.2
0.1
-0.1
-0.2
-0.3
-0.2
-0.2
-o.2
-0.1
-0.1
-0.3
-0.1
-0.1
-0.1
0.1
-0.2
-0.2
-0.1
-0.2
-0.1
-0.3
0.3
0.3
0.8
1.1
r.4
1.4
r.4
r.4
!.7
11
1.5
1.7
t.7
1.8
L.7
1.8
1.6
L.7
!.7
1..8
1.8
2.0
1.8
I
G P043AS-0227 22-RT - t298 Page 237 of 278
Time
4/t3/23 5:44:37
4l13l23 5:44:47
4/L3/23 5:44:57
4h3/235:45:07
4/13/23 5:45:17
4h3/235:45:2?
4113/23 5:45:37
4lL3l23 5:45:47
4/!3/23 5:45:57
4/t3123 5:46:07
4h3/235:46:t7
4/t3/23 5:46:27
4/L3/23 5:46:37
4/13/23 5:46:47
4lt3/23 5:46:57
4h31235:47:07
4lt3/23 5:47:17
4lL3/23 5:47:27
4h3/235:47:37
4l13/23 5:47:47
4lL3/23 5:47:57
4h3/235:48:07
4/L3123 5:48:17
4/t3/23 5:48:27
4/L3/23 5:48:37
4ll3l23 5:48:47
4h3/23 5:48:57
4/L3123 5:49:07
4/L3123 5:49:r7
4lr3l23 5:49127
4/L3123 5:49:37
4lt3/23 5:49:47
4lL3/23 5:49:57
4/t3123 5:5A:A7
4/L3/23 5:50:L7
4lL3l23 5:50:27
4/13/23 5:5ot37
4lL3l23 5:50:47
4lt3/23 s:s0:s7
4/L3/23 5:5r:07
4lL3/23 5:5L:17
4lL3l23 5:51:27
4lL3/23 5:5t:37
4lt3l23 5:5L:47
4/73123 5:5r:57
4h31235:52:07
4/13/23 5:52:17
4/!3/235:52:27
4h31235:52:37
4/131235:52:47
4/B/23s:s2:57
4lt3/23 5153:07
4113123 5:53:17
4/L3/23 5:53:27
4/t3/23 s:s3:37
4/13/23 5:53:47
4/L3/23 5:53:57
41L31235:54:A7
4h3123 5:54:17
4/13/23 5:54:27
4lL3l23 5:54:37
4lt3/23 5:54:47
4l13/23 5:54:57
4lL3l23 5:55:07
4lt3l23 5:55:77
4h31235:55:27
4/13123 5:55:37
4/13/23 5:55:47
4173173 5:55:57
4h31235:56:07
4/t3/23 5:56:t7
4/L31235:56:27
5O2 NOx CO
7.7 335.5 335.5
1.8 337.1 136.7
1.9 337.6 337.1
1.6 337.4 338.2
1.5 337.3 337.2
1.8 332.7 332.7
4.3 325.9 310.7
13.1 195.8 255.6
25.5 36.4 174.5
37.4 4.2 92.5
44.7 3.4 38.0
49.1 3.0 11.0
51.5 2.5 2.9
53.3 2.5 L.2
54.7 2.2 0.6
55.9 1.9 0.1
s6.1 2.0 -0.s
56.1 Z.L -0.7
s6.6 1.9 -0.6
57.1 ?.L 0.6
57.r 1.8 1.6
59.6 7.6 0.9
6,..7 1.8 -0.3
61.9 1.6 -0.8
61.9 1.8 -0.1
62.0 1.9 0.9
61.9 1.9 L.2
62.3 1.8 1.0
62.L L.6 1.0
62.0 1.5 -0.6
61.5 1.8 -1.1
61.8 t.7 -0.9
62.L 1.8 -0.3
62.3 1.9 0.3
62.4 1.8 0.5
52.2 1.9 0.1
6L.2 L.7 -0.8
54.2 1.5 -2.O
41.8 L.2 -2.8
27.2 0.9 -3.1
16.8 1.0 -3.7
10.3 1.1 -3.8
6.6 1.1 -3.3
3.9 1.0 -2.7
2.9 1.0 -2.7
1.8 0.9 -3.0
L.4 0.9 -4.2
r.2 1.0 -4.2
1.1 L.2 -4.0
0.5 1.1. -3.8
0.7 0.9 -3.7
0.4 1.0 -3.8
0.4 1.0 -3.7
0.6 L.2 -4.t
0.5 1.1 -4.8
o.2 1.0 -4.8
o.2 0.9 -4.3
0.2 t.2 -3.3
L.2 L.2 -3.0
4.3 L.2 -3.2
9.5 1.1 -3.0
15.1 1.1 -2.9
19.5 1.1 -2.9
21.8 L.2 -2.r
23.0 1.1 -1.5
23.9 0.9 -1.2
24.7 1.1 -r.7
25.3 L.2 -1.6
25.6 1.1 -!.4
25.6 1.1 -1.2
25.9 1.0 -r.2
26.3 1.2 -1.1
co2
0.0
0.0
0.0
0.0
0.0
0.1
0.2
0.2
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
1.3
3.8
7.3
9.1
9.2
9.3
9.3
9-3
9.2
9.2
9.2
9.2
9.2
9.2
9.2
9.2
9.2
9.2
9.1
9.1
9.1
8.9
6.6
3.3
1.0
0.1
0.0
0.0
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
G P043AS - 0 22 7 22- Rr - L298 Page 238 of 278
Time
4/L31235:56:37
4lL3l23 5:56:47
4lL3l23 s:s6t57
4/B/235:57:07
4lBl23 5:57:L7
41L31235:57:27
ah3/23s:57:37
4l13/23 5:57:a7
4lL3l23 5:57:57
4/L3/23 s:s8:o7
4lL3l23 5:58:L7
41131235:58:27
alBl235:s8:37
4/13/23 5:58:47
4lr3l23 5:58157
4/L3123 5:59:07
a/B/235:59:L7
4lr3l23 5:s9:27
4lL3/23 s:59:37
4lL3l23 5:59:47
4l13/235:59:57
4/t31236:@:07
41L31236:0O:L7
4/,-31236:@:27
co2
-0.1
-0.1
-0.1
-0.1
{.1
{.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.2
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
so2
26.1
26.4
25.6
26.4
26.t
25.s
25.5
26.7
26.L
26.3
26.4
26.3
26.3
25.s
2r.3
15.6
10.1
6.9
4.5
1.2
2.5
1.9
1.9
1.6
NOx
1.0
1.1
1.0
1.3
0.5
0.8
0.9
1.1
1.0
1.0
0.8
1.1
L.r
50.4
111.5
136.5
L52.5
156.0
156.3
155.5
156.7
155.7
156.8
156.8
co
-0.9
-1.0
{.5
-0.3
-0.4
-0.9
-]..2
-!.2
-0.1
0.0
0.2
-0.5
0.2
5.1
25.0
s9.9
100.0
130.6
145.6
\53.2
154.5
154,3
154.0
154.3
G P043AS-0 22 7 22-Rr - L298 Page 239 of 278
'l-ime
4lL3/23 6:55:47
4h3/236:ss:s7
4/L3/23 6:56:07
4lt3l23 6:s6:r7
4lL3l23 6:s5:27
4/L3123 5:56:37
4h3123 6:56:47
4lBl23 6:56157
4h3/23 6:57:07
4h3123 6:57:17
4/13123 6:57:27
4lL3l23 6:57137
4h3/23 6:57:47
4h3123 6:s7:s7
41L31236:s8:07
4h3123 6:58117
41131236.58t27
4lt3/236:58:37
4lt3l23 6:58147
4lt3/23 6:58:57
4113123 6:59107
4/13123 6:59:!7
4113123 6:59:27
4lt3l23 6:59t37
4113123 6:59:47
4173123 6:59:57
4/13/23 7:00:07
41L31237:0O:L7
4/L31237:00:27
4lL3l?37:00:37
4l13/237:00:47
41L31737:00:57
4lL3/237:01:07
4/L3/237:07:L7
41L31237:Ol:27
4/L3/237:0r:37
4/L31237:01:47
4/L3/237:01:57
4l13l23 7:02:07
41Ll1237:O2:L7
4/t31237:02:27
41L31237:02:37
4/L3/237:02:47
41t31237:02:57
4lL3/237:03:07
4l13l23 7:O3:r7
41L31237:03:27
4lL3l23 7t03i37
4lt3l23 7:O3:47
4l!3/21 7:03:57
4lL3/23 7:04:07
4lt3/237:04:!7
4lt3l?3 7tO4:27
4lt3l23 7:04:37
coz so2 NOx co
-0.1
-0.1
-0.1
.0.1
.o.t
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
0.3
2.0
5.0
8.1
9.2
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.4
9.3
9.3
9.3
9.4
0.8 150.2 159.4
0.8 150.4 159,4
0.6 150.6 159.3
0.5 160.8 159.4
0.9 150.5 159.4
0.7 160.5 150.1
0.8 160.4 159.9
o.7 160.6 158.7
0.7 160.4 158.3
0.9 160.2 157.8
0.9 160.2 158.5
0.6 160.5 158.9
0.9 160.6 159.1
0.6 L60.7 1s8.5
1.2 128.9 L53.7
3.9 89.7 135.6
8.9 50.0 t04.2
14.6 10.4 fl.o
19.3 1.9 30.5
22.0 1.5 11.3
24.r L.6 4.0
24.5 1.0 1.6
25.5 L.2 0.8
2s.7 0.8 0.8
26.7 0.8 0.7
26.3 0.7 1.0
26.5 1.1 1.0
27.0 1.2 0.7
26.8 0.7 0.7
26,6 0.7 0.2
26.9 0.8 0.0
26.8 1.0 -0.3
27.1 1.0 -0.3
26.9 0.9 0.3
27.O 0.7 0.9
26.6 1.0 1.6
26.9 0.9 1.4
27.0 0.9 1.1
26.0 0.8 0.4
2L.7 1.0 0.1
15.0 0.8 4.4
8.8 0.8 {.5
5.4 0.8 -1.0
3.4 0.9 -2.2
2.2 0.9 -7.4
1.5 0.5 -1.6
1.3 0.5 -1.1
0.7 0.4 -1.8
0.4 0.4 -L.7
0.5 0.6 -1.8
0.3 0.3 -0.7
o.2 0.4 -0.2
o.4 0.4 -0.6
0.3 0.8 -0.9
G P043AS -02 27 22 -RT - L298 Page 240 of 278
Time
4/t31237:30:07
4lL3/23730:17
4/L31237:30:27
4/L3/237:30:37
4/13/237:10:47
4/131237:30:57
41131237:3L:07
4/1312373L:r7
4h31237:31:27
4/t3/2373137
4/131237:31:47
41L312373r:57
4/t3/237:32:07
4lL3l23 7:32:L7
4/L3123 7:32:27
41L31237:32:37
41L31237:32:47
4173123 7:32:57
41731237:33:07
4lt3/237:33:17
41131237:33:27
41t31237:33:37
4h31237:31:47
41L31237:33:57
4h31237:34:07
4h31237:34:L7
41t31237:34:27
41L31237:34:37
41L31237:34:47
4/t3/237:34:57
4lt3/237:35:07
41L31237:35:77
4/L31237:1s:27
41131237:35:37
4l!31237:35:47
4/L31237:35:57
4lL3/237:36:07
4l!31237:36:t7
4h31237:36:27
41131237:36:37
41131237:36:47
4h31237:36:57
4l13/23 7:37:07
4lL3/237:37:L7
41L31237:37:27
4ll3l23 7:37137
4lL3l23 7:37:47
4lL3/237:37:57
41L31237:38:07
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.3
8.1
5.1
2.2
0.5
0.1
0.0
0.0
0.0
0.0
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0,1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
0.0
0.0
0.0
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
0.3 0.2 -1.5
-0.1 0.3 -1.1
0.2 0.0 -0.5
-0.2 0.0 -0.6
0.1 0.4 -1.3
0.0 0.2 -1.8
-0.1 0.5 -1.6
-0.2 0.6 -L.4
-0.2 0.5 -0.8
-0.3 0.4 -0.8
-0.3 0.4 -0.7
7.4 0.5 -1.1
s.8 0.4 -0.9
12.2 0.4 -0.1
r7.4 0.1 0.3
20.6 0.7 -0.3
22.9 0.8 -0.1
24.t 0.6 t.4
25.3 0.5 2.4
2s.8 0.4 2.6
26.1 0.3 2.L
26.3 0.4 1.0
26.s 0.3 0.6
26,2 0.6 1.3
25.8 0.5 2.L
26.2 0.2 2.2
26.4 0.3 2.2
26,7 0.4 2.5
26.6 0.4 2.2
26.6 0.s 2.o
26.2 0.4 1.8
25.7 0.3 1.3
25.5 0.6 r.2
24.4 0.6 6.1
20.7 58.1 24.0
14.8 130.9 56.0
9.8 145.9 93.3
5.1 146.6 727.9
4.6 L52.6 137.8
3.1 152.1 742.9
2.0 L52.9 150.5
1.8 152.2 151.3
L.4 152.1 151.5
1.4 151.8 r5t.7
L.2 151.9 151.3
1.0 151.8 151.3
L.r 152.2 151.4
1.0 152.3 151.5
L.r 152,2 151.5
G P04 3AS -0 227 22-Nr - 129A Page 241 of 278
Time
4h3/23a:L3:27
4lL3/23 8:L3:37
a/B/238:L3:a7
4/131238:L3t57
41L31238:L4:O7
4/L3/238:L4:77
4/L3/238:L4:27
4/L31238:!4:37
4/L3/238:14:47
4/L3/23 8:].4:57
4lL1l23A:15:07
41L31238:751L7
4/L3/23 8:15:27
4/L31238:ts:37
4lr3l23 8:t5:47
41L31238:].5:s7
4lL3/238:76:07
4/13/238:!6:17
4/13/238:],.6:27
4lt3l23 8:76137
4/L3123 8:76:47
4lL3l23 8:16:57
41131238.17t07
4h3/238;!7:77
4/L3123 8:L7:27
4173/23 8:L7:37
a/L3/23 8:77:a7
4h31238:L7:s7
4/13/23 8:L8:07
4lL3/238:18:t7
4h3/238:18:27
41731238:L8:37
41731238:!8:47
4/131238:!8:57
4h3/238:19:07
4lL3l23 8:19:17
4173123 8:79:27
4h31238:79:37
4h31238:19:47
4lr3l23 8:19:57
4/13/238:20:07
4/L31238:20:17
4h31238:20:27
4/].3/238:?0:37
41131238:20:47
4lt3l23 8t2O:57
4lt3l23 8t2L:07
41].31238:2tr7
4/131238:?L:27
4/!3/238:21:37
4lt3l?3 8:21:47
4/731238:2L:s7
4113123 8:22:07
41L31238:22:17
41L31238:22:27
4/L3/238:22:37
4/t3/23 8:22:47
41t31238:22:57
41L31238:23:07
41L31238:23:17
4lL3l23 8:23:27
4/L3/238:23:37
4/L3/23 8:23147
-0.1
-0.1
.{r.1
.{r.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
{.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
-0.1
0.9
3.3
6.4
8.2
8.4
8.5
8.5
8.7
8.7
8.7
8.7
8.7
8.8
8.9
8.9
8.9
8.9
1.5 L47.O 14L.4
1.1 L47.0 143.8
1.0 L46.9 145.1
1.0 146.9 L45.7
0.9 L47.5 145.5
0.8 148.1 L45.4
0.8 147.9 145.5
0.5 147.7 144.9
0.6 148.0 144.s
0.8 147.9 L44.5
0.9 148.0 r45.L
0.5 748.2 145.3
0.9 148.0 145.1
1.0 147.8 L44.3
0.6 148.0 L44.s
0.5 148.3 t42.4
?.6 91.3 130.3
6.6 20.8 104.8
Lz.Z 4.5 69.7
L7.O 1.9 36.4
19.8 1.0 r4.0
2t.s 1.0 3.8
22.4 0.8 !.2
23.4 0.9 0.5
2t.4 0.7 0.7
23.7 1.0 0.8
24.2 0.8 0.8
24.5 0.5 0.1
24.3 0.5 0.1
24.7 0.5 -0.1
25.2 0.5 -0.4
24.8 0.6 -0.4
25.0 0.4 -0.3
24.4 0.4 0.0
24.8 0.3 -0.1
24.4 0.5 4.2
24.8 0.4 0.1
24.6 0.4 0.1
24.5 0.5 0.0
24.6 0.3 -0.9
24.9 0.5 -0.9
24.8 0.7 -0.6
24.7 0.5 0.0
24.7 0.7 -0.2
24.6 0.6 -0.2
zs.r 0.2 -0.7
24.! 2.3 -0.7
20.7 4.1 -0.4
15.3 3.1 0.0
9.5 0.8 -0.8
s.9 0.4 -2.0
3.4 0.7 -2.4
2.4 0.2 -2.L
1.1 0.4 -L.7
1.1 0.3 -L.7
0.5 0.s -2.0
0.4 0.3 -2.7
0.3 0.3 -3.3
0.2 0.4 -2.9
0,2 0.3 -2.O
0.4 0.6 -L.7
0.2 0.5 -3.0
0.3 0.3 -3.8
G P043AS -02 27 22 -RT - L298 Page 242 of 278
Time
4lr3l23 8:50:L7
41L31238:50i27
4l!3123 8:50:37
4h31238:50:47
4/L31238:50:57
4lL3/23 8:5L:07
4/!3/238:sL:I7
4l!31238:st:27
4/!3/23 8:5t:37
4l!3123 8:51:47
4/L31238:51:57
4lL3l23 8:52:07
41L31238:52:77
a/B/238:s2:27
4lL3l23 8:s2:37
4lt3l23 8:52147
4lL3l23 8:52:57
4lL3l23 8:s3:07
4/13123 8:53:17
4h3/238:53:27
4lL3l23 8:53:37
4/131238:53:47
41131238:53:57
4lt3l23 8:s4:07
4lt3l23 8154:t7
4h31238:s4:27
41t31238:54:37
4lt3l23 8:54:47
4lr3/23 8:54:57
4lL3l23 8:55:07
4lt3l23 8:55:L7
4lt3l23 8:55:27
41131238:55:37
4/131238:55:47
4/131238:ss:s7
4h3/238:55:07
4/]-31238:56:t7
4/L3/238:56:27
4/L31238:s6:37
4/L3/238:s6:47
4h31238:56:57
4/L3123 8:57:07
4/13123 8:57:r7
4lt3l23 8:57:27
4/L3/23 8:57:37
4lL3l23 8t57147
4/L3/23 8:57:57
4/13/23 8:58:07
4lBl238:58:t7
4/L3123 8:58:27
4/73/23 8:58:37
8.8
8.8
8.8
8.9
8.9
8.9
8.8
8.8
8.8
7.8
5.2
2.4
0.8
0.3
o.z
0.2
o.2
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2 -4.r
-0.1 0.1 4.4
-0.3 0.3 4.7
0.1 0.0 -4.9
-0.2 0.2 -4.5
-0.2 0.2 -3.2
-0.1 0.1 -2.s
0,0 0.2 -3.8
-0.2 0.0 -5.5
-0.4 -0.1 -6.1
0.0 0.0 -5.7
r.t 0.0 -4.9
4.8 0.2 -3.8
10.9 0.2 -2.7
15.9 0.0 -1.5
19.0 0.1 -1.6
2L.0 0.2 -L.7
22.5 0.1 -2.L
23.! 0.4 -2.5
23.6 -0.1 -2.9
24.0 0.1 -3.0
24.0 0.1 -1.9
24.L 0.1 -L.4
24.7 0.0 -1.1
24.6 0.2 -1.2
24.7 0.1 -1.1
24.7 0.1 -1.O
24.3 0.0 -1.6
24.4 0.1 -1.8
24.7 0.2 -1.6
24.7 0.3 -0.7
24.6 0.4 -0.5
24.6 0.1 -t.7
24.6 0.1 -2.6
24.6 0.5 -2.9
25.O O.3 -3.O
24.8 0.4 -2.9
25.2 0.4 -1.5
23.L 0.4 6.1
19.0 58.4 27.2
13.5 131.s 50.8
8.5 146.7 97.0
5.7 L47.6 L23.6
3.7 147.6 L37.5
2.6 148.0 L4L.6
2.O L47.9 142.9
1.5 148.3 143.3
1.4 148.3 t4.2
7.2 1118.1 L4,.3
1.1 1ll8.3 144.r.
0.9 L47.8 143.7
G P04 3AS -0 2 27 22 -RT - L298 Page 243 oJ 278
Time
4lL3l23 9:2617
4lL3/23 9:26:27
4/t3123 9:25:37
4h31239:26:47
4/L3/23 9:26:57
41L31239:27:Q7
41L31239:27:L7
4h31239:27:27
4h3/239:27:37
41L31239:27:47
41Ll1239:27:57
4lL3/239:28:07
41731239:28:!7
4/131239:28:27
4lt3/23 9:28:37
4/L31239:28:47
4lt3/239:28:57
4i131239:29:07
4/131239:29:t7
41L31239:29:27
41L31239:29:37
a/B/239:29:47
4/L31239:29t57
4/L3123 9:30:07
4lL3l23 9:30:17
4l!3123 9:30:27
4h3/239:30:37
4lL3/23 9:30:47
a/B/239:30:57
4/L31239:3L:O7
4lL3/23 9t3L:t7
4173/23 9:3L:27
4l13l23 9:31:37
4173123 9:31:47
4173123 9:3L:57
41t31239:32:07
4/L31239:32:L7
41L31739:32:27
41L31239:32:37
41L31239:12:47
4/73/239:32:57
4h31239:33:07
4lL3/23 9:33:77
4lt3l23 9:33:27
4173/23 9:33:37
4l13l23 9:33:47
4/L3/23 9:33:57
41131239:34:07
4lL3/23 9:34:L7
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0-1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
1.5
3.9
7.t
8.6
8.8
8.8
8.8
8.8
8.8
8,8
8.8
8.8
8.8
8.8
8.8
8.8
1.0 148.5 7M.5
1.0 1la.9 14s.0
0.5 149.3 145.2
o.7 149.0 145.7
o.7 148.9 t45.7
0.9 149.0 t45.2
0.8 t49.L 1.454
0.7 148.9 t45.4
0.7 L48.7 145.0
0.7 140.4 L42,2
2.3 130.s L30.7
5.5 71.7 105.5
r2.t 15.0 69.s
17.0 1.8 35.3
19.8 1.1 12.5
2L.9 t.2 2.3
23.1 1.0 -L.2
23.6 0.8 -1.5
24.\ 0.8 -1,5
23.9 0.7 {.9
24.5 0.4 -0.2
27.9 0.6 -0.3
24.6 0.6 -0.5
24.7 0.5 -1.8
25.1 0.5 -2.5
24.A 0.3 -3.9
25.2 0.s -4.3
24.8 0.4 -3.3
24.4 0.5 -2.2
25.0 0.5 -1.7
24.8 0.5 -]-.2
24.9 0.4 -7.4
24.9 0.6 -r.7
23.6 3.3 -1.5
20.7 6.7 -1.5
15.1 4.8 -1.8
9.5 1.3 -Z.r
s.7 0.5 -2.8
3.s 0.5 -3.1
2.4 0.5 -3.9
L.4 0.5 -4.3
L.t 0.5 -4.8
0.3 0.5 -4.7
0.s 0.3 -s.3
0.2 0.5 -s.9
0.2 0.6 -5.5
0.3 0.2 -5.2
0.3 0.3 -4.1
0.2 0.3 -3.7
G P043AS-0227 22- RT - L298 Page 244 of 278
Time
41L312370:22:57
4/L3/23 r0:23:O7
4lL3l23 L0:23:t7
4/L3123 10:23:27
4/L3/23 10:23:37
4lL3l23 L0:23:47
4/L3/23 L0:23:57
4/L3/23 L0:24:07
4/L3123 L0t24:17
4lL3l23 L0t24:27
4lr3l23 L0:24:37
4h3123 t0:24:47
4173123 L0:24:57
4lr3l23 t0:25:07
4h3123 L0:25:17
4/t3123 10:25:27
4/13123 L0:25:37
4lL3l23 10:25:47
4lL3l23 70:25:57
4lL3l23 10:26:07
4lL3l23 !0:26:!7
4lL3l23 10:26127
4lL3l23 t0:26137
4lL3l23 t0:26:47
4/L3/23!0:26:57
4/L!23 L0:27:O7
4lt3l23 70t21:17
4lt3l23 70:27:27
4/L3/23 L0:27:37
4lt3l23 70127:47
4lL3l23 70:27:57
4/t3123 r0:28:O7
4lt3l23 70:28:L7
alL3l23 L0:28:27
4lr3l23 L0:28:37
4/13123 rO:28:47
4h3l23 tO:?'8:57
4lr3l23 L0:29:07
4lL3l23 L0:29:r7
4lL3l23 LO:29:27
4h3lz3 L0:29137
4lL3l23 LO:29:47
4/L3123 70:29:57
4h3123 70:30:07
4lL3/23 N:30:t7
4lL3/23 70:30:?7
4ll3l23 10:30:37
4lL3l23 70:30:47
4/t3/23 tO:30:57
4lL3l23 L0:3r:O7
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.8
8.7
7.0
3.9
1.3
0.4
0.2
o.2
0.2
0.2
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.?
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2 0.1 -5.6
0.0 0.2 -s.7
-0.1 0.1 -5.6
0.0 0.1 -5.7
o.2 0.0 -4.8
-0.3 0.2 -4.9
0.0 0.7 -4.9
-0.1 0.2 -5.6
-0.2 0.1 -5.9
-0.2 0.2 -6.4
0.0 0.1 -5.8
-0.1 0.2 -7.2
-0.2 0.0 -6.4
0.3 0.1 -5.5
2.7 0.4 -4.9
7.5 0.4 ,4.8
13.5 0.0 4.6
L7.9 0.1 4.2
20.2 0.4 -3.8
22.0 0.2 4.2
22.8 0.1 {.1
23.4 0.0 -3.2
23.8 0.1 -2.0
24.0 0.3 -2.1
24.7 0.5 -2.0
24.3 0.1 -1.8
24.0 0.4 -2.L
24.7 0.2 .2.5
24.4 0.0 -2.7
24.4 0.1 -r.2
24.5 0.2 -2.5
24.6 0.2 -2.3
24.7 0.4 -1.1
24.6 0.1 -O.7
24.3 0.2 -0.3
25.0 0.0 -0.8
24.8 0.4 -L.Z
24.6 0.3 -L.6
24.2 0.0 0.5
7L.6 58.7 13.9
16.6 132.L 42.5
11.3 !47.6 80.9
7.3 148.6 113.4
5.0 148.8 133.8
3.3 149.0 !42.L
2.7 149.2 1113.6
1.9 149.0 143.2
t.7 t49.2 142.8
1.5 149.1 143.1
L.2 149.5 t42,8
G P04 3AS -0 227 22 -Rr - t29A Page 245 of 278
Time
4lr3l23 tt:4O:Ll
4ll3l2X Lr:4O:27
4l!3123 Ll:40:37
4lL3l23 Lt:40:47
4173123 L!:4o:57
4/!3123 7r:4L:07
4/13123 t!4r:r7
4lL3l23rL:4!:27
4h3123 Lt:4L:37
4lL3l23 L7:4L147
4173123 Lt:4t:57
4lt3l23 LL:42:07
4lL3/23 rL:42:L7
4/L3123 L!:42:77
4lL3l23 LL:42:37
4lL3l23 LL:42:47
4lL3l23 ll:42:57
4lL3l23 Ltt43:07
4ll3l23 LLi4!r7
4lL3l23 LL43:27
4lL3l23 LL:43:37
4h31237L:43:47
4lL3l23 rL:43:57
4/L3123 rL:44:07
4lL3l23 LL:44:r7
4lL3l23 lL:44:27
4173123 7L:44:37
4173/23 LL:M:47
4lL3l23 Ll:44:57
4lL3l23 Lt:45:07
4/L3/23 LL:45:17
4lt3l23 LL:4s:27
4lL3l23 LL:45:37
4h3/23 rL:45:47
4/L3/23 Lt:45:57
4lL3l23 lL:46:07
4h3123 LL:46:r7
4lL3l23 LL:46:27
4lL3l23 t7:46:37
4lL3l23 tL:46147
4/13123 tL:46:s7
4ll3l23 17:47:07
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.8
2.7
5.7
8.2
8.9
8.9
8.9
8.9
9.0
9.0
9.0
9.0
25.4 0.4 4.4
2r.4 0.5 -3.9
25.8 0.3 -3.1
25.5 0.4 -r.2
25.6 0.4 -3.5
25.3 0.3 4.7
26.t 0,5 -5.0
25.8 0.6 -5.3
26.0 0.6 -4.8
25.6 0.7 -4.1
24.3 51.1 2.2
20.5 128.0 22.8
t4.4 145.9 56.9
9.1 150.7 95.4
s.6 152.0 L?3.6
3.8 151.7 138.3
2.8 151.7 143.2
2.2 1s2.0 743.9
2.0 152.1 144.5
1.6 151.9 1.14.3
t.2 152.0 144.8
1.1 152.1 L44..4
1.0 151.8 144.3
L.2 151.9 743.4
L.t 151.9 142.9
1.1 152.0 143.0
0.8 L52.3 143.0
1.0 152.5 143.L
0.8 152.5 t42.9
0.8 151.8 141.4
1.0 92.8 130.1
0.8 L9.7 104.0
0.7 3.8 66.3
0.3 1.8 30.3
0.0 1.3 6.7
0,1 0.8 -3.5
o.2 0.5 -6.6
4,2 0.8 -7.2
-0.1 1.0 -7.8
-0.2 0.8 -8.0
-0.1 0.5 -7.2
G P043AS -02 27 22-RT - L298 Page 246 ot 278
Time
4/t3123 L2t74:27
4lt3l23 L2:r437
4/13/23 L2:L4:47
4l13/23 t2:14:57
4/L3123 12:15:07
4/L3/23 t2:L5:17
4/13/23 72:15:27
4/L3/23 t2:t5:37
4lL3l23 t2:15147
4/L3123 72:L5:57
4/13/23 r2:L6:O7
4lL3l23 r2:L6:17
4/73/23 !2:L6:27
4/L3/23 r2:L6:37
4/t3/23 L2:L5:47
4l13l23 r2:t6:57
4/L3123 l2:L7:07
4h3/2312:L7:L7
4173/23 r2:L7:27
4h3/23 L2t!7:37
4h3123 t2:71:47
4lL3l23 72:77:57
4lL3/23 L2:L8:O7
4lrll23 LZrS:fi
4/L3/23 t2:r8:27
4/t3/23 t2:r837
4lL3/23 72:L8:47
4/13123 12:L8:57
4lL3/23 r2:r9:07
4lL3l23 72:L9:L7
4lL3/23 72:L9:27
4/13/23 r2:L9:37
4ll3l23 t2:L9:47
4/L3123 !2:t9:57
4/13/23 r2:2Q:07
4h3l2312t2OtL7
4/t3123 r2:2o:27
4lL3/23 L2t2O:37
4lt3l23 L2:20:47
4h3123 12:29:57
4h3/23 L2:21:07
4173/23 l2:2t:L7
4lL3/23 L2:2L:27
4/13123 l2:2L:37
4/L3123 t2:2L:47
4lL3l23 L2:2L:57
a/B/23 L2:22:07
4/L3/23 l2:22:L7
4/L3/23 t2:22:27
4/t3/23 12:22:37
4lL3/23 12:22:47
4lL3l23 12:22:57
4ll3l23 12:23:07
4lL3l23 12:23:L'l
4ll3l23 12:23:27
4173123 L2:23:37
4ll3l23 12:23:47
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
8.1
5.5
2.6
0.8
0.3
0.2
0.2
0.2
0.2
o.2
0.1
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.3
0.3
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
L.4 0.4 -7.2
0.9 0.6 -7.8
0.6 0.3 -8.2
0.3 0.5 -8.0
0.3 0.s -6.6
0.1 0,3 -6.3
0.1 0.3 -6.1
0.2 0.2 -7.0
0.0 0.1 -6.8
0.0 0.2 -7.6
-0.3 0.1 -7.9
-o.2 0.4 -8.1
-0.3 0.4 -8.7
0.0 0.2 -8.8
0.1 0-3 -8.4
-0.1 0.1 -5.5
0.0 57.6 L.2
0.2 129.8 23.3
0.2 146.9 58.5
0.4 1s0.3 96.9
0.3 151.3 1239
0.4 151.5 t37.2
0.8 151.5 t4t.7
0.7 151.5 141.8
0.5 151.6 L42.2
0.6 1s2.0 143.0
0.7 151.8 L44.7
0.5 151.8 L44.9
0.9 L51.7 L44.5
0.9 151.5 143.6
1.1 151.6 L42.7
1.1 151.7 143.3
0.6 151.8 L44.0
0.7 151.6 L43.5
0.7 151.0 L42.9
r.7 150.8 136.0
5.3 91.0 115.5
L0.7 17 3 82.7
t6.2 2.0 44.6
19.9 L.2 15.9
21.5 1.0 1.9
22.8 0.9 -3.1
23.5 0.8 -4.9
24.2 0.7 -5.4
24.s 0.9 -5.5
24.5 0.6 -s.6
25.0 0.3 -5.1
25.r 0.5 -3.9
25.5 0.5 -3.1
25.1 O.4 -3.1
25.4 0.5 -3.9
24.7 0.7 -3.8
25.L 0.4 -3.9
25.L 0.4 4.0
25.3 0.5 -4,L
2s.2 0.6 4.3
25.1, O.1 4.4
G P043AS-0 2 2 7 22 -RT - t298 Page247 of 278
Time
4lL4/23 5:44:33
4h4/235:44:43
4/t4/23 5:44:53
4h4/23s:4s:03
4/t4/23 5:45:13
4/L4/23 5:45:23
4lL4l23 5:45:33
4h4/235:45:43
4/74/23 5:45:53
4/74/23 5:46:03
4h4/235:46:13
4/!4123 5:46:23
4/14/23 5:46:33
4/14/23 5:46:43
4h4/235:46:53
4174123 5:47:03
4/]4123 5:47:L3
4114123 5:47:23
4/74/23 5:47:33
4174/23 5:47:43
4l14/23 5:47:53
4/14/23 5:48:03
4174/23s:48:L3
4lt4/23 5:48:23
4l14l23 5:48:33
4/14123 5:48:43
4lL4lZ3 5:48:53
4/L4123 5:49:03
4lL4/23 5:49:13
4/L4/23 5:49:23
4/L4/23 5:49:33
4lt4/23 5:49:43
4/14/23 5:49:53
4/74/23 5:5O:O3
4/14lZ3 5:50:t3
4h41235:50:23
4h4/235:50:33
4h4/235:50:43
4/14/23 5:50:53
4/14/23 5:51:03
4174/23 5:5t:73
4/14/23 5:51:23
4/74/23 5:57:33
4/14/235:5t:43
4l14/23 5:51153
4lt4l23 5:52:03
4lt4/23 5:52:73
4/14/235:52:23
4/L4/23 5:52:33
4/t4/23 5:52:43
4h4/235:52:53
a/M/235153:03
4/14/23 5:53:L3
4l14/23 5:53:23
4/14/235:53:33
4lL4/23 5:53:43
4/L4123 s:s3:s3
4/L4/23 5:54:03
4/L4123 5:54:73
4/L4/23 5:54:23
4/14/23 5:54:33
4lt4l23 5:54:43
4/!4/23 5:54:53
4/74/23 5:55:03
4/r4/23 5:55:13
4174/23 5:55:23
4/74/235:55:33
4/1.4/23 5:55:43
4/14/235:55:53
4/t4/23 5:56:03
4/t4/23 5:56:73
4/L4123 5:56:23
I 1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
1.0
4.7
10.9
16.8
L7.0
L7.3
18.0
17.8
17.9
L7.8
t7.9
17.9
17.9
77.8
L7.8
17.8
17.9
t7.9
17.9
t?.9
13.4
6.6
2.0
0.4
0.3
0.2
0.2
o.2
0.?
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.3
0.3
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
-0.1
0.0
0.0
-0.1
0.0
0.1
-0.3
0.0
0.2
0.0
-0.1
0.0
-o.2
-0.1
0.0
-0.1
0.2
o.2
-0.1
-0.1
0.2
0.0
0.0
0.0
0.0
-0.1
-0.2
-0.1
-0.1
0.1
0.2
-o.2
0.0
-0.3
0.2
0.0
0.3
1.0
1.3
1.5
1.6
1.5
1.4
1.5
1.9
1.8
r.4
t.4
1.8
1.7
1.5
1.5
r.7
1.5
1.8
1.6
1.9
1.9
4.0
L2.4
23.7
36.6
45.3
s0.6
53.7
55.7
56.8
57.5
57.9
58.4
s9.0
-0.2 3.0
0.2 2.0
0.2 -0.8
0.1 -1.1
0.0 -1.0
-0.3 -1.1
-o.2 -L.2
-0.3 -1.5
-0.3 -1.8
-0.2 -2.2
-0.2 -2.2
-0.1 -1.9
-0.4 -0.8
-0.4 -0.2
-0.3 -o.8
-0.3 -7.4
-0.3 -1.3
-0.1 -2.5
-0.1 -3.8
4.2 -4.5
-0.2 -5.0
-0.3 -s.2
0.0 -5.4
-0.1 -5.1
{.1 -5.5
-0.1 -6.8
{.1 -7.2
-0.1 -7.4
-0.2 -6.6
0.0 -5.5
-0.4 -5.1
-o.2 -5.1
-o.2 -5.6
-0.1 -6.5
45.5 -3.0
161.1 22.O
248.7 78.4
292.8 1s8.s
320.0 23r.2
32L.9 277.4
323.3 297.8
323.8 303.8
324.0 305.2
324.5 320.1
324.8 334.0
334.5 333.5
334.7 333.2
335.3 333.1
335.4 333.4
334.9 333.9
334.7 333,8
t34.1 333.1
333.4 333.s
333.3 333.4
333.3 332.9
333.7 332.4
333.7 332.6
333.8 330.4
267.5 307.a
101.5 251.8
2.1 168.2
0.5 87.4
-0.3 32.2
-0.1 7.t
0.0 -0.8
-0.4 -0.8
-0.2 -0.3
-0.2 -0.1
-0.4 0.2
-0.2 -0.4
4.4 -0.8
G P043AS-0227 22-RT - L298 Page 248 of 278
Time
4/L4/23 5:56:33
4l14l23 5:56:43
4lt4/23 5:56:53
4/L4123 5:57:03
4/L4123 5:57:r3
4/14123 5:57t23
4h4/235:57:33
4lL4l23 5:s7:43
4/14123 5:57:53
4/141235:58:03
4/74/23 5:58:L3
4/141235:58:23
4/L4/23 5:58:33
4/L4123 5:58:43
4/L4/23 5:58:53
4lL4l23 5:59:03
4lt4l23 5t59tL3
4lr4l23 5159:23
4lt4l23 5:59:33
4/14/23 5:59:43
4/t4/23 5:59:53
4lt4l23 6:00:03
4/L4123 6:00:L3
4114/23 6:00:23
4114123 6tOO:33
4h41236:00:43
4h4/236:0O:53
4lt4l236:OLO3
4h4/236:01:73
a/14/23 6:0r:23
4lr4l23 6:Ot:33
4h4123 6:0r:43
4/L4/23 6:0t:53
4/L4123 6:02:03
4/t41236:02:L3
4/L4/23 6:02:23
4/L4/23 6:0?:33
4/!41236:02:43
4/L4/23 6:07:53
a/14/23 6:03:03
41L41236:03:73
4/74/23 6:03:23
4/14/23 6:03:33
4/74/23 6:03:43
4/L4123 6:03:53
4/!4/23 6:04:03
4/74/23 6:04:\3
4h41236:04:23
4lt4l23 6:04:33
4lt4l23 6:04:43
4/L4123 6:04:53
4lt4l23 6:05:03
4lL4/?3 6:05:73
4/t4/23 6:05:23
4/14/23 6:05:33
4lL4l23 6:O5t43
4/t4/23 6:05:53
a/L4/23 6:A6:03
4l14/23 6:06:13
4/L4123 6:06:23
4/L4/23 6:06:33
4l14/23 6:06:43
4lL4l23 6:06:53
4/L4/23 6:O7:03
4lt4/23 6:07:13
4lL4l23 6:07:23
4/L4/23 6:07:33
4/L4/23 6:07:43
4/14/23 6:07:s3
4lL4l23 6:08:03
co2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1.
0.3
2.3
5.2
8.6
8.9
8.9
8.9
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.0
9.1
9.1
8.8
5.3
2.4
0.4
0.2
0.2
0.1
0.1
0.1
0.1
0.L
0.1
0.1.
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.L
0.1
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
so2
59.1
58.7
s8.8
59.0
51.8
62.0
62.5
62.6
62.6
62.3
62.7
62.8
62.9
63.2
63.0
62.1
57.0
45.5
31.5
L8.7
11.3
6.6
4.0
2.4
1.8
1.1
0.9
1.1
0.9
0.2
0.3
0.4
0.5
o.4
0.9
1.1
r.2
1.0
1.3
1.1
7.2
1.0
1.0
1.0
0.8
0.9
1.0
!.2
1.0
1.0
1.1
0.9
0.7
0.5
1.0
1.0
1.4
2.8
7.4
13.4
18.8
22.2
23.7
25.0
25.3
26.2
26.?
26.5
26,6
26.3
NOx
-0.2
-0.1
-0.4
-0.1
.0.3
4.4
{.1
-0.2
-0.1
4.2
-0.3
0.0
{.3
4.2
{.3
{.3
-0.3
-0.1
-0.1
0.0
0.0
-0.2
-0.1
-o.2
-0.3
-0.2
-0.2
-0.2
-0.3
-0.2
-0.1
0.0
-0.3
30.4
107.5
154.8
155.4
155.9
156.4
155.5
156.1
156.1
156.1
155.2
156.2
156.0
L56.2
156.3
155.3
L56.2
155.3
155.2
L56.2
155.1
156.2
t44.9
L76.2
78.9
29.2
-0.4
0.0
-0.3
-0.1
-0.1
-o.2
-0.2
-0.2
-0.3
-0.2
-0.1
co
-t.4
-0.7
0.4
0.4
0.0
-0.7
-0.5
-0.1
-0.2
-0.4
-0.5
-0.5
-0.3
-0.1
-0.2
0.8
0.2
-0.2
-1.5
-2.3
-2.3
-2.4
-3.3
-4.8
-4.7
-4.L
-3.0
-2.5
-2.9
-3.6
-3.8
-3.2
-2.5
8.6
34.5
75.2
!L3.2
t34.7
152.7
156.5
157.9
151.2
156.7
756.7
156.9
t57.5
158.2
1s8.3
158.1
157.2
r56.8
L57.3
158.1
157.6
L56.7
L56.2
r48.7
t26.2
89.1
49.2
20.7
5.5
L.4
0.6
-0.4
-0.6
-0.8
-1.1
-0.9
-0.6
G P04 3AS-02 27 22 -RT - L298 Page 249 of 278
Time
4/141236:36:L3
4lL4/236:36:23
4/14/236:36:33
4/14/236:36:43
4/L4/236:36:s3
4/L4/23 6:37:03
4l!4123 6:37:13
4/14/23 6:37:23
4/14123 6:37133
4/74123 6:37:43
4lL4l23 6:37:53
4h4/236:38:03
4174/236:38:13
4/L41236:38:23
a/L4/236:38:33
4/L4123 6:38:43
41141236:38:53
4/74/23 6:39:03
4h4/23 5:39:73
4lL4/23 6:39:23
4lt4/2X 6:39:33
4/l4123 6:39:43
4/L4/23 6:39:53
4/L4123 6:40103
4/L4/23 6:40:73
4/]4123 6:40:23
4h4/735:40:33
4/!4/23 6:40:43
4/L4/236:4O:53
4/L4/236:41:03
4lL4l23 6:47:LJ
4h4/236:47:23
4/L4/236:4133
4/L4123 5:41:43
4/L4123 6:4r:53
4/L4/236:42:01
4/141236:42tL3
4/]41236:42:23
a/M/236:42:33
41],41236:42:43
4/141236:42:53
4lt4l23 5:43:03
4h41236:43:73
4lt4/236:43:23
4l!4/23 6:43:33
4lt4/23 6:43:43
4l14l23 6:43:53
co2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
L.7
4.4
8.2
9.t
9.2
9.2
9.3
9.2
9.2
9.3
9.3
25.9 4.2 -1.3
27.0 {.3 -1.4
27.2 0.0 -0.9
27.2 -0.4 -1.5
27.0 -0.1 -2.2
27.3 -0.3 -L,4
27.! -0.1 -0.4
27.r -0.1 0.4
27.4 -0.s 0.2
27.6 0.0 -0.s
27.2 -0.3 -0.8
27.2 -0,1 -0.9
27.0 -0.1 -0.3
27.3 -0.3 0.0
27.5 4.2 -0.1
27.1 L3.7 0.2
25.7 {9.4 8.7
2L.s 88.7 33.4
15.6 132.4 72.9
9.7 158.2 Lt3.7
5.0 158.9 t4t.7
4.2 159.1 155.3
2.9 159.2 159.0
2.t 159.3 159.9
1.7 158.9 159.6
r.4 159.3 159.9
1.5 159.0 150,1
1.2 159.6 160.0
1.2 159.5 159.1
!.4 159.2 159.2
r.2 159.1 160.1
1.0 159.0 161.5
1.1 159.4 161.8
0.9 159.5 767.2
1.0 159.5 759.4
0.9 138.6 158.7
0.8 87.L 747.1
0.7 44.7 120.3
0.6 L6.2 78.4
0.0 {.3 39.5
0.1 0.0 13.1
0.2 {.1 1.0
0.1 -0.1 -2.0
0.1 -0.3 -2.L
-0.2 -0.1 -2.2
-0.1 {.3 -2.7
-0.1 -0.3 -2.3
G P04 3AS -0 227 22-RT - 1298 Page 250 of 278
Appendix C.3.2
Unit 2
G P043AS -0 227 22-Rr - t298 Page 25L of 278
PRO}-O22722
PaclfiCorp
Huntington Unit 2
41L412023
Gas level
COz Low
Mid
High
SOr Low
Mid
High
ilOr Low
Mid
High
CO Low
Mid
High
<sYo ot
t 0.5 ppm
<2%
Callbratlon Error T$ts SFtem calibratlon Error
Gas
Value
Analyzer C.ellbratlon
Error
0.6%
-0.2/o
4.8/o
0.o%
-0.8%
-o.t%
4.L%
0.o%
o.6%
-0.s%
0.t%
0.t%
Analyzer
Reiponre
System
Cal Error
0.0%
0.o%
0.iYo
0.0%
o.o%
a.o%
0.o%
O.O/o
0
8.93
L7.94
0
26.51
61.94
0
153:.8
332.3
0
150.9
333.8
0.1
8.9
L7.8
0
26
61.9
-0.3
L53.7
314.4
-1-6
L57.4
334
0.1
8.9
0
26
{.3
153.7
-1.6
151.4
G P04SAS-0227 22-R t - L298 Page 252 of 278
rln bd
brh.
st Ed htd hd
.u^t@
rff hd
iu hd
rfl Ed
Ruihnh
mH hot
Page 253 of 279GP043AS-022722-RT-1298
rE
i6M :1stu
fr hd t*.
il
GN 43 PA - 0227 ?z-RT- 1 298 Page 254 of 278
Time
4/t4/23 8:39:24
4/L4/23 8:39:33
4/t4/23 8:39:43
4/74/23 8:39:54
4h4/238:40:04
4/74/23 8:40:13
4l14/23 8:40:23
4/14123 8:40:34
4/L4/23 8:40:44
4/14/23 8:40:53
4/t4/23 8:4L:03
4/14/23 8:4L:14
4/14/23 8:4L:24
4h4/238:4L:33
4/14/23 8:4!:43
4h4/23 8:41:54
4h4123 8:42tO4
4/14/23 8:42:13
4/L4/238:42:24
4/L4/23 8:42:34
4/74/23 8:42:43
4/t4/23 8:42:53
4/14/23 8:43:04
4174/23 8:43:14
4/74/23 8:43:23
4/t4/23 8:43:33
4/L4/238:43:M
4/L4/23 8:43:54
4/t4/23 8:44:03
4/t4/23 8:44:L3
4lt4/238:M:24
4h4/238:M:34
4/14/23 8:44:43
4lt4l23 8:44:53
4/14/23 8:45:04
4/14/23 8t45t74
4/14/23 8:45:23
4/t4/23 8:45:33
4/L4/23 8:45:44
4/L4/23 8:45:54
4h4/238:46:03
4/14/23 a:46:L3
4/14/23 8:46:24
4/t4/23 8:46:34
4114/23 8:46:43
4/14/23 8:46:54
4/L4/23 8:47:O4
4/L4/23 8:47:L3
4/14/23 8:47:23
4/74/23 8:47:34
4/14/23 8:47:44
4/14/23 8:47:53
4lL4l23 8:48:03
4/14123 8:48:t4
4/L4/23 8:48:24
alL4/23 8:48:33
4lL4/23 8:48:43
4/L4/23 8:48:54
4/t4/238:49:04
4/14/238:49:L3
4/74/23 8:49:23
4/14/23a:49:34
4lt4l23 8:49:44
4/14/23 8:49:53
4/14/23 8:5O:O3
4/L4/23 8:5O:r4
4lt4/238:50:24
4/14/23 8:50:33
4/14/23A:5Q:43
4/74/23 8:50:54
4/14/23 8:5r:O4
4/L4/23 8:51:13
-0.1 -0.2
-0.1 -0.5
-o.2 -0.1
0.0 -0.5
0.0 -0,2
-0.1 -0.2
0.0 -0.3
-0.1 -0.3
-0.1 -0.3
0.0 -o.2
0.0 -0.1
-0.2 -0.3
0.1 -o.2
0.1 {.1
-o.z 4.1
-0.2 -0.3
0.0 0.0
-0.1 -0.4
-0.4 0.0
-0.1 -0.3
0.0 4.2
-0.1 -0.4
0.0 4.2
-0.3 -0.1
-0.1 -0.3
-0.1 -0.1
0.1 -0.3
-0.1 -0.3
'0.5 -o.2
-0.1 -0.3
0.2 -0.3
0.1 4.3
0.0 -0.1
-0.? -0.1
-0.2 -0.1
-0.1 -o.2
0.0 -o.2
-0.1 -o.2
-0.1 -0.1
-o.2 -0.3
0.2 4.2
-o.2 4.3
-0.1 0.1
-0.2 -o.2
0.0 -0.1
0.0 0.1
-0.1 36.8
0.1 218.4
0.8 364.0
1.0 365.4
1.6 366.7
L.7 357.3
t.7 367.7
1.8 368.0
1.8 337.3
2.0 334.0
L.7 334.4
2.0 334.5
1.8 334.8
2.0 334.8
t.7 334.9
1.9 335.2
2.3 335.0
r..8 335.0
1.8 335.1
1.8 335.0
2.0 334.9
r..8 334.7
1.8 334.1
2.0 334.1
1.9 318.5
1.9 243.3
0.1
0.1
0.1
0,1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
1.3
5.5
t2.L
17.9
1,8.2
18.3
L8.4
18.4
18.3
18.4
18.4
18.4
18.4
18.4
17.8
17.8
17,8
t7.8
17.8
17.8
17.8
t7.9
77.8
77.9
71.8
17.8
r7.8
L7.9
L7.9
L7.9
L7.t
10.4
4.5
1.0
0.4
0.3
0.3
0.2
n,
0.2
0.2
0.2
0.2
0.2
0.1
0.2
0.1
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
o.2
0.4
0.2
-1.0
-1.8
-2.5
-2.3
-1.6
-L.2
-1.8
-2.7
-2.6
-1.5
-L.2
-1.5
-1.8
-1.9
-1.3
-L.7
-2.5
-4.0
-4.8
-5.2
-4.9
-4.8
-5.2
-5.6
4.9
4.8
-4.3
-4.8
-4.9
-4.9
-5.3
-5.3
-5.5
-6.9
-6.5
-6.3
-6.4
-6.8
-7.L
-6.9
-6.5
-6.0
-5.4
-2.9
15.8
69.2
151.9
240.2
303.2
334.8
3rt4.3
346.2
347.8
349.0
345.3
333.8
333.3
332.3
332.7
333.4
333.9
334.2
334.2
334.3
334.1
333.2
332.7
333.1
332.7
318.5
G P04 3AS - 02 27 22-P.T - 1298 Page 255 of 278
Time
4174/23 8:51:24
4l14/238:51:34
4/141238:5L:43
4/14/23 8:5t:53
4l14/23 A:52:O4
4/74/238:52:L4
4/L4/238:52:23
4lL4/238:52:33
4174/238:s2:M
4114123 8:52:54
4/L4/23a:53:03
4/14/238:53:L3
4h4/238:53:24
41141238:53:34
4/14/23 8:53:43
4/14/23 8:53:53
4/14123A:54:04
4/141238:54:t4
4/14/23 8:54:23
4/14/23 8:54133
4/14123 8:54:44
4/L4/23 8:54:54
4/14/23 8:55:03
4/L4123 8:55:13
4/L4/23 8:55:24
4/L4/23 8:55:34
4/L4/23 8:55:43
4/L4123 8:55:54
4/L4/23 8:56:04
4h4/238:56:L3
4/L4/23 8:56:23
4/14/23 8:56:34
4/14123 8:56:44
4/14/23 8:56:53
4/14/238:57:03
4/74/23 8:57:L4
4/141238:57:24
4/14/23 8:57:33
4/741238:57:43
4/14/238:57:54
4/14/23 A:58:O4
4/14/23a58:t3
4/t4/23A:58:23
4114123 8:58:34
4/L4/23 8:58:44
4/L4/23 8:58:53
4/L4/23 8:59:03
4/L4/23 8159:L4
4/14/23 8:59:24
4/14/238:59:33
4/74/23 8:59:43
4/14/23 8:59:54
4lt4/239:00:04
4/L4/239:00:13
4/14/23 9:0Ot24
4/14/23 9:QO:34
4/L4/23 9:OO:43
4/t4/23 9:QO:53
4/t4/23 9:0!:04
4/L4/23 9:Ot:r4
4/14/23 9:0r:23
41141239:01:33
4/!41239:0L:M
4/t4/239:0L:54
4/14/23 9:02:03
4/141239:02:L3
4/L4/239:OZ:24
4/14/239:O2:34
4/14/23 9:02:43
4/L4/23 9:02:53
4/L4/23 9:03:04
4/L4/23 9:03:14
G P04 3AS -0 2 27 22 -RT - t29A Page 256 of 278
co2
0.4
n?
0.2
0.1
n
0
0
0
SO2 NOx CO
6.7 764.9 214.6
t7.9 74.9 199.9
32.9 3.4 116.1
45.7 2.4 51.0
53.0 1.9 15.4
57.1 L.7 1.7
59.7 1.5 -1.9
61.5 1.0 -2.8
62.7 0.8 -3.3
53.4 1.0 -2.8
63.4 1.0 -7.1
53.8 0.8 -2.t
62.8 0.5 -2.2
6r.8 0.8 -2.3
61.8 0.6 -2.0
62.L 0.5 -t.7
62.0 0.7 -1.6
61.9 0.7 -1.6
61.9 0.8 -1.4
62.2 0.9 -1.8
62.3 0.9 -1.8
62.2 0.8 -2.0
62.4 0.8 -1.3
62.6 0.3 -1.1
62.7 0.3 -1.5
62.5 0.2 -2.7
62.6 1.4 -3.2
59.7 6.3 -2.9
49.2 9.1 -2.0
34.7 4.4 -1.3
20.5 0.2 -1.6
11.9 0.0 -3.2
7.5 0.1 -4.7
5.0 -0.2 -5.7
3.2 0.2 -5.4
2.2 0.2 -5.1
L.7 0.2 -4.6
1.5 0.1 -4.3
0.8 0.1 -4.5
0.4 0.0 -4.8
0.5 0.4 -5.7
o.2 0.1 -5.9
o.2 0.0 -5.8
0.1 0.1 -4.7
0.4 -0.2 -4.L
0.0 -0.3 -4.2
0.0 0.3 -4.7
0.3 0.5 -2.2
0.5 15.8 10.8
0.8 91.3 38.2
1.4 151.9 77.O
1.4 152.5 113.0
1.1 153.0 136.8
0.6 153.3 t47.1
o.1 154.0 150.5
1.1 153.7 151.9
0.8 153.9 152.t
t.2 153.8 151.3
0.8 153.8 150.9
1.1 L54.t L50.7
1.0 154.2 151.4
0.9 154.3 152.3
o.7 154.2 t53.2
0.9 t54.L 153.1
0.8 154.4 152.5
0.8 154.6 L5L.7
0.7 154.7 151.6
1.2 154.6 151.9
1.1 139.1 t46.2
4.L 63.1 126.3
8.9 2.3 91.0
15.0 1.5 52.r
0.1
0.1
0.1
0.1
0
0
0
0
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.5
2.4
5.1
8.2
8.7
8.8
8.8
8.9
8.9
8.9
8.8
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.9
8.8
7.t
3.8
!.4
0.3
o.2
0.2
0.2
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.2
0.2
0.1
Time
4lt4/23 9103:23
alra/239:03:33
4lt4/239:03:44
4/!4/239:03:54
4/741239:04:03
4/t4/239:O4:r3
4lt4/23 9:04:24
4/t4/239:U:34
4/14/239:04:43
4/14/239:04:s4
41141239:05:04
co2 502 NOx co
0.1
0.1
0.1
0.1
0.1
0.1
0.3
0.5
0.8
o.7
0.6
19.8
22.3
24.O
24.8
25.6
25.7
25.6
26.r
26.t
26,t
26.1
0.5
0.5
0.2
0.2
0.3
o.4
-0.1
0.1
-0.1
0.2
0.1
22.0
6.8
2.O
0.8
{.1
-L.4
-2.4
-2.4
-1.4
-0.9
-1.3
G P043AS-0 2 2 7 22- RT - L298 Page 257 of 278
Time
4h4/239:50:34
4/74/239:50:44
4/L4/23 9:5A:53
4/14/239:5L:03
4/t4/23 9:5L:L4
4/14/23 9:51:24
4h4/239:5L:33
4/141239:57:43
4/14/239:57:54
4/L4/239:52:04
4h41739:52:13
4/L4/239:52:23
4lt4/239:52:34
4/L4/239:52:44
4/14/239:52:53
4/14/239:53:03
4/14/239:53:t4
4/]41239:53:24
4l14/239:53:33
4/74/239:53:43
4/14/23 9:53:s4
4h41239:54:04
4/L4/239:54:13
4/L4/239:54:24
4/L4/239:54:34
4/L4/239:54:43
4174/239:54:53
4/741239:55:04
4/14/239:55:L4
4/74/239:55:23
4/ra/239:5st33
4/L4/239:55:44
4/14/239:55:54
alM/239:56:03
4/!41239:56:13
4/741239:56:24
4/\4/23 9:56:34
4/14/23 9:56:43
4/74/239:56:53
4/!4/239:57:04
4h4/239:57:r4
4/L4/239:57:23
4/14123 9:57:33
co2 so2 NOx
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
1.7
4.5
8.0
9.2
9.2
9.2
9.3
9.3
9.3
9.3
9.3
26.2 -0.1 -1.8
26.5 -0.3 -2.0
27.0 -0.2 -3.3
27.2 -O.2 4.7
27.0 -0.3 -5.s
27.5 -0.3 -4.6
27.L 4.7 -3.5
27.2 -0.5 -3.1
2't.4 -0.3 -2.9
27.2 -0.2 -3.4
27.2 -O.2 -3.9
26.9 4.2 -3.7
27.4 0.8 -0.5
24.9 L7.L L4.2
20.1 9s.3 43.8
13.1 158.s 83.2
7.9 159.1 LL8.7
4.8 159.1 141.5
3.4 1s9.1 152.0
2.4 159.2 154.8
2.r L59.2 155.3
L.7 159.2 155.5
L.4 159.1 155.5
1.3 L59.2 155.4
1.0 L59.2 154.8
1.0 159.6 154.6
0.6 759.7 155.4
0.7 L59,4 1s6.0
1.1 159.5 t55.7
0.9 159.5 15s.s
0.9 159.4 155.0
1.1 150.4 153.7
0.9 106.4 145.5
0.5 64.L 123.0
0.8 29.0 85.9
o.4 0.7 47.L
0.5 0.3 16.9
0.0 0.2 0.1
0.4 0.2 -6.7
0.1 {.1 -8.2
0.1 0.0 -8.1
0.0 0.2 -7.2
0.0 0.1 -6.5
G P04 3AS -0 2 27 22-Rr - 129A Page 258 of 278
Time
4lr4l23 L0:24:!4
4l!4123 L0:24:23
4l!4123 LO:24:33
4lL4lZ3 L0:24:44
4l!4123 LQ:24:54
4lr4l2310:25:03
4h4123 L0:25:L3
4lt4l23 t0:25:24
4/14/23 t0:25:34
4h4123 L0:25:43
4l!4123 L0t25t54
4174123 tO:26:O4
4h4123 L0:26:13
4l!4123 LO:26:23
4174123 L0:26:34
4/L4123 t0:26:44
4/L4123 t0:26:53
4lr4l23 10:27:03
4lL4l23 70:27:14
4lr4l23 10:27:24
4/14123 10:27:33
4h4123 L0:27:43
4/L4123 rO:27:54
4/L4123 t0:28:M
4174123 10:28:L3
4/]4123 !0:28:23
4lL4l23 t0:28:34
4/L4123 10:28:44
4/M/23 10:28:53
4lL4l23 t0:29t03
4lL4l23 t0t29tl4
4lt4l23 !0:29:24
4/t4123 Lo:29:33
4/L4/23 10:29:43
4/t4/23 t0:29:s4
4lL4/23 70:30:04
4/14123 r03O:r3
4/L4/23 L0:30:24
4lL4l23 L0130:34
4/L4/23 L0:30:43
4/L4123 70:30:53
4h4/23 70:3L:O4
4lL4l23 70:31:14
4lL4l23 r03r:23
4/14/23 L03l33
4/74123 L03r:44
4114123 L0:3Lt54
4l14l23 t0:32:03
co2 so2 NOx co
9,2
9,2
9.3
9.3
9.2
9.2
9.2
9.3
9.3
9.2
9.3
9.3
9.3
9.3
9.3
9.1
6.2
3.0
0.8
0.2
0.2
0.2
0.2
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
3.6 -0.1 -6.3
1.8 -O.2 -8.1
Lr -0.3 -8.2
0.9 -0.4 -7.6
0.5 -0.3 -7.1
0.1 .0.1 -6.8
0.3 -0.3 -7.!
0.1 -0.1 -7.6
-0.3 -0.4 -7.9
0.0 -0.2 -8.0
-0.1 -o.2 -7.6
-0.1 -0.1 -7.0
-0.1 -0.1 -5.9
0.0 -0.3 -6.8
0.2 4.2 -7.3
0.0 7.2 -6.9
-0.1 45.5 4.2
0.0 83.6 Zt.8
0.1 125.1 59.1
0.2 1s8.7 99.9
0.7 1s8.7 130.9
0.7 158-9 147.1
0.8 159.1 152.9
0.5 159.2 153.8
0.6 159.1 155,0
o.7 159.2 155.9
0.8 159.1 156.3
0.6 159.2 155.8
0.6 159.3 155.1
o.7 159.2 L54.7
0.7 t59.2 155.1
0.6 159.3 155.9
0.5 159.7 L57.L
0.6 L59.7 L57.5
o.7 158.2 154.0
2.6 14r.7 139.0
7.7 53.1 108.5
74.3 1.0 58.8
19.8 0.6 32.8
22.7 0.4 9.8
24.5 0.0 -0.4
25.2 0.0 -3.4
25.5 0.0 -3.s
26,1 0.0 -3.7
27.L 0.0 -3.6
26.9 -0.1 -3.5
26.7 0.1 -3.8
26.9 -O.2 4.8
G P04 3AS - 0 227 22 -RT - t298 Page 259 of 278
Time
4h4l23lL:0r:O3
4/L4123 LL:OI:L3
4lL4l23 Lr:O!:24
4h4/23 !t:0r:34
4/L4/23 LL:OI:43
4lL4l23 L7:OL:54
4lL4l23 L1:O2:O4
4/L4123 tL:02:r3
4lL4l23 Lf:O2:23
4lL4/23 tt:02:34
4ll4l73 Lr:02:44
4/L4/23 tt:02:53
4lL4/23 LL:O3:O3
4l!4123 LL:03:!4
4lL4l23 L!:03:24
4/L4123 tl:03:33
4/14/23 tL:01:43
4h4123fl:03:54
4/L4123 71:M:O4
4l14/23 fi:O4:13
4lL4l23 Lr:O4:23
4/L4/23 LL:O4:34
4lL4/23 L!:O4:44
4/14/23 lt:04:53
4/14/2X Lt:O5:03
4h4123 t1:O5:14
4174123 Lr:05:24
4lL4/23 17:05:33
4l!4123 !l:05:43
4/74/23 Lt:05:54
4lt4l23 7L:06:U
4lr4l23 fl:06:Lg
4lL4/23 fl:O6:24
4lL4l23 LL:O6:34
4lL4l23 Lr:O6:43
4lL4/23 u:O6:53
4h4123 L7:O7:04
4lr4l23 Lr:O7:14
4/74/23 L!:07:23
4/L4/23 tt:07:33
4lL4/23 LL:07:M
4lL4l23 f:Ol:54
4lL4l23 u:O8:O3
4/L4/23 L!:O8:!3
4h4123 L7:Q8:24
4lL4l23 Ll:08:34
4lL4/2? L7:08:43
4lr4l23 rL:O8:53
4/14123 IL:O9:O4
4/14123 1L:O9:L4
4h4P3 71:09:23
4lt4l73 LL:O9:33
4lL4/23 Lr:O9:44
4lL4l23 Lt:09154
4lL4/23 1t:10:03
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
L.7
4.4
7.9
9.2
9.2
9.3
9.3
9.3
9.3
9.3
9.3
27.3 -0.2 -1.5
27.4 -0.3 -2.3
27.L -0.2 -2.L
27.L -0.2 -2.L
27.2 -0.2 -2.0
26.9 -0.1 -2,C
27.4 -0.2 -2.6
26.9 -0.3 -3.2
26.9 4.2 -3.9
26.7 -0.3 -3.8
27.3 -0.2 -3.9
27.3 -0.2 -3.3
27.6 -0.3 -2.4
27.4 -0.3 0.3
25.0 u.4 13.4
19.8 69.7 43.0
L3.2 116.5 82.6
7.8 Lr1 .0 118.8
4.9 1L7.7 139.8
3.3 727.5 150.6
2.4 137.9 153.9
1.9 748.2 153.9
1.5 148.4 153.2
r.4 t48.4 152.8
1.1 148.5 152.5
0.9 144.6 153.3
1.0 t49.4 754.2
0.9 152.8 154.3
1.1 153.1 754.4
0.9 153.6 153.4
1.0 153.8 t52,4
0.7 153.9 152.3
0.8 154.0 152.1
0.9 L54,2 L52.7
1.0 154.0 152.8
0.8 154.3 152.6
0.7 154.5 L52.L
0.7 154.6 Ls2.L
0.7 155.3 t5!.7
0.7 155.0 1s1.6
0.6 154.8 151.8
0.7 155.3 1s2.4
0.6 155.3 L52.9
0.6 155.5 151.8
0.6 L40.2 L44.1
o.7 53.5 727.7
0.4 2.5 85.1
0.1 !.4 44.9
4.2 0.3 t4.7
0.1 0.4 -L.4
-0.2 {.1 -7.0
-o.1 0.1 -8.4
-0.1 0.2 -8.3
o,2 0.1 -8.2
-o.2 0.1 -7.6
G P04 3AS -02 27 22-Rr - t298 Page 260 of 278
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.4
9.0
5.7
2.6
0.6
o.2
0.2
o.2
0.2
o.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
2.4 -0.3 -6.1
t.4 -o.2 -8.0
1.1 -0.4 -7.9
0.4 -0.4 -7.9
o.2 -0.2 -8.1
o.2 -0.1 -8.9
0.1 -0.3 -9.0
-0.1 4.2 -8.2
-0.1 4.2 -8.0
0.0 4.2 -8.3
-o.2 4.2 -8.5
-0.1 -0.1 -8.7
-0.2 -0.1 -8.6
-0.2 4.2 -8.5
o.o 0-o -7.9
-0.2 15.4 1.3
0.2 94.2 2s.2
0.0 158.0 63.2
0.5 158.3 103.6
0.3 159.4 132.3
0.6 159.2 L47.5
1.0 159.3 !52.6
0.7 159.4 153.5
0.5 160.1 154.0
0.5 159.8 154.3
o.7 159,9 t54.7
0.8 160.0 t*.2
1.0 159.8 153.7
0.8 159.8 153.8
0.5 1s9.8 L54.2
0.8 1s9.9 153.9
0.8 159.5 1s3.1
0.7 150.4 ts2.6
0.8 150.9 L52.2
0.8 161.0 150.6
L.6 145.3 L4L.9
5.4 65.3 117.8
!L.4 1.5 84.4
15.5 0.9 45.5
2t.o 0.3 L7.3
22.9 0.3 2.6
24.5 {.1 -1.9
2s.7 0.1 -2.8
25.5 0.1 -2.4
26.4 4.2 -1.7
26.3 -0.3 -1.0
26.7 -0.1 {.9
25.8 -0.2 -1.3
26.9 4.2 -2.L
26.7 -0.3 -2.4
26.8 -O.4 -2.2
25.8 -0.3 -1.3
Time
4lL4l23 LL:36:33
4lL4l23 1136:44
4l14/23 Lt:36:s4
4lr4l23 Lt:37:03
4/L4/23 rL37:t3
4/t4/23 Lr37:24
4114123 Lr37:34
4h4123 Lt:37:43
4lr4l23 Lr37:54
4h4123 Lr38:04
4h4123 Lt38:r3
4/74/23 Lr38:23
4lL4l23 Lr38:34
4/14/23 Lr:38:44
4l!4123 rL38:53
4114123 L7:39103
4lL4l23 l!:39:!4
4lL4l23 17139:24
4lt4l23 Lt:39:33
4lM/23 Lt:39:43
4/14/23 l!:39:54
4/L4123 LL:40:o4
4l14l23 L140:13
4lL4l23 L7:40:23
4h4173 L1:40:34
4lr4l23 Lr:40:44
4l14l23 L140:53
4h4123 Lr:4L:03
4lt4l23 LL:4L:74
4h4123 Lr:4L:24
4lr4l23 LL:4L:33
4lr4l23 lL:41:43
4lr4l23 l1:4L:54
4lr4l23 Lr:42:04
4/14123 Ll:42:L3
4lr4l23 LL:42t24
4/!4123 rr:42:34
4lr4l23 rL:42:43
4/L4/23 LL:42:53
4114123 rl:43114
4/L4123 L7:43:t4
4l14l23 L7:43123
4/L4/23 Lt:43:33
4114/23 Lt:43144
4lt4l23 L1:43154
4lr4l23 rr:M:03
4lr4l23n:a4:B
4lL4l23 L7:44124
4l14/73 i:44:34
4l14/23 Ll:44:43
4lL4l23 tL:44:53
41141?3 LL:45:M
G P04 3AS -0 227 22-Nt - L298 Page 26L of 278
Time
4lt4l23 L2:t2:44
4lr4l23 72:L2:54
4l!4123 !2:L3:O3
4lt4l23 L2:L3:r3
4/14123 t2:L3:24
4lt4l23 r2:L3:34
4h4123r2:t3:43
4/L4123 r2:L3:54
4lr4l23 t2:L4:04
4lL4/23 L2:L4:73
4lL4l23 L2:r4:23
4lL4l23 L2:14:34
4lt4l23 t2:74:44
4/L4/23 t2:L4:53
4lL4l23 L2:L5:03
4lt4l23 L2:L5tL4
4lt4lZ3 L2:L5:24
4/L4/23 !2:L5:33
4lL4l23 t2:!5:43
4lL4lZ3 LZ:r5:54
4lr4l23 !2:L6:O4
4l!4123 !2:!6:L3
4lr4l23 t2:r5:23
4lt4l23 L2:L6:34
4lL4l23 12:L6:M
4h4123 !2:L6:53
4lL4l23 12:17:O3
4h4123 L2:77:14
4/L4123 L2:!7:24
4lt4l23 L2:L7:33
4lL4l23 L2:!7:43
4/L4123 L2:17:54
4lL4l23 L2:r8:O4
4/L4123 L2:78:73
4lt4l23 L2:r8:24
4/L4123 L2:r834
4lr4l23 t2:L8:43
4/!4/23 L2:L8:53
4lr4l23 r2:r9:O4
4h4123 r2:L9:L4
4lr4l23 t2:L9:23
4/74/23 12:L9:33
4/1412312:L9:44
4lr4l23 r2:L9:s4
4h4/23 L2:20:03
coz so2 NOx co
0,1
0.1
0.1
0.1
0,1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.6
2.9
6.0
9.1
9.3
9.3
9.3
9.3
9.4
9.4
26.9 -0.2 -6.7
26.4 -O.2 -5.4
27.2 0.1 -3.6
27,4 -0.3 -3.4
27.2 -0.4 -?.2
27,0 -0.1 -3.3
27.O -0.2 -3.3
27.3 -0.1 -4.0
27.r -0.4 -4.0
26.9 4.2 4.L
27.2 {.3 -3.5
27.4 0.0 -3.1
27.2 0.0 -3.2
27.O 0.4 -0.1
24.5 17.3 15.4
19.5 97.7 46.8
t2-9 162.4 88.2
8.3 162.7 123.9
5.2 162.8 145.4
3.5 153.0 153.5
2.3 162.8 155.2
1.9 162.8 156.3
1.5 163.0 153.9
1.3 162.8 153.8
r.4 163.3 153.4
r.2 163,1 154.0
0.9 153.3 L*.2
o.7 163.3 154.3
\.L 163.2 t54.4
1.1 163.4 153.8
0.8 153.3 153.5
0.6 153.5 153.7
0.8 163.4. 1s3.8
o.7 163.3 153.8
o.7 163.5 153.2
0.8 163.4 L50.7
1.0 L47.3 137.8
0.9 65.8 L07.5
0.4 L.2 66.8
0.1 0.7 29.7
0.4 0.3 5.6
o.2 0.2 -5.1
0.1 0.1 -8.1
-0.2 0.1 -8.2
0.0 4.3 -8.3
G P043AS-0227 22-RT - L298 Page 262 of 278
Time
4lt4l23 t2:4s:s3
4lt4l23 t7t46:04
4lL4l21 12:45:14
4h4/23 L2:46:23
4/t4/23 12:46:33
4/t4123L2:46:44
4h4123 ]^2:46:54
4lt4l23 12:47:03
4lt4l23 ]^2:47:t3
411412372:47:24
4lL4l23 12:47:34
4lL4l2312:47:43
4lL4l23 t2:47:53
4lL4l23 12:48:04
4lL4/23L2:4:r4
4lt4l23 72:48:23
4lL4l23 12:48:33
4lt4l23 L2:48:44
4h4/2312:48:54
4l14/23 12:49:03
4lr4l23 L2:49:L3
4l14l23 L2:49:24
4lt4l23 L2:49134
4lL4l23 12:49:43
4l14/23 L2:49:s4
4/14123 L2:sO:04
4lt4l23 L2:50113
4lL4l23 t2:50:23
4h4/23 L2:50:34
4lr4l23 L2:50:44
4/14123 L2:50:53
4lr4l23 t2:5t:03
4h4123 L2:5r:L4
4h4123 L2:51:24
4lr4l23 t2:5r33
4/74123 12:51:43
4lr4l23 12:5!:54
4lL4/23 r2:s2:04
4lt4l23 72:57:13
4lMl23 r2:s2:23
4lL4l23 t2:52:34
4lL4l23 !2:52:44
4/L4/23 72:52:53
4/14123 12:53:03
4lL4l23 L2t53t14
4lL4l23 L2:53:24
4/L4/23 12:53:33
4l14l23 L2:53:43
4lL4l23 L2:53:54
4lL4l23 L2t54:A4
4lr4l23 r2:s4:13
4lL4l23 LZi54:24
4l14l23 L2:54:34
4lL4/23 L2:54:43
4lL4l23 12:54:53
4lL4l23 r2:s5:0a
4lr4l23 L2:55:14
4h4123 L2:55123
4lt4l23 L2:55131
4lt4/23 L2:55:M
4114/23 L2:s5:54
9.3
9.3
9.3
9.3
9.3
9.4
9.3
9.3
9.4
9.4
9.4
9.3
9.3
9.2
9.3
9.2
9.2
9.2
9.2
9.2
9.3
9.2
9.2
9.2
9.2
9.3
9.0
6.3
3.0
0.8
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
0.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
2.2 {.2 -3.6
1.4 -0.4 -5.2
0.8 4.2 -s.6
0.s -0.3 -6.7
0.2 -0.3 -8.8
o,2 -0.2 -9.3
-0.2 -0.3 -8.4
-0.2 -0.4 -7.0
-0.2 0.0 -5.5
0.0 -0.2 -7.L
0.2 -0.1 -7.9
0.0 -0.3 -8.5
0.0 -0.4 -7.9
0.0 -0.1 -7.3
-0.1 -0.2 -7.2
-0.2 -0.2 -7.4
-0.3 -0.1 -7.L
0.0 -0.1 -7.8
0.0 -0.3 -8.0
-0.3 0.0 -8.4
-o.2 4.2 -9.1
o.2 {.4 -9.5
0.0 {.1 -9.6
-0.1 4.2 -8.9
-0.2 -0.1 -8.1
-0.1 {.1 -7.8
0.0 4.6 -8.2
-o.1 30.2 -1.5
o.2 61.0 19.4
0.3 rL7.6 56.2
0.3 163.5 97.0
0.7 163.9 L29.1
o.7 164.0 146.8
0.8 164.1 152.8
0.9 164.5 152.9
0.7 164.2 L52,7
0.7 ru.6 152.9
0.8 164.6 154.0
0.8 163.9 154.s
0.8 154.0 153.7
0.7 L64.2 1s2.8
o.7 154.0 152.1
0.5 164.3 L5L.7
o.5 164.7 151.3
0.7 164.9 t52.2
o.7 163.8 149.5
3.2 L46.4 133.8
8.3 65.3 102.3
15.1 0.9 63.7
19.6 0.7 28.5
22.! 0.3 7.9
23.9 0.3 -0.1
25.7 0.2 -1.8
26.0 0.1 -2.L
26.7 4.2 -2.3
26.9 -O.3 -2.8
26.7 -0.1 -3.1
27.L 4.2 -3.1
26.9 -O.s -2.4
27,L 0.0 -L.9
GP043AS-0227 22-RT -L298 Page 263 ot 278
Time
4/14123 13:23:53
4lr4l23 73:24104
4h4lZ3 L3:24i14
4h4/23 t3:24:23
4/L4123 L3:24:33
4/L4123 L3:24:44
alL4/23 L3:24:s4
4lt4/23 L3:25:O3
4lL4l23 L3:25:r3
4h4/23 L3:25:24
4i14123 73:25:34
4lr4l23 t3:25:43
4/14123 13:25:54
4/t4/23 t3:26:O4
4174123 t3:26:13
4ll4l23 !3:26:23
4/L4/23 13:26:34
4/L4/23 L3:26:44
4/L4/23 L3:26:53
4lL4l23 L3:77:03
4/t4123 L3:27:r4
4h412313:27:24
4lL4l23 L3:27:33
4lL4/23 L3:27:43
4lr4l23 B:27:54
4l!4123 r3:28:O4
4lr4l23 73:28:13
4/t4/23 L3:28:23
4/L4123 L3:28:34
4lL4l23 L3:28:44
4lL4/23 l3:78:s3
4lLal23 13:29:03
4/L4123 L3:29:t4
4lL4l23 t3:29:24
4/74/23 f3:29:33
4/14123 L3:29:43
4h4123 L3:29:54
4lL4l23 L3:30:04
4lL4l23 L330:r3
4lt4l73 L3:30:24
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.0
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.0
0.1
0.0
0.1
0.8
3.1
6.5
9.1
9.2
9.2
9.2
9.3
9.3
9.3
9,2
9.2
27.3 -0.1 -2.7
?7.2 -O.2 -1.7
27.4 -0.2 -1.0
27.t -0.5 -1.6
27.t 4.2 -2,4
27.3 -0.s -4.0
27.3 4,2 -4.8
27.1 4.2 4.L
27.O 4.2 -0.4
25.0 16.1 L4.6
t9.7 98.2 44.7
t3.4 154.5 84.4
8.5 164.6 717.9
5.8 155.5 140.2
4.0 155.3 149.8
2.6 155.2 152.8
2.4 165.6 153.8
r.7 L65.7 154.3
1.1 165.5 154.3
0.9 16s.6 153.9
0.7 165.6 152.9
0.9 L65.7 L57.7
1.1 165.6 151.3
0.9 165.5 7s2.t
0.9 L65.2 152.9
0.9 155.4 153.4
1.0 165.5 L54.7
0.6 165.6 154.8
0.8 1il.8 150.5
1.0 147.7 133.6
o.7 66.2 101.9
0.5 L.2 61.3
0.1 0.7 25.9
-o.2 0.2 4.1
0.0 0.3 -4.8
-0.3 0.0 -8.0
-0.2 -0.2 -9.4
-0.2 -0.2 -9.7
-0.1 -0.3 -9.6
-0.1 -0.4 -9.1
G P043AS -02 27 22-RT - t29 I Page 264 of 278
Time
4lL4l23 L3:56:33
4lt4l23 L3:56143
4114123 L3:56:54
4l!4173 L3:57:04
4/!4/23 L3:57:t3
4h4123 L3:57:24
4lr4l23 L3:s7:34
4h4123 t3:57:43
4lL4/23 t3157t53
4lL4l23 !3:58:04
4/L4123 t3:58:L4
4/L4123 L3:58:23
4lL4l23 t3:58:33
4lr4l23 !3:58:44
4lL4l23 13:58:54
4h4123 73:s9:03
4/14123 13:59:!3
4lL4l23 13:59:24
4lL4l23 L3:s9:34
4/t4/23 L3:59:43
4lt4l23 L3t59:53
4/L4123 L4:00:04
4lL4l23 74:00:74
4lL4l23 L4:00:23
4lL4l23 L4:00:33
4/L412314:00:M
4lL4l23 74100:54
4lt4l23 L4:0t:03
4/1412314:0r:73
4lL4l23 l4t0tt24
4lr4l23 L4:OL:34
4174123 t4:0L:43
4lt4l23 l4:O7:54
4h4123 14:02:04
4/L4/23 r4:02:L3
4lr4l23 !4:02:23
4lI4l23 !4:02:34
4lL4l23 L4:02:M
4/L4123 L4:02:53
4lL4/23 L4:03:O3
4lL4/23 t4:03:r4
4lL4l23 t4:O3:24
4/t4/23 14:03:33
4/L4/23 L4103:43
4lL4l23 L4103:54
4lL4l23 !4:04:04
4/L4123 t4tD4:13
4ll4l23 74:04:23
4lL4/23 L4:04:34
4/14123 L4:U:44
4lL4/23 L4:O4:53
9.3
9.3
9.3
9.3
9.3
9.3
9.3
9.4
9.3
9.3
9.3
9.3
9.3
8.7
4.9
2.0
0.3
0.2
o.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.2
o.2
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.5 -0.2 -9.0
0.0 -0.3 -9.9
0.2 -o.2 -L0.7
-0.2 -0.3 -11.0
0.1 -0.3 -10.5
-0.2 -0.3 -9.7
-0.3 0.1 -9.2
-0.1 -0.1 -9.1
-0.1 0.1 -9.4
-0.2 -0.1 -10.4
-0.2 4.r -11.0
0.0 4.4 -10-8
0.2 4.4 -10.9
0.1 -0.1 -8.6
4.4 L6.2 3.5
0.1 98.4 32.L
0.0 t@.4 72.r
0.5 154.5 110.3
0.4 164.8 t36.2
0.5 165.7 t48.2
0.5 165.8 151.5
0.6 155.8 151.9
0.6 165.8 151.9
0.6 166.3 151.6
0.5 165.5 150.4
0.7 166.0 149.7
0.7 156.1 749.3
0.8 166.3 749.9
0.5 766.4 151.4
0.6 t66.2 Ls2.7
0.7 15s.9 153.3
0.7 166.7 ts2.6
0.6 154.6 t52.2
1.8 92.7 L42.8
6.3 39.3 116.1
r2.3 18.0 77.0
L7.8 0.5 38.s
2t.2 0.4 !2.6
23.6 0.0 0.4
24.8 0.2 -3.5
25.7 0.1 -4.2
26.1 {.1 -3.7
26.4 4.4 -3.1
26.9 -0.2 -3.4
26.9 -0.4 4.5
26.9 4.2 .5.3
27,' -0.2 -5.2
27,1 -0.2 4,7
27,0 -0.3 4.5
27.2 -0.1 -4.1
G P04 3AS -0 227 22 -Rr - L298 Page 265 of 278
Time
4h4/23 L4:3L:53
4l!4123 L4:32:03
4l!4123 t4:32:L4
4lr4/23 14:32:24
4/t4/23 L4:32:33
4/L4/23 L4:32:43
4lL4lZ3 L4:3?:54
4lL4/23 L4:37:04
4/14123 L4:33:13
4lL4/23 L4:33:24
4/L4/23 L4:33:34
4lL4l23 t4:33:43
4/14/23 L4:33:s3
4/14/23 14:34:04
4lL4l23 L4:34:L4
4/L4123 L4:34:23
4lL4/23 L4:34:33
4lL4l23 L4:34:44
4lL4/23 L4:34:54
4l14/23 L4:35:03
4lL4l21 t4:35:L3
4i14123 r43s:24
4h4/23 1435:34
4lL4l23 L4:35:43
4lL4l23 L4:35:53
4lL4l23 L4:36:04
4lL4/23 L436:r4
4/L4/23 t4:36:23
4/14/23 14:36:33
4lL4l23 14t36:44
4lL4l23 t4:36:54
4lL4/23 14:37:03
4/L4123 1437:L1
4/L4/23 L4:37:24
4/t4123 L4:37:34
4lL4/23 L4:37:43
4h4/23 t4:37:54
4lr4l23 14:38:04
4l14/23 L438:r3
4/L4/23 1438:23
4l14/23 !4:38:34
4lt4l23 L4:38:4a
4lL4l23 L4:38:53
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0,r
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.8
3.1
6.5
9.1
9.1
9.2
9.2
9.3
9.2
9.3
9.2
4.7
27,0 -0.1 4.2
27.O {.3 4.4
27.2 -0.3 {.6
27.2 -0.2 -3.8
27.1 -0.2 -2.6
27.2 0.2 -2.2
27.4 -0.3 -2.8
27.7 -0,2 -3.0
27.2 -0.1 -r.4
27.4 -0.2 -3.0
27.3 3.3 -2.5
27.2 27.8 4.3
23.4 50.1 24.6
L7.3 114.5 59.8
10.7 166.4 99.3
6.7 166.9 130.3
4.2 167.1 147.3
3.0 167.4 153.8
1.8 L67,5 153.8
1.5 L67.1 154.8
1.5 L67.O 155.2
1.1 L67.3 154.0
t.2 167,2 1s3.1
0.8 L67.3 152,1
0.9 167.7 7s2.9
0.9 767.4 154.0
0.8 L57.3 Ls4.t
1.0 t67.6 154.1
0.8 L67.5 L53.4
0.8 167.4 153.2
0.8 t67.5 153.2
0.6 166.8 148.8
0.9 !49.7 134.1
0.7 66.7 103.5
0.s 1.5 53.1
0.3 0.6 26.3
-0.2 0.2 3.3
0.2 4.2 -6.2
-0,2 0.0 -8.5
-0.2 0.1 -9.1
-0.3 0.3 -9.5
0.4 2.8 -10.3
G P04 3AS-0 22 7 22-RT - L298 Page 266 ot 278
Appendix C.4
Calibration Gas Certificates
G P04 3AS-0 227 22-RT - t298 Page267 ot278
Airgas"
an Air Liqui(b cornpeny
Airgas Specialty Gases
Airgas USA LLC
S2S North Industrial toop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
153402559134-1
150.0 cF
2015 PS|G
590
Oct03,2022
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600iR-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 95o/o. There are no significant impurities which affect the use of this calibration mixtur€. All concentrations ars on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below 100 osia. i.e.0.7
8.930 7o
10.83 Yo
G1
G1
+l- 0.8o/o NIST Traceable
+l- 1.0o/o NIST Traceable
Type Lot lD
CALIBRATION STANDARDS
No Concentration
CC41'1744 7.489o/o CARBON DIOXIDE/NITROGEN
SG9161286BAL 12.05%OXYGEN/NITROGEN
Date
May 14,2025
Dec 14,2023
NTRM
NTRM
1 3060405
98051010
lnstrumenUMakelModel
Triad Data Available Upon Request
Sionature on file
Approved for Release
G P043AS-0 2 27 22-RT - L29 I
ANALYTICAL EQUIPMENT
Analytical Principle Last Calibration
Page 1 of 1
268 of 278
CERTIFICATE OF AI\ALYSIS
Grade of Product: EPA PROTOCOL STAI\DARI)
E03N180E15A0015
cc16591
124 -Tooele (SAP) - UT
872022
co2,02,BALN
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Oct 03. 2030
AI\TALI/TICAL RESULTS
Actua! ProtocolConcentration Method
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02
Page
Airgas.
an Air Liquide company
Airgas Specialty Gases
Airgas USA LI,C
525 North Industrial loop Road
Tooele, III 84o74
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
E03Nt61E1540287
EB0157206
124 -Tooele (SAP) - UT
872022
c02,02.BALN
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
1 53-402506334-1
158.0 CF
2015 PSIG
590
4u908,2022
Expiration Date: Auq 08.2030
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 20 12)" document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interferenco. 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 noted. The results relate only to the items tested. The report shall noi be reproduced except in full without approval of the laboratory. Do
Not use This below 100 osio. i.e.0.7
17.94 0/o
21.O',! o/o
CALIBRATION STANDARDS
Concentration
24.04 o/o CARBON DIOX IDE/NITROGEN
22.53 O/O OXYGEN/N ITROGEN
+l- O.7o/o NIST Traceable
+l- O.5o/o NIST Traceable
G1
G1
Type Lot lD Cylinder No Uncertainty Expiration Date
Dec 11, 2025
May 13,2025
0.6%
0.4o/o
NTRM
NTRM
13060802
09061434
cc415397
cc282492
ANALYTICAL RESULTS
Actua! ProtocolConcentration Method
Total Relative
Uncertainty
lnstrumenUMake/Model
ANALYTICAL EQUIPMENT
Analytical Principle
CO2 NDIR (Dixon)
ry
Jul 20,2022
Jul 20.2022
Horiba VIA-510 SV4MEUTJ CO2
Horiba MPA-510 W603MM58 02 02 Paramagnetic (Mason)
Triad Data Available Upon Request
Sionatura on file
Approved for Release
G P04 3AS-02 27 22 - RT - L298
Page I of I
Page 269 of 278
Aitgas.
an Air Liquide company
Airgas Specialty Gases
Airgas USA LLC
SzS North Industrial Ioop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number: XC0229748
Laboratory:124 -Tooele (SAP) - UT
SO2,BALN
Expiration Date: Oct17,2026
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12i531, 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 othenvise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder b6low 100 psig, i.e. 0.7
Grade of Product: EPA PROTOCOL STANDARI)
E02Nt99E15A1190
CERTIFICATE OF ANALYSIS
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
1 53-402560667-1
144.0 CF
2015 PS|G
660
Oct 17,2022
PGVP Number: 872022
Gas Code:
SULFUR DIOXIDE
NITROGEN
26.00 PPM
Balance
26.51 PPM +l- 0.9o/o NIST Traceable 1 0 I 1 0 I 2022, 1 0 I 1 7 I 2022
AIYALYTICAL RESULTS
Actual Protocol Total Relative
NTRM 16011058 CC473939 49.02 PPM SULFUR DIOXIDE/NITROGEN 0.8%Mat 22.2028
ANALYTICAL EQUIPMENT
Nicolet iS50 AUP2010228 SO2 LSO2 FTIR Oct04.2022
Triad Data Available Upon Request
Sionatrrra on fila
Approved for Release
G P04 3AS - 0 2 2 7 22 - RT - L29 I
Page 1 of 1
Page 27O of 278
Aitga$.
an Air Liquid. company
Airgas Specialty Gases
Airgas USA LLC
5zS North Industrial Loop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402465526-1
144.0 CF
2015 PS|G
660
Jun 21,2022
Expiration Date: Jun 21.2030
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600/R-1 2/531 , 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 signmcant impurities which aff€ct the use of this calibration mixture. All concentrations are on a
mole/mole basis unl€ss otherwise noted. The results relate only to the itgms tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below 100 Dsiq. i.e.0.7
SULFUR DIOXIDE
NITROGEN
62.00 PPM
Balance
61.94 PPM +l- 0.9Yo NIST Traceable 06t 1 4t2022, 06t 21 t2022
CERTIFICATE OF AIYALYSIS
Grade of Product: EPA PROTOCOL STAI\DARI)
E02Nt99E15404P9
4LM041741
124 - Tooele (SAP) - UT
872022
SO2,BALN
CALIB RATI ON STAI{DARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM
NTRM
98.32 PPM SULFUR DIOXIDE/NITROGEN
49.02 PPM SULFUR DIOXIDE/NITROGEN
17060436
1 601 1 030
cc486456
cc473235
0.8o/o
0.806
Dec07,2022
Jun 17.2022
lnstrumenUMake/Model
ANALYTICAL EQUIPMENT
Analytical Principle Last Multipoint Calibration
Nicolet iS50 AUP2110269 SO2 LSO2 FTIR Mav 24.2022
Triad Data Available Upon Request
Sionature on file
Approved for Release
G P04 3AS-02 27 22 -RT - L298
Page 1 of I
Page 271 of 278
Airgas
an Air Liquido company
Airyas Specialty Gases
Airgas USA LLC
Sz5 North InduSrial hop Road
Tooele, UT 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
CylinderVolume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153402645362-1
144.0 CF
2015 PS|G
660
Jan 30, 2023
Expiration Date: Jan 30.203i
Certification 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 calibralion mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items testod. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder below 100 Dsiq, i.e. 0.7 msoaoascals.
NOX
CARBON MONOXIDE
NITRIC OXIDE
NITROGEN
150.0 PPM
150.0 PPM
150.0 PPM
Balance
G1
G1
G1
+l- 1.0o/o NIST Traceable
+l- 0.60/o NIST Traceable
+l- 1.0o/o NIST Traceable
01 t23t2023, 01 t30t2023
01t23t2023
01 t23t2023, 01 130t2023
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
E03Nt99E1540353
cc503690
124 - Tooele (SAP) - UT
872023
CO,NO,NOX,BALN
ANALYTICAL REST]LTS
Actual Protocol Total RelativeConcentration Method Uncertainty
NTRM
PRM
NTRM
GMIS
09010226
12409
20061 057
1534012021103
KALOO4835 98.48 PPM CARBON MONOXIDE/NITROGEN
D913660 15.01 PPM NITROGEN DIOXIDE/AIR
CC73U82 98.61 PPM NITRIC OXIDE/NITROGEN
ND73O12 4.956 PPM NITROGEN DIOXIDE/NITROGEN
or RGM noted above is only in reference to the GMIS used in the assav and not Dart of the
0.506
1.5o/o
0.90/o
1.60/o
oct.16,2024
Feb 17,2023
Oct 06, 2026
Jun 15,2025
ANALITICAL EQUIPMENT
Jan 05, 2023
Jan 25,2023
Jan 25,2023
Nicolet iS50 AUP201O228 CO LCO
Nicolet iS50 AUP201O228 NO LNO
Nicolet iS50 AUP2010228 NO2
FTIR
FTIR
FTIR NO2
Triad Data Available Upon Request
Sionature on file
Approved for Release
G P043AS-0227 22-RT - L298
Page 1 of 1
Page 272 of 278
Airgas.
an Air Lhuidc cornpany
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Ioop Road
Tooele, UT 84o74
Airgas.com
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153-402645363-1
144.0 CF
2015 PS|G
660
Jan 30, 2023
Expiration Date: Jan 30.2031
Certification 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 @rrection 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 concentraiions are on a
mole/mole basis unless otheryvise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below '100 osio. i.e.0.7
NOX
CARBON MONOXIDE
NITRIC OXIDE
NITROGEN
330.0 PPM
330.0 PPM
330.0 PPM
Balance
G1
G1
G1
+l- 1.2o/o NIST Traceable
+l- 0.7o/o NIST Traceable
+l- 1.2o/o NIST Traceable
0 1 I 23 t2023, O'.t t30 t2023
01t23t2023
o 1 I 23 I 2023, O 1 I 30 I 2023
CERTIFICATE OF AI{ALYSIS
Grade of Product: EPA PROTOCOL STAMARI)
E03Nt99E15A0456
41M023189
124 -Tooele (SAP) - UT
872023
ANALYTICAL RESULTS
Actual Protocol Total Relative
Concentration Method Uncertainty
1 5060535
12409
20060324
20060305
1534012021103
CC450676 491.9 PPM CARBON MONOXIDUNITROGEN
D913660 15.01 PPM NITROGEN DIOXIDSAIR
EBO113041 250.3 PPM NITRIC OXIDE/NITROGEN
E80112886 250.3 PPM NITRIC OXIDE/NITROGEN
ND73O12 4.956 PPM NITROGEN DIOXIDSNITROGEN
NTRM. PRM, or RGM noted above is onlv in reference to lhe GMIS used in the assay and not part of the
0.6%
1.5o/o
0.8o/o
0.8%
1.6o/o
Mar05,2027
Feb 17,2023
Oct 19, 2026
Oct 19, 2026
Jun 15, 2025
ANALYTICAL EQTIIPMENT
Nicolet iS50 AUP2010228 CO MCO
Nicolet iS50 AUP2010228 NO MNO
Nicolet iS50 AUP2010228 NO2
FTIR
FTIR
FTIR NO2
Jan 05, 2023
Jan25,2023
Jan25.2023
Triad Data Available Upon Request
Sianetura on fila
Approved for Release
G P04 3AS-02 27 22-RT - L298
Page I of I
Page 273 of 278
Appendix C.5
Accred itation I nformation / Certifications
G P043AS -02 27 22-RT - L29 I Page 274 of 278
SIAE
Accredited Air Emission Testing Body
A2LA hos occredited
MONTROSE AIR QUALITY SERVICES
ln recognition of the successful compleiion of the joint A2LA ond Stock Testing Accreditotion Council (STAC)
evoluoiion process, this loborotory is occredited to perform testing octivilies in complionce with
ASTM D7036:2004 - Slondord Proctice for Competence of Air Emission Testing Bodies.
Vice President, Accredilotion Services
For the Accreditoiion Council
Certificoie Number 3925.0 I
Volid to Februory 29,2024
This ucreditation program is not included. under the A2LA ILAC Mutual Recognition Arrangement.
Americon Associofio n f or Loborotory Accreditotion-m
PresenieQ this 4th doy of Februory 2022.
GPO43 AS -0227 22-RT- 1298 Page 275 of 278
CERTIFICATE OF COMPLETION
Craig Kormylo
This document certifies that this individual has passed a comprehensive examination and is now a
Qualified lndividual (Ql) as defined in Section 8.3 of ASTM D7036-04 for the following method(s):
Source Evaluation Society Group 1z EPA Manual Gas Volume and Flow Measurements and lsokinetic
Particulate Sampling Methods
Certifi cate Number: 043-2020-3
-*/4,-cz DATE OF ISSUE: 1213'1120
Tate Strickler, VP - Quality Systems
DATE OFEXPIRATION: 12130125
M$PNTNTJ
GW43 AS-O227 22-RT- I 298 Page 276 of 278
CERTIFICATE OF COMPLETION
Craig Kormylo
This document certifies that this individual has passed a comprehensive examination and is now a
Qualified Individual (Ql) as defined in Section 8.3 of ASTM D7036-04 for the following method(s):
Source Evaluation Society Group 5: Part 75 CEMS RATA Testing
Certificate N umber:..Q!!!@[
-* r/t--,rcz DATE OF ISSUE: 12130120
Tate Strickler, VP - Quality Systems
DATE OF
EXPIRATION: 12129125
m$PNIm[q
GPO43 AS-O227 22-RT- 1 298 Page 277 ol 278
This is the Last Page of This Document
If you have any questions, please contact one of the following
individuals by emai! or phone.
Name: Craig Kormylo
Title: District Manager
Region: USA - Stack - Great Plains - Operations
Email: [e-mail]
Phone: [phone]
Name: GIen Capra
Title: Vice President
Region: USA - Stack
Email : [e-mail]
Phone: (5L2) 772-6450
.,YJffi,,,friiilr?il^i,;
1,.,,r _1ZU,t_3
DiVISION OF AIR QUAL'TY
G P04 3AS -0 22 7 22-RT - L298 Page 278 of 278