DAQ-2025-001952

1

DAQC-355-25
Site ID 10335 (B4)

MEMORANDUM

TO: STACK TEST FILE – TESORO REFINING AND MARKETING COMPANY –
Salt Lake City Refinery

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Paul Morris, Environmental Scientist

DATE: April 8, 2025

SUBJECT: Source: Ultraformer Unit Furnace F-1 and Crude Unit Furnace H-101
Contact: Rheannon Schaefer– 801-366-2033
Location: 474 West 900 North, SLC, Salt Lake County, Utah
Test Contractor: Alliance Technical Group, LLC
Permit/AO#: AO DAQE-AN103350075-18, dated January 11, 2018
FRS ID# UT000000493500004
Action Code: TR
Subject: Review of Revised Stack Test Report Received April 1, 2025
On April 2, 2025, Utah Division of Air Quality (DAQ) received reports for the Ultraformer Unit Furnace
F-1 and Crude Unit Furnace H-101. A test was performed on February 17-18, 2025, to demonstrate
compliance with emission limits as defined in conditions II.B.3.a. The test results are as follow:

Source Test Date Pollutant DAQ Result Test Result Limit

F-1 2/17/2025 NOx 0.036 lb/MMBtu 0.036 lb/MMBtu 0.065 lb/MMBtu

H-101 2/18/2025 NOx 0.044 lb/MMBtu 0.044 lb/MMBtu 0.054 lb/MMBtu

DEVIATIONS: No deviations reported.

CONCLUSION: The source appears to have been operating in compliance with the
applicable emission limit at the time of testing.

RECOMMENDATION: None.

HPV: No.

ATTACHMENTS: Revised stack test report received April 2, 2025, and DAQ generated
spreadsheets.

6 3
,
/m\\-.-,9!/.
salt Lake city Refinery
474 West 900 North
salt Lake city, UT 84103-1494
Tesoro Refining &
Marketing Company LLC
ET.IVITTOI{MEMA AUUTY
APR - 2 2025
DM8ION OF AR
A
April 1,2025
Bryce Bird, Director
Division of Air Quality
Department of Environmental Quality
195 North 1950 West
P.O. Box 144820
Salt Lake ciry, uT 84114-4820
Tesoro Refining & Marketing Company LLC
Salt Lake City Refinery
Ultraformer Furnace F-l and Crude Furnace H-101 Ultra-Low NOx Burners
Nitrogen Oxides Emissions Performance Test Reports
FCCU WGS RATA Report CO, Oz, NOx, SOz
FCCU Regen RATA Report CO, Oz, COz
COBB RATA Report CO, Oz, NOx, SOz
Dear Mr. Bird:
Enclosed please find the 2025 Ultraformer Furnace Nitrogen Oxides Emissions
Performance Test Report conducted February 17,2025, the 2025 Crude Furnace Nitrogen
Oxides Emissions Performance Test report conducted on February 18,2025.
The Ultraformer Furnace had an average emission rate of 0.036 lb/l\4MBtu NOx
compared to the 0.065 lb/MMBtu NOx limit listed in AO DAQE-ANI03350075-18.
The Crude Furnace had an average emission rate of 0.044Ib/MMBtu NOx compared to
the 0.054 lb/MMBtu NOx limit listed in the AO DAQE-AN103350075-18.
These tests satisff AO DAQE-AN103350075-18 Condition II.B.3.a annual testing
requirement for the F-1 and H-l0l NOx emissions.
Also enclosed are the Relative Accuracy Test Audits (RATA) Reports for the primary
and redundant CO, Oz, NOx, and SOz Wet Gas Scrubber (WGS) analyzers, the primary
and redundant CO, Oz, and COz Regen analyzers and the primary and redundant set of
CO, Oz, NOx, and SOz Carbon Monoxide Boiler Bypass (COBB) analyzers.
Hand Delivered
I certiff that testing was conducted while the source was operating at the rate and/or
conditions specified in the applicable approval order, operating permit, or federal
regulation. During testing, the source combusted fuels, used raw materials, and
maintained process conditions representative of normal operations, and operated under
such other relevant conditions specified by the Executive Secretary. Based on
information and belief formed after reasonable inquiry, the statements and information
contained in the report are true, accurate, and complete.
Please contact Rheannon Schaefer at [phone] ifyou have any questions.
Sincerelv.
Wfr'(u.A,r**)
Dean Anderson
VP Refining
Salt Lake City Refinery
u'i.i\lt DlPn:i]-:,.][iiT ol:
ENVIIIONMENTAL OIJAUTY
llil .-trAt6l#
]ECHNICAL GROUP
Source Test Report
Marathon Petroleum Corporation
Tesoro Refining and Marketing Company
474 West 900 North
Salt Lake city, uT 84103
Source Tested: Crude Unit Furnace H-101 & Ultraforrner
Unit (UFU) Furnace F- I
Test Date: February 17 & 18,2025
Proj ect No. AST-2025 -03 62
Prepared By
Alliance Technical Group, LLC
3683 W 2270 S, Suite E
West Valley City, UT 84120
pd/lErrpe
TECIiNICAL GNOIJF:Sourcc Tcst Rcport
Test Program Summary
Resulatorr Info rmetion
Permit No.
Source Information
DAQE-AN103350075-18
Source Name
Crude Unit Furnace H-101
tlltraformer Unit (LIFI, Fumace F-l
Contect Informetion
Source ID
PS#I
PS#2
Target Parameter
NOx
NOx
Test Location
Marathon Petoleum Corporation
Tesoro Refrning and Marketing Company
474 West 900 North
salt Lake ciry, uT 84103
Facility Contact
Rheannon Schaefer
Rschaefer@marathonpetoleum. com
[phone]
Test Company
Alliance Technical Group, LLC
3683 W 22705, Suite E
West Valley City, I-ff 84120
Project Manager
Charles Horton
[e-mail]
(3s2) 663-7s68
Field Team Leader
Alan Jensen
alan j [e-mail]
(847)220-3e4e
QA/QC Manager
Kathleen Shonk
katie. [e-mail]
(812) 4s2478s
Report Coordinator
Delaine Spangler
delaine. [e-mail]
Report Reviewer
Sarah Perry
[e-mail]
AST-2025-0362 Tesoro - Salt Lakc City, UT Page i
Al 6.oiiCIJIJICAI ,GNC ]P Source Test Report
C ertifrc a tio n S t al e men t
Alliance Technical Group, LLC (Alliance) has completed the source testing as described in this report. Results apply
only to the source(s) and operating condition(s) that were tested during the specific test date(s) and time(s) identified
within this report. All results are intended to be considered in their entirety, and Alliance is not responsible for use of
less than the complete test report without written consent. This report shall not be reproduced in full or in part without
written approval from the customer.
To the best of my knowledge and abilities, all information, facts and test data are correct. Data presented in this report
has been checked for completeness and is accurate, error-free and legible. Onsite testing was conducted in accordance
with approved intemal Standard Operating Procedures. Any deviations or problems are detailed in the relevant
sections ofthis test report.
This report is only considered valid once an authorized representative of Alliance has signed in the space provided
below; any other version is considered draft. This document was prepared in portable document format (.pdf) and
contains pages as identified in the bottom footer of this docurnent.
4t1t2025
Charles Horton, QSTI
Alliance Technical Group, LLC
Date
AST-2025-0352 Tesoro - Salt Lake City, I-l"f Page ii
r E C [1 I,J IC A I- G R O U P Source Test Repon
Table of Contents
TABLE OF CONTENTS
1.3 Site Specific Test Plan & Notification.................. ....................... l-l
3.1 U.S. EPA Reference Test Method 3A - Oxygen/Carbon Dioxide................... ...................... 3-l
3.2 U.S. EPA Reference Test Method 7E - Nitogen Oxides ............ 3-l
3.3 U.S. EPA Reference Test Method 19 - Mass Emission Factors ....................... 3-l
3.4 U.S. EPA Reference Test Method 205 - Gas Dilution System Certification. ........................3-l
3.5 Quality Assurance/Quality Control - U.S. EPA Reference Test Methods 3A and 7E................................ 3-2
LIST OF TABLES
Table 2-l: Summary of Results - PS#l ...........2-l
Table2-2: Surnmar of Results - PS#2......... .......................2-l
APPENDICES
Appendix A Sample Calculations
Appendix B Field Data
Appendix C Quality Assurance/Quality Control Data
Appendix D Fuel Factor Analysis
Appendix E Process Operating/Control System Data
AST-2025-0362 Tesoro - Sdt Lake City, UT
.nOl.F--Source Tesl Report
Introduction
1.0 Introduction
Alliance Technical Group, LLC (Alliance) was retained by Marathon Petroleum Corporation (NPC) to conduct
compliance testing at the Tesoro Refining and Marketing Company (Tesoro) Salt Lake City, Utah refinery. Portions
of the facility are subject to provisions of the Utah Departrnent of Environmental Quality, Division of Air Quality
(UDAO PermitNo. DAQE-ANI03350075-18. Testing was conducted as outlined in Table l-l below.
The data obtained for the UFU Furnace F-l was used to determine the correct emission factor for the NOx Cap
calculation per the annual requirement detailed in the permit as well as compliance with the 3-hour average NOx 0.065
lbA4MBtu limit detailed in the Tesoro Consent Decree lodged July 18, 2016.
Table l-1: Test Matrix
1.1 Facility Description
The Crude Unit Furnace H-l0l is equipped with ultra-low NOx burners and emissions are exhausted through one
stack designated as PS#l. The maximum fired heat capacity is no greater than 174 MMBtu/hr (LHV) based on a l-
hour average.
The Ultraformer Unit (UFU) Furnace is fued using plant gas and employs ultra-low NOx burners to control NOx
emissions. The UFU stack is tested once every calendar year to determine the correct emission factor for compliance.
1.2 Project Team
Personnel involved in this project are identihed in the following table.
Table l-2: Project Team
MPC Personnel Meannon Schaefer
Alliance Personnel Alan Jensen
Supilani Mailei
1.3 Site Specilic Test Plan & Notilication
Testing was conducted in accordance with the Site Specific Test Plans (SSTP) that were submitted to UDAQ by MPC.
Nitrogen Oxides (NOx)
Crude Unit Furnace H-lOl (PS#l)
Ultraformer Unit (IFII) Fumace F-l (PS#2)
AST-2025-0362 Tesoro - Salt Lake City, UT Page 1-l
tEe
r 11,
pJ/ta
Source Test Report
Summary of Results
2.0 Summary of Results
Alliance conducted compliance testing at the Tesoro facility in Salt Lake City, Utah on February 17 atd 18,2025.
Testing consisted of determining the emission rate of NOxat the outlets of the Crude Unit Furnace H-l0l (PS#l) and
the Ultraformer Unit (llFtD Furnace F-l (PS#2).
Tables 2- I and2-2 provide summaries of the emission testing results with comparisons to the applicable UDAQ permit
limits. Any difference between the summary results listed in the following tables and the detailed results contained in
the appendices is due to rounding for presentation.
Table 2-l: Summary of Results - PS#l
RunNumber Run 1 Run 2 Run 3 Averege
Date 2ll8,DS 2n8ns 2nBns
\itrogen Oxides Data
Concentration, ppmvd
Emission Factor, lbAdMBtu
Emission Limit, lb/IvIMBtu, 3-br average
Percent of Limit,%o
31.98
0.044
31.73
0.043
31.70
0.044
31.80
0.044
0.054
81
Trble 2-2: Summary of Results - PS#2
RunNumber Run I Run 2 Run 3 Averege
Date 21fin5 2tfin5 2n7ns
\itrogen Oxides Data
Concentration, ppmvd
Emission Factor, lb[v[MBtu
Emission Limit, lb/IvIMBtu, 3-hr average
Percent of Limit,%o
23.23
0.037
22.96
0.036
22.95
0.036
23.05
0.036
0.065
50
AST-2025-0362-001 Tesoro - Salt Lake City, UT Page 2- I
pill6rrce
TECI]I'JICAL GNOL] P Source Test Report
Testing Methodologt
3.0 Testing Methodology
The emission testing program was conducted in accordance with the test methods that are listed in Table 3-1. Method
descriptions are provided below, and quality assurance/quality contol data is provided in Appendix C.
Table 3-1: Source Testing Methodology
3.1 U.S. EPA Reference Test Method 3A - Oxygen/Carbon Dioilde
The oxygen (Oz) and carbon dioxide (COz) testing was conducted in accordance with U.S. EPA Reference Test
Method 3A. Data was collected online and reported in one-minute averages. The sampling system consisted of a
stainless-steel probe, Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas
conditioning system was a non-contact condenser used to remove moishue from the stack gas. If an unheated Teflon
sample line was used, then a portable non-contact condenser was placed in the system directly after the probe.
Otherwise, a heated Teflon sample line was used. The quality control measures are described in Section 3.5.
3.2 U.S. EPA Reference Test Method 7E - Nitrogen Oxides
The nitrogen oxides (NOx) testing was conducted in accordance with U.S. EPA Reference Test Method 7E. Data was
collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe, Teflon
sample line(s), gas conditioning system and the identified gas analyzer. The gas conditioning system was a non-
contact condenser used to remove moisture from the stack gas. If an unheated Teflon sample line was used, then a
portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample
line was used. The quality control measlues are described in Section 3.5.
3.3 U.S. EPA Reference Test Method 19 - Mass Emission Factors
The pollutant concentrations were converted to mass emission factors (lbA4MBtu) using procedures outlined in U.S.
EPA Reference Test Method 19. A recent fuel gas analysis was used to calculate a dry Ozbased F-Factor in accordance
with U.S. EPA Reference Test Method 19. The mass emission factor (lbA{MBtu) was calculated using the pollutant
concentration, Oz concenhation and the calculated F-Factor.
3.4 U.S. EPA Reference Test Method 205 - Gas Dilution System Certilication
A calibration gas dilution system field check was conducted in accordance with U.S. EPA Reference Method 205.
Multiple dilution rates and total gas flow rates were utilized to force the dilution system to perform two dilutions on
each mass flow controller. The diluted calibration gases were sent directly to the analyzer, and the analyzer response
recorded in an electonic field data sheet. The analyzer response agreed within 2% of the actual diluted gas
concentration. A second Protocol I calibration gas, with a cylinder concentration within l0% of one of the gas divider
settings described above, was intoduced directly to the analyzer, and the analyzer response recorded in an electronic
field data sheet. The cylinder concentration and the analyzer response agreed within 2%. These steps were repeated
three (3) times. Copies of the Method 205 data can be found in the Quality Assurance/Quality Conhol Appendix.
Instrumental AnalysisNitrogen Oxides
Mass Emission Factors
Gas Dilution System Certification
AST-2025-0362 Tesoro - Salt Lake City, UT Page 3-l
TICr]NIO.\al tl a'r l l iii Source Test Repon
Testing Methodologt
3.5 Quality Assurance/Quelity Control - U.S. EPA Reference Test Methods 3A and 7E
Cylinder calibration gases used met EPA Protocol | (+l- 2%) standards. Copies of all calibration gas certiflcates can
be found in the Quality Assurance/Quality Control Appendix.
Low Level gas was introduced directly to the analyzer. After adjusting the analyzer to the Low-Level gas
concentration and once the analyzer reading was stable, the analyzer value was recorded. This process was repeated
for the High-Level gas. For the Calibration Error Test, Low, Mid, and High Level calibration gases were sequentially
inboduced directly to the analyzer. All values were within 2.0 percent of the Calibration Span or 0.5 ppmv/% absolute
difference.
High or Mid-Level gas (whichever was closer to the stack gas concentation) was inhoduced at the probe and the time
required for the analyzer reading to reach 95 percent or 0.5 ppmv/% (whichever was less restrictive) of the gas
concentration was recorded. The analyzer reading was observed until it reached a stable value, and this value was
recorded. Next, Low Level gas was introduced at the probe and the time required for the analyzer reading to decrease
to a value within 5.0 percent or 0.5 ppmv/% (whichever was less restrictive) was recorded. If the Low-Level gas was
zero gils, the response was 0.5 ppmv/% or 5.0 percent of the upscale gas concenhation (whichever was less restrictive).
The analyzer reading was observed until it reached a stable value and this value was recorded. The measurement
system response time and initial system bias were determined from these data. The System Bias was within 5.0
percent of the Calibration Span or 0.5 ppmv/oZ absolute difference.
High or Mid-Level gas (whichever was closer to the stack gas concentation) was intoduced at the probe. After the
analyzer response was stable, the value was recorded. Next, Low Level gas wils introduced at the probe, and the
analyzer value recorded once it reached a stable response. The System Bias was within 5.0 percent of the Calibration
Span or 0.5 ppmvlYo absolute difference or the data was invalidated and the Calibration Error Test and System Bias
were repeated.
Drift between pre- and post-run System Bias was within 3 percent of the Calibration Span or 0.5 ppmv/o/o absolute
difference. If the drift exceeded 3 percent or 0.5 ppmv/%, the Calibration Error Test and System Bias were repeated.
To determine the number of sampling points, a gas stratification check was conducted prior to initiating testing. The
pollutant concentrations were measured at six traverse points. Each traverse point was sampled for a minimum of
twice the system response time.
If the pollutant concentration at each traverse point did not differ more than 5 percent or 0.5 ppmv/0.3% (whichever
was less restrictive) of the average pollutant concentration, then single point sampling was conducted during the test
runs. If the pollutant concentration did not meet these specifications but differed less than l0 percent or 1.0 ppmv/0.5%
from the average concentration, then three (3) point sampling was conducted (stacks less than 7.8 feet in diameter -
16.7, 50.0 and 83.3 percent of the measurement line; stacks greater than 7.8 feet in diameter - 0.4, 1.0, and 2.0 meters
from the stack wall). If the pollutant concentration differed by more than l0 percent or 1.0 ppmv/0.5% from the
average concentration, then sampling was conducted at a minimum of twelve (12) traverse points. Copies of
stratification check data can be found in the Quality Assurance/Quality Control Appendix.
An NOz - NO converter check was performed on the analyzer prior to initiating testing and at the completion of
testing. An approximately 50 ppm nitrogen dioxide cylinder gas was introduced directly to the NOx analyzer and the
AST-2025-0362 Tesoro - Salt Lake City, UT Page 3-2
put6rpe
#:;:;;;y;;TECIlNICAL GROUP
instnrment response was recorded in an electonic data sheet. The instnrment response was within +/- l0 percent of
the cylinder concentation.
A Data Acquisition System with battery backup was used to record the instrument response in one ( 1) minute averages.
The data was continuously stored as a *.CSV file in Excel format on the hard drive of a computer. At the completion
of testing, the data was also saved to the Alliance server. All data was reviewed by the Field Team Leader before
leaving the facility. Once arriving at Alliance's office, all written and electonic data was relinquished to the report
coordinator and then a final review was performed by the Project Manager.
AST-2025-0362 Tcsoro - Salt Lake City, l.I"f Pagc 3-3
Example Calculations
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Ultraformer Unit Furnace F-l
Project No.: AST-2025-0362-001
Run No. /lVlethod Run I / Method 3A
Or - Outlet Concentration (Cs), %i dry
co.= (co6,_ce)x ,affc;l
where,Cou. 7.49 = average analyzer value during test, o/o dry
C"-:T-: average of pretest & posttest zero responses,Yo dry
CMA-Tf:OF: actual concenhation of calibration gas,Yo dry
CM-T[96-: average of pretest & posttest calibration responses, 0/o dry
Cs"-7Tl-: Oz Concentration, % dry
COz - Outlet Concentration (CsoJ, Y" dry
where,
cco,= (co5.-cs)x , afftll
Cob, 8.10 : average analyzer value during test, oZ dry
C"-:0-: average of pretest & posttest zero responses,Yo dry
CMA
-T090-:
actual concentration of calibration gas, %o dry
CM
-TIIG[-
: average of pretest & posttest calibration responses, 0/o dry
Ccq-fr0T-: COz Concentration, o/o dry
=taAIIGE)Example Calculations
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source:
Project No.: AST-2025 -0362-001
Run No. /Itlethod Run I / Method 7E
NOx - Outlet Concentration (Cy6), ppmvd
where,
cNo*: (cos.-cs)x , ffanl
Cob, 23.6 : average analyzer value during test, ppmvd
C" --fi;l- : average of pretest & posttest zero responses, ppmvd
CM .-[.F= actual concentration of calibration gas, ppmvd
CM-[-: average of pretest & posttest calibration responses, ppmvd
CNg*-I-: NOx Concentation, ppmvd
NOx - Outlet Emission Factor (EFroro,J,lb/lVIMBtu
EFNo*ot =CNorxKxFdx
where,CNo* 23.2 : NOx - Outlet Concentration, ppmvd
K 120-tr6-: constant,lb/dscf 'ppmvdFd.Tftrs-: fuel factor, dscflMMBtuCs,-Tl- : oxygen concentation, oZ
EFNonod
-[5T7-
= lb/]vIMB tu
Al6rrEE)Emissions Calculations
Location MPC-Tesoro - Salt Lake City Refinery, UT
Source Crude Unit Furnace H-l0l
Project No. A5T-2025-0362-001
Run Number Runl Run2 Run3 Average
Date 2ll8l25 2ll8l25 2ll8l25
Start Time 10:35 ll:46 12:55
Stop Time I l:35 12:46 13:55
Source Data
Fuel Factor (O2 &v). dscf/IrdMBtu Fd 8,522 8,535 8,535 8,531
Cdculated Data - Outlet
Oz Concenhatiot,Yo dry co" 5.49 5.33 5.39 5.41
COz Concentration, % dry cco, 9.09 9.18 9.16 9.14
NOx Concentation, ppmvd
NOx Emission Factor, lbA,IMBtu (O2d)
CNo,
EFNor oza
3 1.98
0.044
3 1.80
0.044
3t.73
0.043
31.70
0.044
pllIAIEE)
',[:')r]l-'
Runl-RMData
Ifi.do!:
Sore:
Prclcct No.:
I)ttc:
TIDC
Uult
(}r- Od.t COr- Ord.r
%.i[y %iify
NOr - Oud.t
pPWd
Vdid
AYGratc
Cd GI ConcaErdo! (Cu)
Prctcrt SftcE ZGrc Rrrpom
Podtst SyrtGE z.rc Rdpou
AEntG Z.rc R.sponrc (Co)
Prrt6t SyrtGE Cd RspouC
Porttat Syttcr Cd Rapoilc
Avcngc €d Rcqorrc (Cy)
Corot dnu
l0:35
l0:36
l0:37
l0:38
l0:39
t0:,l()
l0:41
l0:42
10:43
10:tl4
l0:45
l0:46
l0:47
l0:4t
l0:49
l0:50
l0:51
l0:52
l0:53
l0:Stl
l0:55
l0:56
l0:57
l0:58
l0:59
I l:00
I l:01
ll:02
I l:03
I l:O4
I l:05
I l:06
I l:07
I l:08
I l:09
I l:10ll:ll
t l:12
I l:13
I l:14
I l:15
I l:16
I t:17tl:lt
I l:19
I l:20
I t;21
ll:22
ll:23
ll:24
I l:25
ll:26
ll:27
ll:2E
ll:29
ll:30
ll:31
ll:32
ll:33
I l:34
ll.m
0.09
0.13
0.1 I
10.94
10.96
10.95
5.49
5.12
5.12
5;t'l
5.55
5.56
5.E2
5.53
5.4
5.57
5.50
5.54
5.53
5.50
5.54
5.60
5.61
5.60
5.57
5.54
5.57
5.56
5.53
5.53
5.53
5.55
5.54
5.56
5.56
5.54
5.56
5.53
5.14
5.54
5.53
5.50
5.51
5.53
5.51
5.46
5.41
5.44
5.42
5.42
5.45
5.44
5.51
5.32
5.33
5.56
5.5E
5.36
5.48
5.6r
5.51
5.45
5.40
5.44
5.45
5.45
5.41
10.90
4.06
-0.05
{.06
I 1.00
I 1.02
I 1.01
9.09
9.05
t.99
9.00
9.14
9.t2
E.93
9.16
9.04
9.13
9.11
9.15
9.16
9.lE
9.14
9.13
9.r2
9.t2
9.14
9.16
9.r3
9.14
9.t7
9.16
9.rt
9.lE
9.t7
9.rt
9.t7
9.r8
9.t1
9.t8
9.17
9.19
9.18
9.20
9, l9
9.19
9.19
9.22
9.24
9.23
9.2s
9.21
9.21
9.24
9.20
9.30
9.29
9.16
9.t8
9.27
9.21
9.t7
9.24
9.24
9.27
9.24
9.23
9.21
9.21
50.00
0.02
0.00
0.01
49.62
50.06
49.U
31.98
lt.92
31.86
32.01
31.t7
31.80
31.11
32.14
3t.7',|
32.02
3t.76
31.il
31.71
31.70
31.61
31.t5
3t.71
31.t3
31.85
3t.75
3t.7E
31.78
31.7t
3 1.78
31.t5
31.93
32.0t
32.01
31.99
11.97
31.95
31.96
3 1.96
31.93
31.t9
3 t.t3
3t.15
31.il
lt.'19
3 t.t4
31.93
31.95
3r.92
31.E9
31.il
31.80
31.t0
3l.tE
3t.u
3 l.t2
12.t5
31.95
31.83
32.t9
32.24
12.M
3 1.93
31.t9
3 1.96
31.93
3 1.85
plll6rrpE)
TrCIr.,:-,Fr')irP
Run2-RMData
Soucc:
PTJGCt No.:
Drtc:
Ircrdonr MPC-T@rc -
AYETgG
Cd G.r CoD6E do! (C&J
hrt6t SyttcE z.rc Rdpom
Porttgt SyrtcE Zm Rqpore
Avcng. Zcrc RsDou (Co)
Prctqt SyttrE Cd Rcryouc
Porttst Syrt@ Cd Rdportc
Avlngc Cd RcrDoEtc (Cx)
Corotcdnu
TIEudt
I l:46
ll:41
I l:48
I l:49
I l:50
t l:51
I l:52
I l:53
ll:54
ll:55
I 1:56
I t:57
I l:58
I t:59
l2:00
l2:01
12:02
l2:03
l2:M
l2:05
12t06
12:01
l2:08
l2:09
l2: l0
l2:l I
17,:12
12:13
l2tl4
l2:15
l2:16
l2tl7
l2:1 6
l2:19
12t2o
12:21
12:22
l2:23
l2:24
12125
12:26
12i27
l2:28
12:29
l2:30
t2:31
l2:32
l2:33
12t14
l2:35
l2:36
l2:37
l2:3E
l2:39
12:40
12t4l
12142
ll:11
l2:44
l2:15
(}r- O[d.t
'/. ajr!
5.38
lt.m
0.13
0.14
0.14
I0.96
10.96
10.96
5.47
5.46
s.41
5.51
5.49
5.47
5.45
5.48
5.49
s.49
5.52
5.54
5.51
5.52
5.50
5.44
5.35
s.!1
5.35
5.35
5.34
5.31
5.31
5.29
5.29
5.27
5.24
5.28
5.30
s.2t
5.25
5.25
5.32
5.34
5.35
5.35
s.36
5.35
5.3t
5.42
5.43
s.45
5.44
5.11
5.12
5.32
5.30
s.35
5.38
5.3E
s.3t
5.r'l
5.36
5.36
5.36
5.36
5.37
5.38
5.41
5.40
9.26
10.90
-o.05
{.05
-0.05
I1.02
I 1.00
I t.0l
9.20
9.21
9.20
9.15
9.19
9.19
9.2t
9.20
9. l9
9.20
9.19
9.lt
9.19
9.19
9.19
9.24
9.28
9.29
9.2E
9.28
9.2t
9.28
9.31
9.33
9.r2
9.31
9.35
9.32
9.31
9.32
9.33
9.!1
9.29
9.30
9.29
9.28
9.28
9.28
9.25
9.24
9.23
9.24
9.23
9.28
9.29
9.30
9.31
9.26
9.27
9.27
9.28
9.2'l
9.2t
9.21
9.28
9.28
9.27
9.27
9.23
9.26
31.6
50.00
0.m
0.01
0.01
50.06
49.74
49.90
tt-71
31.0E
lt.41
3t.41
31.55
31.55
,1.52
,t.57
3 1.65
31.69
11.67
31.E2
3 l.t4
31.75
31.70
31.78
31.75
31.70
31.70
31.81
31.75
31.?t
rL12
31.7t
31.73
31.7t
3t.16
tt.72
31.70lt.6
31.73
31.73
1t.73
3t.75
31.74
3 l.6t
31.70
1t;15
31.6E
1t;13
31.56
,t.12
3 1.76
11.74
11.61
31.5E
31.55
31.53
31.55
3 l.6trt.6
31.69
31.71
31.59
31.60
31.67
3 r.6t
31.70
1t.62
3t.61
1t.61
COr-Oud.t NOt-O!d!rY.dry pprYd
Run3-RMData
Iartioa:
Sore;
Pmjcst No.:
Drtc:
TIDG
Uilt
Strtr.
(}'-Ord.It CO'-Oudct
'/.iky %iitryVrlid Valid
NO!- Ord3t
ppEvd
Arcrrgc
Cd Gr CoD€trtdo! (Cei)
P?.tc.r SyrtcE Zcrc Rdpoe
Porttgt SyrtGE ZGrc R6pou
Av.ngc rc R6pom (Co)
Prctdt Syltcn Cd Rcrpouc
Porttcrt SyltcE Cd Rapouc
Avcngc Crl Rsponrc (Cx)
Coretrd Ru!
l2:55
12t56
12:51
l2:58
12:59
l3:00
l3:01
l3:02
l3:03
l3:fi
l3:05
l3:05
l3:07
l3:08
l3:09
13: l0
l3:l I
l3:12
l3:13
13: l4
l3: l5
l3: l5
l3; l7
l3:1 8
l3: l9
l3:20
l3:21
l3:22
l3:23
13:24
l3:25
13:26
13t27
l3:28
l3:29
l3:30
l3:3 I
13:32
t3:33
l3:34
l3:35
l3:36
13:37
l3:38
l3:39
l3:40
l3:41
13:42
13:43
l3:,14
l3:45
l3:46
13:47
l3:4t
l3:49
l3:50
l3:51
13152
l3:53
l3:54
5.44
I 1.00
0.14
0.t5
0.15
10.95
10.96
10.96
9.23
10.90
-0.05
-0.0t
4.0?
11.00
10.99
I 1.00
9.24
9.21
9.24
9.26
9.25
9.27
9.26
9.24
9.22
9.23
9.25
9.24
9.25
9.25
9.23
9.23
9.22
9.22
9.22
9.22
9.22
9.23
9.22
9.24
9.24
9.21
9.25
9.24
9.26
9.24
9.24
9.25
9.26
9.26
9.28
9.26
9.26
9.25
9.2s
9.2',1
9.26
9.25
9.26
9.2s
9.2s
9.09
9.04
9.30
9.t6
9.24
9. l6
9.13
9.25
9.0t
9.21
9.15
9.t7
9.21
9.06
9.21
31.60
50.00
0.01
0.01
0.01
49.74
49.94
49.84
5.42
5.44
5.43
5.3t
5.39
5.36
5.39
5.45
5.47
5.45
5.4r
5.42
5.41
5.42
5.43
5.45
5.44
5.46
5.46
5.47
5.45
5.45
5.45
5.44
5.43
5.39
5.41
5.42
5.42
5.42
5.44
5.41
5.42
5.41
5.37
5.40
5.40
5.40
5.39
5.17
5.39
5.41
5.40
5.40
5.40
5.61
5.6t
5.31
5.4E
5.44
5.52
5.62
5.39
5.66
5.43
5.55
5.5'l
5.43
5.6',1
5.50
31.38
31.50
31.5t
31.55
31.59
31.58
31.56
3 t.5E
3 r.55
31.t2
31.71
31.65
3t.61
3t.65
31.69
3 1.70
31.63
3 1.66
31.6E
31.613t.a
3t.62
3 1.60
31.60
31.53
31.51
31.52
31.59
3t.52
31.56
31.55
31.60
31.61
31.65
31.5t
3t.57
31.52
3 1.53
31.4t
31.51
31.45
31.52
lt.67
3 1.60
31.61
tl.44
31.6t
3 1.66
tt.46
31.63
3 1.60
3 t.75
31.53
31.71
31.76
3t.il
tt.74
31.54
31.59
3t.73
rEE)'. ,.|=TAAI Emissions Calculations
Location MPC-Tesoro - Salt Lake City Refrnery, UT
Source UlEaformer Unit Furnace F-l
Project No. A5T-2025-0362-00 I
Run Number Runl Run2 Run3 Average
Date
Start Time
Stop Time
2lt7l2s 2lt7l2s 2ll7l25
13:57 15:10 16:23
14:57 16:10 17:23
Source Data
Fuel Factor (O2 drv). dscflMMBtu Fd 8,485 8,491 8,490 8,489
Celculated Data - Outlet
Dz Concentration, % dry coo 7.47 7.40 7.4t 7.43
COz Concentr ation, %o dry cco, 8.01 8.04 8.02 8.03
NOx Concentation, ppmvd
NOx Emission Factor, lb/IvIMBtu (O2d)
CNo*
EFNor oza
23.23
0.037
22.96 22.9s
0.035 0.036
23.05
0.035
Runl-RMData
lrsdonr
Sowcc:
Pnlcct No.:
Irrtc:
Ttm
Uilt
O.-Oudct COr-Oudct NOr-Ord.t
'Adty 'A&! ppmd
UEcorectcd Rm AvGrr8G (Ce)
Cd Gil Co[cmErdon (CM)
PE6t SyttrE Zcro R6pom
PoattBt SyttcE Z.ro RsDoM
Avmgc Zcrc Rc4om (Co)
h6t SynGD Cd Rctpom
Po$tat SyrtcE Cd Rdpors
AYrngG Cd Rspo!rc (Cx)
l3:57
l3:5t
l3:59
l4:00
l4:01
l4:02
l4:03
l4:04
l4:05
l4:06
l4:07
l4:08
l4:09
l4: l0
l4:ll
l4:12
l4: l3
14:14
l4: l5
l4: l6
l4:17
l4:18
l4; l9
14tzo
14t2l
l4:22
l4:23
l4:24
l4:25
l4:26
l4:27
l4:28
l4:29
l4:30
l4:31
l4:32
l4:33
l4:34
l4:35
l4:35
l4:3'l
l4:38
l4:19
l4:40
l4:41
l4:42
l4:43
14:44
l4:15
l4:46
14t4'l
t4:4E
14149
l4:50
l4:51
l4:52
14:53
l4:54
l4:55
l4:56
7.49
I 1.00
0.15
0.17
0.16
10.94
10.97
10.96
1
7.54
7.50
7.50
7.46
7.4E
7.52
7.51
7.50
7.!4
7.52
7.67
7.61
7.46
7.38
7.17
7.45
7.49
7.50
1.53
7.56
7.56
7.53
7.53
7.50
7.51
7.46
1.54
7.52
1.55
1.49
1.42
1.40
't.43
7.46
7.51
7.59
7.55
7.53
7.61
7.63
't.48
1.35
1.34
1.4t
1.48
't.41
7.46
7.48
7.4t
7.50
7.51
?.50
7.41
1.43
7.38
7.42
7.45
7.50
7.4't
7.41
6.10
10.90
-0.01
-0.04
4.03
I1.03
I1.04
ll.M
8.04
t.05
8.06
t.09
t.0E
8.04
t.05
8.08
8.16
t.05
7.98
8.02
8.1 I
t.l5
8. t5
t.t I
E.09
8.09
t.07
8.05
t.06
8.08
t.0t
t.l0
8.09
E.l2
8.07
t.08
8.08
t.t I
E. l4
8.r5
t.t3
8.12
t.0t
8.05
t.06
t.09
t.03
t.03
E.l3t.tt
t. l9
t.l5
t.l I
E.l2
8.12
E.l2
t.l2
t.l I
8.08
t.l t
8.t2
t.t4
8.18
t. l6
E.l5
t.rI
E.l4
8.14
50.00
0.29
0.43
0.36
50.64
50.25
50.45
23.23
23.t6
23.72
23.t5
23.70
23;70
23.il
23;14
23.96
23.61
23;10
24.01
23.96
23.84
23.65
23.30
23.65
23.44
23.51
23.65
23.19
27;12
23.56
23.t3
23.82
21.79
23.59
23.76
21.46
23.50
23.52
23.53
23.43
21.29
23.24
21.79
21.83
23.87
23.10
23.74
23.t9
23.66
23.36
23.27
23.40
23.45
23.58
21.64
23.60
23.61
23.52
23.59
23.64
23.s9
23.45
21.34
23.34
23.4t
23.59
23.62
23.52
AI Run2-RMData
Inrdo!: MPC-T@rc - Sslt t tc Cisoue,ffiEEffiffit
PrcJcct No,:
Ir.tc:
TIDC
udr
Or-Oud.t COr-Oudct%iJr! ' dry
NOr - OctLt
ppmd
Vslid
U!@retcdRuAren8c
Cd Grr CoDcarrdo! (Cu)
Prctcrt SyttcE Zrro Rctpo!*
Potttdt Sylt E ro Rdpouc
AvcnSc Zcro RdpoLrc (Co)
Prctdt Sylt m Cd Rcrpo4
PornEt SystlE Cd R6pom
Awngc Cd Rc{oe (CJ
l 5:10
l5:l I
l 5:12
l 5:13
I 5:14
l 5:15
l 5:16
l5: l7
l5:lE
l5: l9
l5:20
l5:21
l5:22
l5:23
l5:24
l5:25
l5:26
l5:27
l5:2t
l5:29
l5:30
l5:3 I
15:32
l5:33
l5:34
l5:35
l5:36
l5:37
l5:3E
l5:39
l5:40
15:41
15t42
l5:43
l5:44
l5:45
l5:46
15:4'l
l5:4t
l5:49
l5:50
l5:51
l5:52
l5:53
l5:54
l5:55
I 5:56
15:5'l
l5:5t
l5:59
l6:00
l6:01
l6:02
l6:03
l6:04
l6:05
t6:06
t6:07
t6:0t
t6:09
I 1.00
0.17
0.18
0.r6
10.97
10.96
10.97
7.4
7.48
7.46
7.46
7.4
7.45
7.41
7.42
7.40
7.36
7.3E
7.42
7.46
7.45
7.42
7.41
7.48
1.53
7.49
7.46
't.43
1.40
1.41
't.45
7.4t
7.46
1.45
7.43
1.44
1.46
't.46
1.46
7.44
1.41
7.4t
7.45
7.42
1.44
1.44
7.42
7.40
7.40
7.13
7.4t
7.47
7.44
7.4't.&
7.42
7.46
7.44
?.39
7.44
7.46
7.41
7.40
7.41
7.40
7.41
7.43
7.39
10.90
-0.04
-0.02
-0.03
It.u
I t.06
I 1.05
8.04
50.00
0.43
0.46
0.45
50.25
50.r9
50.22
22.96
8.13
t.t4
E. t5
8. t6
t.r5
t.r4
E.l5
8.18
8.2r
E.IE
t. t7
t.l4
E.l5
t.l7
t.l7
8.13
t. l0
E.l3
E.l4
8.16
t.l7
8.16
8. l5
t. t3
E.l4
t.r4
8.16
t.l4
t.l4
8.15
8. l5
8.15
8.r2
t.t2
E.t3
8. l6
E.l4
t. l4
E.l5
t.r6
E.r6
E.l5
t. t2
t. l2
8.14
t.l5
E.l5
t. r4
t. t2
8. r3
t.tE
t. r3
t.t t
8.15
t. t5
E.l4
8. r5
8.t4
t.r3t.rt
23.06
23.t4
23.05
23.12
23.31
21.42
21.29
23.33
23.29
23.33
23.10
23.45
23.50
23.56
23.56
21.4t
23.62
21.66
23.62
23.5'1
23.34
2320
23.39
23.53
23.62
21.61
21.69
8.50
23.45
23.61
23.64
23.47
23.34
23.39
23.39
21.29
23.46
23.26
23.25
23.01
23.t t
23.26
23.21
21.4t
232't
23.22
23. t0
22.93
22.9'7
23.10
22.96
23.03
23.05
22.93
23.t2
23.t3
23.05
23.t9
23.22
22.97
Run3-RMData
tcrdo!: MPC-Tffi - Srlt L8kr Citv Rcfucry, UT
Sorro: Ultr8foffi Unit Fmec F-l
Prclcct No.:
Drtc:
Tle
Unlt
O' - Oudct
%&v
vdid
COr-Oud.t N(}r-Ord.t%dry ppwd
Avcrrgr
Cd G.r ColsErdo! (Crr)
Prttst Syrtcm Zcrc Rqponrc
Poattst SyttlE Zaro Rdpouc
Avcmgc Zerc Rcrpouc (Co)
PrttstSyrt DCdR.qom
Portt6t SyrtcD Cd R6pou
Avcngc Cd Rspou (Cr)
1.45
ll.m
0.18
0.17
0.lE
10.96
10.98
10.97
t.t5
10.90
-0.02
-0.03
-0.03
I t.06
I l.t0
I 1.08
8.15
t.t3
t.r4
E.t7
8.15
t.l5
8. t6
8. t5
8.14
t.t5
t.l5
t.l5
t.t6t.l4
t.r5
t.t4
t.l3
8.14
8.14
t. l4
t. l4
8.17
8. r6
8.15
t.l3
8.t3
t.l4
E.l5
t.l3
E.l5
t.l5
8. t5
t.t5
t.l5
8.14
t.l4
8.14
t.l4
E.l4
t. t7
E. l7
E.l7
t.l5
t.t2
t. r5
E.l6
8.lt
t.l4
8. t3
t.t5
E. l6
t. r6
E. l6
t.l?
E.l8
8. r7
t.l6
t.t6
8. l6
t. r6
50.00
o.46
0.42
0.44
50.19
50.22
50.21
7.4 71
l6:23
l6:24
l6:25
l6:26
l6:27
l6:2t
t6..29
l6:30
l6:31
l6:!2
l6:33
l6:34
l6:35
l6:36
l6:37
l6:3E
l6:39
1,6:40
l6:41
16t42
l6:43
l6:44
t6:45
l6:46
16147
l6:4t
16:49
t6:50
l6:51
l6:52
l6:53
l6:54
l6:55
t6:55
l6:57
l6:5t
l6:59
l7:00
l7:01
17:02
l7:03
11:04
l7:05
l7:06
17:O7
l7:08
l7:09
1,7: l0
l7:ll
17:12
l7: l3
t7: l4
l7:1 5
17:16
l7tl7
l7:lt
l?:19
17:2O
11:21
17:22
1.19
7.43
7.44
7.40
7.41
1.43
't.41
7.42
7.44
1.43
1.44
1.44
7.42
7.45
7.16
1.44
1.45
7.44
7.4
7.45
7.15
1.42
't.42
7.44
7.45
7.48
1.46
7.47
't.47
1.45
't.44
7.46
7.46
1.46
't.46
7.47
7.47
7.4t
?.4E
7.42
1.40
7.41
7.,18
7.50
7.46
7.46
't.44
7.4t
7.50
7.4t
7.46
7.15
7.45
't.41
7.41
'1.44
7.47
7.47
1.46
7.11
22.6t
22.E0
2!.09
22.96
23.05
22.91
22.95
23.06
23.01
23.05
21.13
23.00
23.14
23.13
21.t3
212E
2).41
23.33
21.12
23.31
21.11
23.31
23.5t
23.34
23.25
23.27
23.15
21.44
23.41
23.32
23.36
23.50
23.29
23.2t
21.42
23.34
23.22
23.36
23.45
21.4t
23.50
21.22
23.36
23.29
23.46
21.!7
21.36
23.2t
23.48
23.36
23.3E
23.46
23.38
21.47
23.r8
23.29
23.23
23.47
23.40B.q
TEE)=laAI QA Data
Location MPC-Tesoro - Salt Lake CiW Refinerv, UT
Source Crude Unit Furnace H-l0l
Project No. AST-2025-0362-001
Parameter Or - Outlet COr - Outlet NOx - Outlet
Make
Model
s/N
Ooeratins Rense
Servomex
4900
t00269
2s
Servomex
4900
100259
100
Thermo
42iQ
1,2327730s21
100
Cylinder ID
7*ro
Low
Mid
Hiph
NA
NA
RR02538
EB0069884
NA
NA
RR02538
EB0069884
NA
NA
EB00l 1606
E8001 1606
Cylinder Certilied Values
Z,ero
Low
Mid
Hish
NA
NA
I1.00
23.99
NA
NA
10.9
23.9
NA
NA
s0l
501
Cylinder Expiration Date
Znro
Low
Mid
Hieh
NA
NA
9^9/3r
4/U32
NA
NA
9n9/31
4/1132
NA
NA
9lt6/31
9n6/31
Tvpe of Samnle Line Heated Line
Response Times
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Crude Unit Fumace H-l0l
Project No.: AST-2025 -03 62-001
seconds
Paremeter Or - Outlet CO: - Outlet NOx - Outlet
7*ro
Low
Mid
Averase
30
NA
30
30
NA
30
60
NA
60
30.0 30.0 60.0
FTAAI Calibration DataIEE)
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Crude Unit Fumace H-101
Proj ect No.: AST-2025 -03 62-001
D*e:2/18/25
Parameter O, - Outlet COr - Outlet NOx - Outlet
Exoected Averese Concentration 6.00 9.00 40.00
Span Between
Low
High
Desired Soan
6.00
30.00
23.99
9.00
45.00
23.90
40.00
200.00
100.00
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
9.60
14.39
9.s6
t4.34
40.00
60.00
High Range Gas
Low
Hieh
NA
NA
NA
NA
NA
NA
Actual Concentration (o/o or PPm)
Z,ero
Low
Mid
Hish
0.00
NA
I 1.00
23.99
0.00
NA
10.90
23.90
0.00
NA
50.00
100.00
Resoonse Time (seconds)30.00 30.00 60.00
Upscale Calibration Gas (CuJ Mid Mid Mid
Instrument Response (% or ppm)
Zero
Low
Mid
Hish
0.00
NA
I 1.00
24.00
-0.0s
NA
I l.l6
23.83
0.00
NA
50.34
99.91
Performance (7, of Span or Cal. Gas Conc.)
7*ro
Low
Mid
Hish
0.01
NA
0.00
0.04
0.20
NA
1.09
0.29
0.00
NA
0.34
0.09
Linearity (7o of Span or Cal. Gas Conc.)
Status
7*ro
Low
Mid
Hieh
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
Bias/Drift Determinations
Location:
Source:
Project No.: AST-2025-0362-001
MPC-Tesoro - Salt Lake City Refinery. UT
Crude Unit Furnace H-l0l
Parameter Or - Outlet COr - Outlet NOx - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.09
0.13
t0.94
10.96
-0.06
-0.05
I1.00
I 1.02
0.02
0.00
49.62
50.06
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
0. l3
0.14
10.96
10.96
-0.0s
-0.05
I 1.02
I 1.00
0.00
0.01
50.06
49.74
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.14
0.15
10.96
10.96
-0.05
-0.08
I 1.00
10.99
0.01
0.01
49.74
49.94
Bias/Drift Determinations
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Crude Unit Fumace H-lOl
Project No.: AST-2025-0362-00 I
Peremeter O, - Outlet C0: - Outlet NOr - Outlet
Run I Dete 2ll8l25
Span Value
Initial Instrument Zero Cal Response
Initial lnstrument Upscale Cal Response
Final InstumentZero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
23.99
0.00
I 1.00
0.00
I 1.00
0.09
0. l3
10.94
10.96
23.90
-0.05
I 1.15
-0.05
I l.t6
-0.06
-0.05
I 1.00
I 1.02
100.00
0.00
50.34
0.00
50.34
0.02
0.00
49.62
50.06
Bias (%)
Praest Zero
Posttest Zero
Pretest Span
Posttest Span
0.37
0.54
-0.25
-0.17
-0.05
-0.01
-0.67
-0.59
0.02
0.00
-0.'72
-0.28
Drift(%)
Zerc
Mid
0.17
0.08
0.04
0.08
-0.02
0.44
Run 2 Date 2lltlzi
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstrrment Zero Cal Response
Final Insfument Upscale Cal Response
Pretest Systern Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale ResDonse
23.99
0.00
I 1.00
0.00
I 1.00
0.13
0. l4
10.96
10.96
23.90
-0.05
I l.l6
-0.05
I l.l6
-0.05
-0.05
1 1.02
1 1.00
r00.00
0.00
50.34
0.00
50.34
0.00
0.01
50.06
49.74
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.54
0.58
-0.17
-0.17
-0.01
-0.01
-0.59
-0.67
0.00
0.01
-0.28
-0.60
Drift(%)
Zero
Mid
0.04
0.00
0.00
-0.08
0.01
-0.12
Run 3 Date 2ll8l25
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstrument Zero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem l]nscale Resoonse
23.99
0.00
r 1.00
0.00
I 1.00
0.14
0. l5
10.96
10.96
23.90
-0.05
I l.l6
-0.05
I 1.16
-0.05
-0.08
I1.00
10.99
100.00
0.00
s0.34
0.00
50.34
0.01
0.01
49.74
49.94
Sias (%)
Jretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.s8
0.62
-0.l7
-0.17
-0.01
-0.1 3
-0.67
-0.71
0.01
0.01
-0.50
-0.40
Drift (%)
Zero
Mid
0.04
0.00
-0.13
-0.M
0.00
0.20
pur6lt QA Data
Location MPC-T".o
Source
Project Xo.
Paremeter Or - Outlet COr - Outlet NOx - Outlet
Make
Model
SN
Oneretinp Ranse
Servomex
4900
100269
25
Servomex
4900
t00269
100
Therrro
42iQ
12327730s2r
100
Cylinder ID
7*ro
Low
Mid
Hish
NA
NA
RR02s38
EB0069884
NA
NA
RR02538
880069884
NA
NA
EB00l 1606
EB00l 1606
Cylinder Certilied Values
Zero
Low
Mid
Hiph
NA
NA
I 1.00
23.99
NA
NA
10.9
23.9
NA
NA
501
501
Cylinder Expiration Date
7*to
Low
Mid
Hish
NA
NA
9lt9l3t
4nt32
NA
NA
9^9t31
4^132
NA
NA
9n6t3t
9^6/31
fvne of Samnle Line Heated Line
pllIATEE)
T E (l 11 li lCl A L (', R,:) Ll rl
Locstion: MPC-Tesoro - Salt Lake Citv Refinerv. UT
Response Times
Source: Ultaformer Unit Furnace F-l
Project No.: AST-2025 -0362-001
seconds
Parameter Or - Outlet COr - Ouflet NOx- Outlet
Znro
Low
Mid
Averase
30
NA
30
30
NA
30
60
NA
60
30.0 30.0 60.0
AI =tcrrEe
. r - a :'
Calibration Data
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Ultaformer Unit Furnace F-lSource:
Project No.:AST-2025-0362-001
Date:2ll'1125
Parameter O: - Outlet CO: - Outlet NOx - Outlet
Exnected Averase Concentration 9.00 10.00 2s.00
Span Between
Low
High
Desired Soan
9.00
45.00
23.99
10.00
50.00
23.90
25.00
12s.00
100.00
Low Range Gas
Low
Hieh
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
9.60
t4.39
9.56
t4.34
40.00
60.00
lligh Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Actual Concentration (7o or ppm)
Z,ero
Low
Mid
Hish
0.00
NA
I1.00
23.99
0.00
NA
10.90
23.90
0.00
NA
50.00
100.00
Resoonse Time (seconds)30.00 30.00 60.00
Uoscele Calibration Gas (C-^)Mid Mid Mid
lnstrument Response (% or ppm)
Z,ero
Low
Mid
Hish
0.00
NA
tt.02
24.00
-0.03
NA
I 1.19
23.87
0.01
NA
49.28
100.00
Performance (7o of Span or Cal. Gas Conc.)
Znro
Low
Mid
Hish
0.00
NA
0.08
0.04
0. l4
NA
l.2l
0. l3
0.01
NA
0.72
0.00
Status
Tnro
Low
Mid
Hioh
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
FTAAI Bias/Drift Determinations
a
tEe
i-,
Location:
Source:
Project No.:AST-2025-0362-001
MPC-Tesoro - Salt Lake CiW Refinery, UT
Ulhaformer Unit Furnace F-l
Parameter O, - Outlet COr - Outlet NOx - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0. l5
0.l7
10.94
t0.97
-0.01
-0.04
I 1.03
I1.04
0.29
0.43
s0.64
s0.25
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
0.17
0.18
10.97
10.96
-0.04
-0.02
11.04
I 1.06
0.43
0.46
s0.25
50.1 9
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0. l8
0.17
10.96
10.98
-0.02
-0.03
I1.06
I l.l0
0.46
0.42
50.19
s0.22
BiaslDrift Determinations
Locedon: MPC-Tesoro - Salt Lakc Citv Refrnerv. UT
Source: Ultaformer Unit Funrace F-l
Project No.: AST-2025-0362-00 I
Prrrmeter Or - Outlet COr - Outlet NOr - Outlet
Run I Dete zlfins
Span Value
lnitial lnstument Zcro Cal Response
Initial Instument Upscale Cal Response
Final lnstrument Zero Cal Response
Final Instrument Upscale Cal Response
Pretest Systern Zero Response
Posttest System Zoo Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
23.99
0.00
I 1.02
0.00
I 1.02
0.15
0. l7
10.94
10.97
23.90
-0.03
1 1.19
-0.03
I l.19
-0.0r
-0.04
I1.03
I 1.04
t00.00
0.01
49.28
0.01
49.28
0.29
0.43
50.64
50.25
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.63
0.71
-0.33
-0.21
0.10
-0.03
-0.67
-0.53
0.28
0.42
1.36
0.97
Drift(%)
Zero
Mid
0.08
0. l3
-0.13
0.M
0.14
-0.39
Run 2 Dete 2n7ns
Span Value
lnstnrment Zero Cal Response
lnstrument Upscale Cal Response
Final Instrument Zero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zcro Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
tt.02
0.00
I 1.02
0.17
0.18
10.97
10.95
23.90
-0.03
I l.l9
-0.03
l l.19
-0.04
-0.02
I 1.04
I 1.06
100.00
0.01
49.28
0.01
49.28
0.43
0.46
s0.25
50. l9
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.71
0.75
-0.21
-0.25
-0.03
0.05
-0.63
-0.54
0.42
0.45
0.97
0.91
Drift(%)
Zero
Mid
0.M
-0.04
0.08
0.08
0.03
-0.06
Run 3 Date 2ll7l2s
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final Instument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Postl€st Svstm I Jnscale Rmmnse
23.99
0.00
I 1.02
0.00
I 1.02
0.18
0.17
10.96
10.98
23.90
-0.03
I 1.19
-0.03
I 1.19
-0.02
-0.03
I 1.06
I 1.10
100.00
0.01
49.28
0.01
49.28
0.46
0.42
50.1 9
50.22
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Snan
0.75
0.7t
-0.25
-0.17
0.05
0.01
-0.54
-0.38
0.45
0.41
0.91
0.94
Driff (%)
Zero
vid
-0.04
0.08
-0.M
0.17
-0.04
0.03
PJI.Affid-l.
Accreditation ,162754
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shroveport, A 71107
800-551 -81 50
PGVP Vendor lD # G1.2024
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
-80069884
127907
1900 PS|G
:80069884 20240320-0
Certification Oate:
Expiration Oate:
MFG Facility:
Lot Number:
Tracking Number:
Previous Cerlification Dates:
)4103t2024
)4t01t2432
80069884 20240320
)84212711
This calibration standard has been certified per the May 2012 EPA Traceability -12t531,
inq orocedure G2
I
concentrauon Uncertalnty Analytlcal Prlnclple A$ayed On
23.9o/o
23.99 o/o
*:O.1 o/o
10.06 %
20 01 vo
24 76 0/o
Analytical lnstrumentation
02
co2 FTIR
Thermo
MKS
410r
MKS 2031DJG2EKVS13T
'r 152980025 03118D024
017146467 04n2n024
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This
calibration/test was performed usrng Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 950/0 confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
6qffrlu,"
Brittany Johnson
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revrsed on 2018-09-17
Red Ball Technical Gas Seryice
555 Craig Kennedy Way
Shreveport, LA 71107
800-551 -81 50
PGVP Vendor lD * G12o23
EPA PROTOCOL GAS CERTIFIGATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
RR02538
125371
1900 PS|G
RR02538 20230831-0
Certification Date.
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certifi cation Dates:
)9t21t2023
)9t19t2031
- Snreveoon - LA
1R02538 20230831
o3925t25
This calibration standard has been certified per the May 2012 EPA Traceability Protocol,12t531,
G1
Certified Concentration(s)
Dioxide
Concentratlon
1o.9 %
11.00%
Uncertalnty
*.0.',|1 0/o
10.03 %
Anatyfical Prlnciple
FTIR
MPA
Assayed On
o9t21t2023
09t18t2023Orygen
Balance
cc737012.20230228
EAOO22021 .20180323
1 162980025 09t18t2023
017146467 09D1t2023
SMART.CERT
This is to certity the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specifled or required calibrataon/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confldence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
fr,* e-h
Jasmine Godfrey
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revrsed on 2018-09-17
PJI/trydEta
Accreditation #62754
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 71107
800-551-8'150
PGVP Vendor lD # Gl2023
EPA PROTOCOL GAS GERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
:8001 1606
24235
1900 PS|G
:B001 1 606.20230906-0
Certification Date:
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certifi cation Dates:
)9t18t2023
)9/1 6/2031
- Shreveport - LA
:8001 1606.20230906
)25274639
his calibration standard has been certified per the May 2012 EPA Traceability Protocol, Documenl EPA-600/R'12/531,
ino orocedure G1.
Gertified Concentration(s)
Concentratlon Uncertalnty Analytlcal Prlnclple Assayed On
o9t11t20,f.l/9n8t2o,f.Nitric Oxide 501 P t3 PPM Chemiluminescence
otal Oxides of Nitrogen 503 PPM
itrooen Balance
Analytical Measurement Data Available Online.
41 -tvl-50
E80059947 202301 1 7
sx32691 202301 1 7
9 7 PPI\/I
280 PPM
279 8 PPru
Analytical lnstrumentation
Make Model
42i-HLNO Chemiluminescence Themo 1152610017 0A12912023
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined speciflcations. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternatronal System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specifled or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
,hrrdt lbrr/aL
Aaron Varelas
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revrsed on 2018-09-'!7
NOx Converter Check
-I:_-.,:. 1 j.t. '? ,i :'
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Project No.: AST-2025-0362-001
NOr Converter Check - Outlet
Analyzer Make Thermo
Analyzer Model 42ra
Seriel Number 1232'1730521
Cytinder ID Number CCfiOTfl
Cylinder Exp. Date 4ll6ln
Cvlinder Concentration. ppm 49.7
Pre-Test Dete 2ll8l25 Time 10:08
Pre-Test ConcentET6ilppm 45"68
Pre-Test Efficiencv. 7o 92
Post-Test Dste 2ll8l25 Time 14:l I
Post-Test Coo"uol-""ti*, pp- 4a?3
Post-Test Efficiencv. %o 9t
*Required Efficiency is >- 90 ol.
=laAI NOx Converter Check]GE)
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Project No.: A5T-2025-0362-001
NO2 Converter Check - Outlet#AnalYzer Model
,,32773052rSerial Number #Cylinder Exp. Date
Cvlinder Concentration. DDm 49.7
Pre-Test Date 2ll7l25 Time 13:32
Pre-Test Concentration, ppm 46.01
Pre-Test Efficiencv. 7o 93
Post-Test Date 2ll7l25 Time 17:38
Post-Test Concentration, ppm 46.08
Post-Test Efficiencv. 7o 93
Efficiency is 2
L*
---E*5--.Accreditation #627S
Red Ball Technical Gas Service
555 Craig Kennody Way
Shreveport, LA 71107
800-55't -8150
PGVP Vendor lO # G12024
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lO Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
cc77077
124731
145t) PSt(;
cc770777 20240212-0
Certification Date:
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certification Dates:
)4t16t2024
)4116t202t
- snreveoon - [A
:c770777 .20240212
108893227
This calibration standard has been certified per the May 201 -12t531,
G2
Nitrogen Dioxide
Concontratlon Uncertalnty Analytical Prlnclple
49.7 P
Assayed On
02t 16t2024, 04 I 16t2024
Balance
Certifi ed Concentration(s)
Analytical
29 22 PPM
94 5 PPM
63 3 PPirl
c21 90301 02
c2190301 02
c2190301 02
IUKS 2031 DJG2EKVSl 3T
MKS 2O3lGPPP1A5ZK1XX
017146467
1 12424254
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined speciflcations. This
calibratlon/test was performed usrng Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specifled or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
,--7 //;; u;
Timothy Davis
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J. Revrsed on 2018-09-17
M205 QA DataIEE)=laAI
MPC-LoedoD:
Sourc:
ProJcct No.:AST-2025-0362{01
Dttc Nl7/25
Anallzr Makc:
Anelyzcr Modcl:
Analyzc SN:
Environics ID:
Componcny'Balmce Ga:
Cylindr Ga ID @ilution):
Cylindr Ga Conmeation @ilution), ppm:
Cylinda Gu ID (Mid-L:vcl):
EB0069814
RR0253E
Cylindr G* Concatration (Mid-Lrvcl), ppm: I 1.00
Alelyzcr
Concatrrrdon
InJedon I
Enor
( !2u.\
Inlcflol 2
Enor
( * 2./.\
InJccdon 3
Enor
( + 7./.1
-|J. l"/a -0.|o/a
-u- t,,
4 O.4Yo 4",
2 -0.4%09
Callbrrdon Dlret to
Ll[Drlgotr
Ges
CoEccEtrrflon
ulfloE r
Alrlyzer
Conccrtrrtlon
annmt
EJEqoE a
Aldyzcr
Conccntrrdotr
,n6m)
UJEEOtr J
Anrlyzcr
C oncetrtrrdoD
ahnh)
Avcngc
Andyzcr
Conccntrrdon Dlfferencc
Avcnga
Enor
( r 2./.r
I 1.00 10.99 10.99 t t.00 10.99 -o ot -o.to/n
A/tSOUBCE TESTING
Mass FIow Controller Calibration
Note: The mass flow controller's calibration values are used by the dilution system's operatinS software to improve accuracy. These calibrations are not
necessarilyindicativeofthesystemsoverallperformance. PerformanceisverifiedbyconductingaMethod205priortoeachfielduse.
Calibration Performed By JFT
Dilution System Make:
Dllutlon sptem Model:
Dllutlon System S/N:
Callbratlon Equlpment Make:
Callbratlon Equlpment Model:
Callbratlon Equlpment S/N:
Flow Cell S/N:
Flow Cell S/N:
Callbratlon Gas:
Barometrlc Pressure, mmHg:
Amblent Temperature,'F:
Environics
4040
8029
Alicat Scientific
M-losLPD/sM M-D/sM, M-15LPM-O/s
2l2L2O;27212t
272t20
272L2t
Nitrogen
25.559
70.7
Mass Flow Controller lD
Slze, ccm:
Make:
Model:
s/t{:
#1
10,000
Environics
4040
455242003
#2
10,000
Environics
4040
455242004
#3
1,000
Environics
4UO
45s242002
Set Flow True Flow Dlffercnce
cclmln cclmin
Set Flow True Flow Dlfference
cc/min cc/mln
Set Flow True Flow Difference
cc/mln cc/mln
5%
LO%
20%
30%
40%
50%
60%
70%
80%
90%
100%
500 489 2.2%
1,000 987 t.3%
2,000 t,970 1.5%
3,000 2,985 0.5%
4,000 4,014 0.4%
5,000 5,034 0.7%
6,000 6,053 0.9%
7,000 7,084 r.2%
8,000 8,119 L.s%
9,000 9,156 t.7%
10,000 Lo,202 2.o%
500 454 9.2%
1,000 959 4.t%
2,000 1,989 0.5%
3,000 3,003 0.t%
4,000 4,ot4 0.4%
5,000 5,033 0.7%
6,000 5,055 0.9%
7,000 7,093 7.3%
8,000 8,t23 t.5%
9,000 9,160 7.8%
10,000 10,195 2.O%
50 47 6.0%
100 97 3.O%
200 196 2.O%
300 298 0.7%
400 400 0.0%
s00 s02 0.4%
600 602 O.3/o
700 706 0.9%
800 810 t3%
900 914 L.6%
1,000 1,020 2.o%
Date 4ll9l24
=r€rAI Stratification Check
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Crude Unit Furnace H-lOl
Project No.: AST-2025-0362-001
Date:211812025
Traverse Point Time o2
(%l
Coz
(o/"1
NOx
(oom)
A-1
7
3
B-l
2
3
l0:23
l0:25
l0:27
l0:29
l0:31
l0:33
5.97
5.71
5.75
5.74
5.81
5.83
5.8
8.85
9.04
9.03
9.03
8.98
8.97
9.0
31.99
31.95
31.99
32.ts
32.10
31.85
32.0Average
Criteria Met Smgle Pomt Smgle Pomt Srngle Pomt
plll6rrrcE)
'I
Stratification Check
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Ultraformer Unit Fumace F-l
Proj ect No. : AST-2025 -03 62-001
Dile:2/17/2025
Traverse Point Time o2
(Vol
Cor
(Yol
NOr
(onm)
A-l
2
3
B-l
2
3
l3:46
13:48
l3:50
13:52
l3:54
l3:56
7.49
7.54
'1.53
7.50
7.s3
'1.56
7.5
7.96
8.00
8.02
8.04
8.04
8.02
8.0
25.70
23.67
23.71
23.s9
23.73
23.86
24.0Average
Criteria Met Srngle Potnt Single Pomt 3 Pomt
FuelAnalysis
Location:
Project No.:
MPC-Tesoro - Salt Lake Ciw Refinerv. UT
AST-2025-0362-00 I
FI]EL FACTOR CALCULATION BASED ON FUEL ANALYSIS
COMPOIYENT MW MOLE%MOLES C MOLES H MOLES O MOLESN MOLES S
T{YDROGEN 2.0t6 20.736 41.472
METHANE 16.M3 55.944 55.944 223.776
NITROGEN 28.013 4.328 8.656
ETHYLENE 28.054 5.631 tt.262 22.524
ETHANE 30.070 9.471 t8.942 56.826
HYDROGEN SULFIDE 34.076 0.00t 0.002 0.001
PROPYLENE 42.081 t.t24 3.372 6.7M
CARBONDIO)(IDT ,14.010
PROPANT M.097 1.737 5.211 13.896
BL]'TYLENES 56.08
ISO.BUTANT 58.24
N-BUTENE 58.24 0.164 0.656 r.3t2
PENTENES 70.35
ISO.PENTANE 72.5t
N-PENTANE 72.5l 0.829 4.145 9.948
BENZENE 78.t4
HEXANE 86 78
TOLUENE 92.141
HEPTANE 100.205
ETHYLBENZENE 106.168
XYLENE 106.168
TOTAI.99.96s 99.532 376.500 8.656 0.001
WEIGHT &BS]1,t95.479 379.474 r21.242 0.032
WEIGIIT%70.479 22.372 0.000 7.t48 0.002
LHV GTU/SCF):903 : SUM [ (MOLE%, o LHV 1) + 100 ]: SUM [ (MOLE%r . HHV ) + 100 ]: SUM [ (MOLE %i . DENSITY ) * 100 ]
= DENSITY (LB/SCF) + DENSITY,un P.0763 LB/SCF)
:HHV+DENSITY
= SUM [ (MOLE%, . MW ) + 100 ]
:106 . [(3.64o%H) + (1.53.%C) + (0.14o/sy1+ p.57'%S) -(0.46o%O)]+GCV
= 106 . [ (5.57 o%H) + (1.53.%C) + (0.14 o%N) + (0.57'%5) - (0.46 o%O) ] * ACV: 106 . (0.321 o%C) + GCV
:0.209oFa+Fc
HIIV GTU/SCF):
DENSITY (LB/SCF):0.M5
SPECIFIC GRAVITY:0.586
GCV GTU/LB):22,326
MWGB/LBMOLE):t6.966
F6 @SCF/ITIMBTII):8,522
F. (WSCF/TVIMBTU):10,456
F^(SCF/IVIMBTI.I):1,013
Erpected Foi 1.758
=taAITEE!
Location: MPC-Tesoro - Sat Lak" Cry n.n"".y,Ut
Project No.,
FTIEL FACTOR CALCT]LATION BASED ON FT]EL ANALYSIS
FuelAnalysis
COMPOITEI\iI MW MOLEo/n MOLES C MOLES H MOLES O MOLES N MOLES S
TTYDROGEN 2.016 19.430 38.860
METTIANE 16.043 57.085 57.085 228.340
NMROGEN 28.013 4.424 8.848
ETHYLENE 28.054 5.701 11.402 22.8M
ETHANE 30.070 9.569 19.138 57.414
HYDROGEN SI,'LFIDE 34.076 0.001 0.002 0.001
PROPYLENE 42.08 r 1.086 3.258 6.516
PROPANE 44.09'.1 t.697 5.091 13.576
N-BUTANE 58.t24 0.1 64 0.656 t.3t2
N-PENTANE 72.t51 0.861 4.305 t0.332
TOTAI-100.018 100.935 379.t56 8.848 0.001
WEIGIIT (LBSI t,2t2.330 382.151 t23.931 0.032
WEIGET%70.548 22.238 0.000 7 _2t2 0.002
LIIV GTU/SCD:9t2 = SUM [ (MOLE%, . LHVi) * 100 ]
= SLIM I Gr/OLE%i . HHV ) + 100 ]
= SUM [ (MOLE o/oi . DENSITY ) * 100 ]
= DENSITY (LB/SCF) + DENSITY,qTn P.0763 LB/SCF)
= HlfV + DENSITY
= SUM [ (MOLE%I . MW ) * 100 ]
= 106 r [ (3.64 o/61]) + (1.53.%C) + (0.14 o%N) + (0.57'%5) - (0.46 ofiQ 1 + GCV
= 106 . [ (5.57 oy"X1 + fi.53 .%C) + (0.14 o/,lt!) + (0.57'%S) - (0.46 .%O) ] + GCV
= 106 . (0.321 c%C) + GCV
=0.209.Fa+F"
EIIV GTU/SCD:
DENSITY [B/SCF):0.M5
SPECIFIC GRAVITY:0.593
GCVSTU/LB):22,248
MlY GBILBMOLE):17.188
F6 @SCF/Iv[MBTU):8,535
F*(WSCF/MMBTU):10.465
F. (SCF/I}IMBTID:1,018
Expected Fol 1.753
FTATEE)AI FuelAnalysis
Locatlon:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
AST-2025-0362-00 I
FTIEL FACTOR CALCT]LATION BASED ON FUEL ANALYSIS
COMPONENI MVv MOLE%MOLES C MOLES H MOLES O MOLES N MOLES S
HYDROGEN 2.015 19.440 38.880
METHANT 16.043 56.941 s6.941 227.764
NTTROGEN 28.013 4.407 8.814
ETIIYLEM 28.054 5.756 I 1.5 12 23.024
ETTIANE 30.070 9.689 19.378 58.1 34
HYDROGEN SULFIDE 34.076 0.001 0.002 0.001
PROPYLENE 42.081 t.137 3.41I 6.822
PROPANE 44.097 1.630 4.890 13.040
N-BUTANE 58.124 0.1 58 0.632 t.264
N-PENTANE 72.t51 0.848 4.240 10.1 76
TOTAL 100.007 101.004 379.106 8.814 0.001
WEIGHT &BSI r,213. 159 382.101 123.455 0.032
WEIGHT%70.584 22.231 0.000 7.1 83 0.002
LIIV GTU/SCD:913 = SUM [ (MOLE%, . LHV ) + 100 ]: SUM [ (MOLE%, . HHV ) + 100 ]: SUM [ (MOLE o/o1 o Pg;Y31ry ) * 100 ]: DENSITY (LB/SCF) - DENSITYTn P.0763 LB/SCF)
:HHV+DENSITY
: SUM [ (MOLE%, . MW) * 100]
= 106 , [(3.64o%H) + (1.53.%oC) + (0.14o%N) + (0.57'%5) -(0.46o%O)]* GCV
: 106 , [ (5.57 ./oXS + ft.53.%C) + (0.14 o%N) + (0.57'%3) - p.a6 o%O) ] + GCV: 106 . (0.321 .%C) + GCV
:0.209 o F a + F "
IIEV GTU/SCFI:
DENSITY &B/SCF):0.M5
SPECIFIC GRAVITY:0.594
GCV GTU/LB):22,252
MW&B/LBMOLE):17.191
F6 @SCF/MMBTU):8,535
F.(WSCF/MMBIU):10,463
F"(SCF/IVIMBTTI):1,018
Expected Foi 1.752
=TATEEAI FuelAnalysis
Location:
Project No.:
MPC-Tesoro - Salt Lake City Refmerv. UT
AST-2025-0362-00 1
FT]EL FACTOR CALCIJLATION BASED ON FI]EL ANALYSIS
COMPOI\ENT MTY MOLE%MOLES C MOLES H MOLES O MOLES N MOLES S
IIYDROGEN 2.016 25.547 51.094
METHANE 16.043 49.507 49.507 198.028
NITROGEN 28.013 4.883 9.766
ETHYLENE 28.054 5.898 fi.796 23.592
ETHANE 30.070 10.042 20.084 60.252
IIYDROGEN STILFIDE 34.076 0.001 0.002 0.001
PROPYLENE 42.081 t.023 3.069 6.1 38
PROPANE 44.097 2.017 6.051 16.136
ISOBUTYLENE 56.1 08 0.160 0.640 1.280
N-PENTANE 72.151 0.865 4.325 10.380
TOTAI.99.943 95.472 366.902 9.766 0.001
WEIGET &BS'1,t46.7t4 369.801 136.789 0.032
WEIGHT%69.358 22.367 0.000 8.214 0.002
LI{V BTU/SCH:8',7'.|= SUM [ (MOLE%, . LHV ) + 100 ]
= SUM [ (MoLE%i . HHV ) + 100 ]
= SUM [ (MOLE %i . DENSITYi * 100 ]
= DENSIY GB/SCF) + DENSITY,qTn P.0763 LB/SCF)
= HIIV - DENSITY
: SUM [ (MOLE%, . MW ) + 100 ]
: 106, [ (3.64 . %H) + (1.53 . %C) + (0.1 4 o /61111 + p.57'%S) - @.aO o %O) ] + GCV
= 106 . [(5.57 c%H) + (1.53.%oC) + (0.14c%N) + (0.57'%5) -p.a6o%O) ]+ GCV
= 106 , (0.321 o%C) + GCV
:0.209oFa+F"
IIHV GTU/SCD:
DENSITY &B/SCO:0.M4
SPECIFIC GRAVITY:0.571
GCV (BTU/LB):22,237
MW&B/LBMOLE):16.534
Fa @SCFMMBTU):8,485
F*(WSCFMMBTII):t0.427
F.(SCF/1!IMBTU):1,001
Erpected Fol 1 .771
=IAAITGE)
i .. :l
Location: MPC-Tcsoro - Salt Lake Ciw Refinerv. UT
Project No.: A5T-2025-0362-001
FI,]EL FACTOR CALCT]LATION BASED ON FI]EL ANALY$S
FuelAnalysis
COMPONENI MW lil.{OLEY' MOLES C MOLESH MOLES O MOLES N MOLES S
TTYDROGEN 2.Ot6 25.187 50.374
METHANE 16.043 49.647 49.il1 198.588
NITROGEN 28.013 4.886 9.772
ETFTYLENE 28.054 5.872 1r.744 23.488
ETHANE 30.070 1 0.1 08 20.2t6 60.648
ITYDROGEN SULFIDE 34.076 0.002 0.0M 0.002
PROPYLENE 42.081 1.271 3.813 7.626
PROPANE 44.097 2.006 6.018 15.M8
ISOBUTYLENE 56. I 08 0.1 70 0.580 1.350
N-PENTANE 72.151 0.885 4.425 10.520
TOTAI 100.034 96.543 358.755 9.772 0.002
WEIGIIT (LBS)I,159.578 371.669 136.873 0.064
WEIGET%69.51 I 22.280 0.000 8.205 0.004
LIIVGTU/SCD:884 = SUM [ (MOLE%, . LHV i) + 100 ]
= SUM [ (MOLE%; . HHV i) + 100 ]
= SUM [ (MOLE %i . DENSITY ) * tOO ]
= DENSITY (LBISCF) + DENSITY,.R P.0763 LB/SCF)
=HHV+DENSITY
= SUM [ (MOLE%1 . MW ) + 100 ]
= 106 . [(3.64o/sl]) + (1.53.%C) + (0.14o/,lr!) + (0.57.%3) - (0.46.%O)l+ cCV
= 106 . t F.57 .%H) + (1.53 .%oC) + (0.14 o%N) + (0.57'%S) - (0.46 o%O) I + cCV
= 106 , (0.321 o%C) + GCV
=0.209oFa+Fc
HIIV BTU/SCB:
DENSITY (LB/SCD:0.044
SPECIFIC GRAVITY:0.576
GCV(BTU/LB):22,213
MW&B/LBMOLE):16.682
F6 @SCF/MMBT[r):8,49r
F. (WSCF/TIMBTU):t0.427
F.(SCF/TIMBTID:1,005
Erpected Foi t.767
=TAAIIEE)
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Project No.: AST-2025-!!!? !Q]
FT,IEL FACTOR CALCT]LATION BASED ON FTIEL ANALYSIS
FuelAnalysis
COMPOhIEI\II MW MOLE%MOLES C MOLES H MOLES O MOLES N MOLES S
ITYDROGEN 2.0t6 25.0U 50.008
METHANE 16.043 50.149 s0.149 200.596
NTIROGEN 28.013 4.899 9.798
ETHYLENE 28.054 5.867 11.734 23.468
ET}IANE 30.070 9.988 19.976 59.928
HYDROGEN SULFIDE 34.076 0.001 0.002 0.001
PROPYLENE 42.O81 1.054 3.t62 6.324
PROPANE 44.097 t.957 5.871 1s.656
ISOBUTYLENE 56.108 0.165 0.660 1.320
N-PENTANE 72.t51 0.862 4.310 10.344
TOTAL 99.946 9s.862 367.646 9.798 0.001
WEIGHT (LBSI I,151.398 370.550 t37.238 0.032
WEIGHT%69.394 22.333 0.000 8.271 0.002
LI{V (BTU/SCF)r 879 = SUM [ (MOLE%i . LHV ) + 100 ]: SUM [ (MOLE%I . HHV ) + 100 ]
= SUM [ (MOLE o/o1 o P61t151ry ) * 100 ]: DENSITY (LB/SCF) + DENSITYA,R P.0763 LB/SCF)
: HITV = DENSITY
: SUM [ (MOLE%, . MW ) + 100 ]
= 106 , [ (3.U o%H) + (1.53.%C) + (0.14.%N) + (0.57-%5) - (0.46 o%O) ] + GCV
:106 . [(5.57 o%H) + (1.53.%C) + (0.14ofi1t!) + (0.57'%5) -p.a6 o%O)]+ GCV: 106 . (0.321 o%C) + GCV
:0.209oFa+Fc
IIIIV (BTU/SCF)r
DENSITY GBISCF):0.M4
SPECIFIC GRAVITY:0.573
GCV (BTU/LB): 22,2t6
MW[B/LBMOLE):16.593
F6 @SCF/IvIMBTfI):8,490
F. (WSCF/IVTMBTU):10.431
F.(SCF/}TMBTII}:1,003
Erpected Fol 1.770
Run 1 21L812025
lStart time 10:35
moteTo
HYDROGEN 20.736
OXYGEN
NITROGEN 4.328
H25 0.001
METHANE 55.944
Carbon Monoxide
CARBON DIOXIDE
ETHYLENE 5.631
ETHANE 9.47t
PROPANE L.737
PROPYLENE L.124
ISOBUTANE
N BUTANE
N BUTENE 0.164
ISOBUTYLENE
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
N PENTANE 0.829
C6+
Total 99.964
Run 2 217812025
lstart rime 11=46
mole o/o
HYDROGEN 19.430
OXYGEN
NITROGEN 4.424
H2S 0.001
METHANE 57.085
Carbon Monoxide
CARBON DIOXIDE
ETHYLENE 5.701
ETHANE 9.569
PROPANE 1.697
PROPYLENE 1.086
ISOBUTANE
N BUTANE
N BUTENE 0.164
ISOBUTYLENE
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
N PENTANE 0.861
C6+
Total 100.017
Run 3 217812025
lsta* time 12:55
mote%
HYDROGEN t9.MA
OXYGEN
\ITROGEN 4.407
H2S 0.001
VIETHANE 56.941
Sarbon Monoxide
3ARBON DIOXIDE
ETHYLENE 5.756
ETHANE 9.689
PROPANE 1.630
PROPYLENE 1.t37
ISOBUTANE
N BUTANE
N BUTENE 0.158
ISOBUTYLENE
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
N PENTANE 0.848
C6+
Total 100.007
2tt7t2025
Time 13:57
HYDROGEN 25.il7
OXYGEN
NITROGEN 4.883
H2S 0.001
METHANE 49.507
CARBON DIOXIDE
ETHYLENE 5.898
ETHANE 10.042
PROPANE 2.017
PROPYLENE 1.023
ISOBUTANE
N BUTANE
N BUTENE
ISOBUTYLENE 0.160
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
\ PENTANE 0.865
06+
lotal 99.943
Run 2
Start Time
HYDROGEN
OXYGEN
NITROGEN
H2S
METHANE
CARBON DIOXIDE
ETHYLENE
ETHANE
PROPANE
PROPYLENE
ISOBUTANE
N BUTANE
N BUTENE
ISOBUWLENE
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
N PENTANE
C6+
TotaI
2t17t2025
25.187
4.886
0.002
49.647
5.872
10.108
2.006
1.271
0.170
0.885
100.033
Run 3
Start Time
HYDROGEN
OXYGEN
NITROGEN
H25
METHANE
CARBON DIOXIDE
ETHYLENE
ETHANE
PROPANE
PROPYLENE
ISOBUTANE
N BUTANE
N BUTENE
ISOBUTYLENE
TRANS BUTENE 2
CIS BUTENE 2
ISOPENTANE
N PENTANE
C6+
TotaI
zfl12025
25.004
4.899
0.001
50.149
5.867
9.988
1.957
1.054
0.165
0.862
99.946
APR - 2 2-0?-5
DIVISION OF AIR OUALITY
AtAre
TECHNICAL GROUP
RATA Report
Marathon Petroleum Corporation
Tesoro Refining and Marketing Company
474 West 900 North
Salt Lake City, Utah 84103
Source Tested: Wet Gas Scrubber
Test Dates: February 19 &20,2025
Proj ect No. AST -2025 -0362-003
Prepared By
Alliance Technical Group, LLC
3683 W 2270 S, Suite E
West Valley City, UT 84120
Source Test Reporl
Test Program Summary
Resulatorv Information
UDAQ Permit No.
Regulatory Citations
Source Informetion
UDAQ Permit No. DAQE-AN 103350075- I 8
40 CFR 60, Appendix B, PS 2, 3,4A and 6
Source Name
Wet Gas Scrubber
Contect Information
MTA Parameters
Oz, SOz, NOx, CO, VFR
Test Location
Marathon Petroleum Corporation
Tesoro Refining and Marketing Company
474 West 900 North
Salt Lake City, Utah 84103
Facility Contact
f,lsann61 Schaefer
Rschaefer@marathonpefr oleum. com
(8ol) 367-8r02
Test Company
Alliance Technical Group, LLC
3683 W 2270 S, Suite E
WestValley City, UT 84120
Project Manager
Charles Horton
[e-mail]
(3s2) 663-7s68
Field Team Leader
Alan Jensen
alan j ensen@alliancetg. com
[phone]
QA/QC Manager
Kathleen Shonk
[e-mail]
(8t2) 4s2478s
Report Coordinator
Delaine Spangler
delaine. [e-mail]
Report Reviewer
Sarah Perry
[e-mail]
AST-2025-0352-003 Tesom - Salt Lake City, Utah Page i
TECIiNICAL GROI-JP Source Test Repoa
C ertific ation Stat ement
Alliance Technical Group, LLC (Alliance) has completed the source testing as described in this report. Results apply
only to the source(s) and operating condition(s) that were tested during the specific test date(s) and time(s) identified
within this report. All results are intended to be considered in their entirety, and Alliance is not responsible for use of
less than the complete test report wittrout written consent. This report shall not be reproduced in full or in part without
written approval from the customer.
To the best of my knowledge and abilities, all information, facts and test data are correct. Data presented in this report
has been checked for completeness and is accurate, error-free and legible. Onsite testing was conducted in accordance
with approved internal Standard Operating Procedures. Any deviations or problems are detailed in the relevant
sections of this test report.
This report is only considered valid once an authorized representative of Alliance has signed in the space provided
below; any other version is considered draft. This document was prepared in portable document format (.pd0 and
contains pages as identified in the bottom footer of this document.
41112025
Date
Alliance Technicel Group, LLC
AST-2025-0362-003 Tesoro - Salt Lake City, Utah Page ii
Affarpe
T E C I] N IC A L G R O LJ P Source T*t Repon
Table ofContents
TABLE OF CONTENTS
1.3 Site Specific Test Plan & Notification.................. ....................... l-l
3.1 U.S. EPA Reference Test Methods I and2 - Sampling/Traverse Points and Volumetric Flow Rate ........ 3-1
3.2 U.S. EPA Reference Test Method 3/3A- Carbon Dioxide........ ....................... 3-1
3.3 U.S. EPA Reference Test Method 3A - Oxygen ..... 3-l
3.4 U.S. EPA Reference Test Method 4 - Moisture Content........ .....3-2
3.5 U.S. EPA Reference Test Method 6C - Sulfur Dioxide........ .......3-2
3.6 U.S. EPA Reference Test Method 7E - Nitrogen Oxides ............3-2
3.7 U.S. EPA Reference Test Method 10 - Carbon Monoxide.... ......3-2
3.8 U.S. EPA Reference Test Method 205 - Gas Dilution System Certification .........................3-3
3.9 Quality Assurance/Quality Contol - U.S. EPA Reference Test Method 3/3A ............ ......... 3-3
3.10 Quality Assurance/Quality Control - U.S. EPA Reference Test Methods 3A, 6C, 7E and l0 .............. 3-3
LIST OF TABLES
Table 2-l: Summary of Performance Specification Results - CEMS I ................... ......2-l
Table2-2: Srunmary of Perforrnance Specification Results - CEMS 2.................. .......2-2
APPENDICES
Appendix A Sample Calculations
Appendix B RA Calculations & Field Data
Appendix C Quality Assurance/Quality Contol Data
Appendix D Process Operating/Contol System Data
AST-2025-0362-003 Tesoro - Salt Lake City, Utah Page iii
put6lpe
TECIlNICAL GROTJP Source Test Rqorl
Introduction
1.0 Introduction
Alliance Technical Group, LLC (Alliance) was retained by Marathon Petoleum Corporation (N[PC) to conduct
performance specification (PS) testing at the Tesoro Refining and Marketing Company (Tesoro) Salt Lake City, Utah
refinery. Portions of the facility are subject to provisions of 40 CFR 60, Appendix B, PS 2, 3, 4A and 6 and the Utah
Departnent of Environmental Quality, Division of Air Quality (UDAQ) Permit No. DAQE-AN103350075-18.
Testing is outlined in the table below.
Table 1-1: PS Test Mstrir
Wet Gas Scrubber Oxygen, Sulfur Dioxide, Nitrogen Oxides, Carbon Monoxide,
Volumetric Flow Rate
1.1 CEMS Descriptions
Wet Gas Scrubber
Parameter:
Make:
Model:
Serial No.:
Span:
Parameter:
Make:
Model:
Serial No.:
Span:
Pollutant
OzlNOx-CEMS I
CAI
700
1908029
0-10 % Oz
0-200 ppmvd NOx
Pollutant
Oz / NOx - CEMS 2
CAI
700
1908030
0-10%Oz
0-200 ppmvdNOx
Pollutant
SOz - CEMS I
Teledyne
TIOOH
429
0-200 ppmvd SOz
Pollutant
SOz-CEMS 2
Teledyne
TIOOH
428
0-200 ppmvd SOz
Pollutant
co-cEMs r
Horiba
VIA-s10
NP7X7084
0-1,000 ppmvd
Pollutant
CO _ CEMS 2
Horiba
VIA.s10
UGTUOOOB
0-1,000 ppmvd
Flow Rate
VFR
Rosemount
3 05 I CD I AO 2 AI ANT'B2II2DZ
2862407
NA
Flow Rate
VFR
Rosemount
3 05 I CD I A0 2 At ANtsBztlzDZ
286240',t
NA
1.2 Project Teem
Personnel involved in this project are identified in the following table.
Table 1-2: ProJect Team
MPC Personnel f,fusennoa Schaefer
Allience Personnel Alan Jensen
Supilani Mailei
1.3 Site Specific Test Plen & Noffication
Testing was conducted in accordance with the Site Specific Test Plan (SSTP) that was submitted to UDAQ by MPC.
1.4 Test Program Notes
Method 3/3A was not included in the test plan but was used for sampling CO2 for Molecular Weight determination.
AST-2025-0362-003 Tcsoro - Salt Lakc City, Utah
AI Source Test Report
Summary of Results
2.0 Summary of Results
Alliance conducted PS testing at the Tesoro facility in Salt Lake City, Utah on February 19 and 20,2025. PS testing
included conducting RATAs on the Oz, SOz, NOx, and CO CEMS serving to monitor emissions and the VFR CERMS
serving the Wet Gas Scrubber.
Tables 2-l and 2-2 provide summaries of the RA results in comparison to the applicable RA requirements. Any
difference between the summary results listed in the following tables and the detailed results contained in appendices
is due to rounding for presentation.
Table 2-l: Summary of Performance Specification Results - CEMS I
I Calculated using the applicable source standard for the pollutant. See Appendix B for the applicable standard used.
2 Calcularcd using the mean reference method.
lEe
! l l'
Fla
,tl-
CEMS
Performence Tect Dett Reletive Accurecy
Reference
Method
I)ete
CEMS
Datl
Performence
Required
Performence
Demonstrrted
Sulfur Dioxide Data
Concentration, ppmvd
Concentration, ppmvd @ 0% Oz
Emission Rate, lb/hr
-0.093
-0.12
-0.092
0.31
0.39
0.31
<l0Yo
st0%
sl0%
3.00 Yol
2.99 Yol
4.25 Yol
Nitrogen Oxides Data
Concentration, ppmvd
Concentration, ppmvd @ 0% Ot
Emission Rate, lblhr
0.00
0.00
0.00
0.00
0.00
0.00
sl0%
sl0%
<l0%o
0.023 0 l
0.018 % t
0.033 0 l
Cerbon Monoxide Data
Concentration, ppmvd
Concentration, ppmvd @ 0% Oz
2.16
2.73
5.38
6.81
s5%
<5Yo
0.91Yol
0.920 1
Oxygen Data
Concentration, % (dry)4.35 4.39 s20%t.t'7 %2
Volumetric Flow Rate Data
Flow Rate, scfrn (dry)98,680 l0 t,176 <20%4.76 Yo2
AST-2025-0362-003 Tesoro - Salt Lake City, Utah
put6rrce
TECHNICAL GROUP Source TxtRqort
Sumnary of Resulu
Teble 2-2: Summery of Performence Speclflceflon Rerultc - CEMS 2
Sulfur Diodde Drtg
Concentration, ppmvd
Concentration, ppmvd @ 0% Oz
Emission Rate,lblhr
< l0Yo
st0%
< l0Yo
1.35 o/o I
137 %l
L.93 o/ol
Nitrogen Oxider Detr
Concentrationo ppmvd
Concentratioq ppmvd @ 0% Oz
Emission Rate, lb/hr
< l0Yo
3L0 o/o
< l0o/o
6.55 o/oL
6.49%l
5.90o/ol
Crrbon Monodde Detr
Concentration, ppmvd
Concentration, ppmvd @ 0% Oz
l.OgYor
1.09o/o I
Oxygen Data
Concentratiot,% (&y)0.71o/o2
Volumetric Flow Rrte Dete
Flow Rate, scfin (dry)
t Calculatcd usiug thc aprplicablc rourcc gtandard for thc polftrtart. Scc Appcndix B for thc applicablc sandard ucd.
2 Calculatcd using thc mcan rcfcrcncc mcthod"
AST-2025-0362-003 Tcsom - Salt I:kc City, Utah
puldrrcE)
Tf CIiItICAL GROUP Source Test Report
Testine Methodolonl
3.0 Testing Methodology
The emission testing program was conducted in accordance with the test methods that are listed in Table 3-1. Method
descriptions are provided below, and quality assurance/quality conhol data is provided in Appendix C.
Table 3-1: Source Testing Methodology
3.1 U.S. EPA Reference Test Methods I end 2 - Sampling/Treverse Points and Volumetric Flow Rate
The sampling location and nwnber of traverse (sampling) points were selected in accordance with U.S. EPA Reference
Test Method l. To determine the minimum number of haverse points, the upsteam and downsteam distances were
equated into equivalent diameters and compared to Figure l-2 in U.S. EPA Reference Test Method l.
Full velocity taverses were conducted in accordance with U.S. EPA Reference Test Method 2 to determine the
average stack gas velocity pressure, static pressure and temperature. The velocity and static pressure measurement
system consisted of a pitot tube and inclined manometer. The stack gas temperature was measlued with a K-type
thermocouple and pyrometer.
Stack gas velocity pressure and temperature readings were recorded during each test run. The data collected was
utilized to calculate the volumetric flow rate in accordance with U.S. EPA Reference Test Method 2.
Stack gas velocity pressure and temperahue readings were recorded during each test run. The data collected was
utilized to calculate the volumetric flow rate for comparison to the volumetic flow rate continuous emissions
monitoring system (CERMS). The relative accuracy of CERMS was determined based on procedures found in 40
CFR 75, Appendices A & B.
3.2 U.S. EPA Reference Test Method 3/3A - Cerbon Dioride
Thecarbondioxide(COz)testingwasconductedinaccordancewithU.S.EPAReferenceTestMethod3/3A. One(l)
integrated Tedlar bag sample was collected during each test run. The bag samples were analyzed on site with a gas
analyzer. The remaining stack gas constituent was assumed to be nitrogen for the stack gas molecular weight
determination. The quality control measures are described in Section 3.9.
3.3 U.S. EPA Reference Test Method 3A - Orygen
The oxygen (Oz) and carbon dioxide (CO) testing was conducted in accordance with U.S. EPA Reference Test
Method 3A. Data was collected online and reported in one-minute averages. The sampling system consisted of a
Volumetric Flow Rate Full Velocity Traverses
Integrated Bag / Instrumental Analysis
Tesoro - Salt Lake City, Utah
Tf ctlt,l tcAr. ..1 []our Source Test Reporl
Testing Methodologt
stainless-steel probe, Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas
conditioning system was a non-contact condenser used to remove moisture from the stack gas. If an unheated Teflon
sample line was used, then a portable non-contact condenser was placed in the system directly after the probe.
Otherwise, a heated Teflon sample line was used. The quality control measlues are described in Section 3.10.
The relative accuracy of the Oz CEMS was deterrnined based on procedures found in 40 CFR 60, Performance
Specification 3.
3.4 U.S. EPA Reference Test Method 4 - Moisture Content
The stack gas moisture content (BWS) was determined in accordance with U.S. EPA Reference Test Method 4. The
gas conditioning train consisted of a series of chilled impingers. Prior to testing, each impinger was filled with a
known quantity of water or silica gel. Each impinger was analyzed gravimetrically before and after each test run on
the same balance to determine the amount of moisture condensed.
3.5 U.S. EPA Reference Test Method 6C - Sulfur Dioxide
The sulfiu dioxide (SOz) testing was conducted in accordance with U.S. EPA Reference Test Method 6C. Data was
collected online and reported in one-minute av€rages. The sampling system consisted of a heated stainless steel probe,
Teflon sample line(s), gas conditioning system and the identified analyzer. The gas conditioning system was a non-
contact condenser used to remove moisture from the source gas. If an unheated Teflon sample line was used, then a
portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample
line was used. The quality confrol measures are described in Section 3.10.
The relative accuracy of the SOz CEMS was determined based on procedwes found in 40 CFR 60, Perforrnance
Specification 2.
3.6 U.S. EPA Reference Test Method 7E - Nitrogen Oxides
The nitogen oxides (NOx) testing was conducted in accordance with U.S. EPA Reference Test Method 7E. Data was
collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe, Teflon
sample line(s), gas conditioning system and the identified gas analyzer. The gas conditioning system was a non-
contact condenser used to remove moishre from the stack gas. If an unheated Teflon sample line was used, then a
portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample
line was used. The quality control measures are described in Section 3.10.
The relative accuracy of the NOx CEMS was deterrnined based on procedures found in 40 CFR 60, Performance
Specification 2.
3.7 U.S. EPA Reference Test Method 10 - Carbon Monoxide
The carbon monoxide (CO) testing was conducted in accordance with U.S. EPA Reference Test Mettrod 10. Data
was collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe,
Teflon sample line(s), gas conditioning system, and the identified gas analyzer. The gas conditioning system was a
non-concact condenser used to remove moisture from the gas. If an unheated Teflon sarnple line was used, then a
portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample
line was used. The quality control measures are described in Section 3.10.
AST-2025-0362-003 Tesoro - Salt Lake City, Utah
pul6nrcE)
Source Test Repon
Testing MethodologtrIcr]l]ic;:GT]OL P
The relative accuracy of the CO CEMS was determined based on procedures found in 40 CFR 60, Perforrnance
Specification 4A.
3.E U.S. EPA Reference Test Method 205 - Gas Dilution System Certilication
A calibration gas dilution system field check was conducted in accordance with U.S. EPA Reference Method 205.
Multiple dilution rates and total gas flow rates were utilized to force the dilution system to perform two dilutions on
each mass flow confroller. The diluted calibration gases were sent directly to the analyzer, and the analyzer response
recorded in an electronic field data sheet. The analyzer response agreed within 2% of the actual diluted gas
concentration. A second Protocol I calibration gas, with a cylinder concenkation within l0% of one of the gas divider
settings described above, was introduced directly to the analyzer, and the analyzer response recorded in an electonic
field data sheet. The cylinder concentration and the analyzer response agreed within 2Yo. Tbese steps were repeated
three (3) times. Copies of the Method 205 data can be found in the Quality Asswance/Quality Conhol Appendix.
3.9 Quality Assurance/Quality Control - U.S. EPA Reference Test Method 3/3A
Cylinder calibration gases used met EPA Protocol I (+l- 2%) standards. Copies of all calibration gas certificates can
be found in the Quality Assurance/Quality Contol Appendix.
Low-Level gas was introduced directly to the analyzer. After adjusting the analyzer to the Low-Level gas
concentation and once the analyzer reading was skble, the analyzer value was recorded. This process was repeated
for the High-Level gas. For the Calibration Error Test Low, Mid, and High-Level calibration gases were sequentially
introduced directly to the analyzer. All values were within 2.0 percent of the Calibration Span or 0.5% absolute
difference.
At the completion of testing, the data was also saved to the Alliance server. All data was reviewed by the Field Team
Leader before leaving the facility. Once arriving at Alliance's office, all written and electronic data was relinquished
to the report coordinator and then a final review was perforrned by the Project Manager.
3.f 0 Quality Assurance/Quality Control - U.S. EPA Reference Test Methods 3A, 6C, 7E end 10
Cylinder calibration gases used met EPA Protocol 1 (+l- 2%) standards. Copies of all calibration gas certificates can
be found in the Quality Assurance/Quality Control Appendix.
Low Level gas was introduced directly to the analyzer. After adjusting the analyzer to the Low-Level gas
concentation and once tle analyzer reading was stable, the analyzer value was recorded. This process was repeated
for the High-Level gas. For the Calibration Error Test, Low, Mid, and High Level calibration gases were sequentially
introduced directly to the analyzer. All values were within 2.0 percent of the Calibration Span or 0.5 ppmv/% absolute
difference.
High or Mid-Level gas (whichever was closer to the stack gas concentration) was inhoduced at the probe and the time
required for the analyzer reading to reach 95 percent or 0.5 ppmv/% (whichever was less restrictive) of the gas
concentration was recorded. The analyzer reading was observed until it reached a stable value, and this value was
recorded. Next, Low Level gas was introduced at the probe and the time required for the aralyzer reading to decrease
to a value within 5.0 percent or 0.5 ppmv/% (whichever was less restrictive) was recorded. If the Low-Level gas was
zero gas, the response was 0.5 ppmv/% or 5.0 percent of the upscale gas concentation (whichever was less restrictive).
The analyzer reading was observed until it reached a stable value and this value was recorded. The measwement
AST-2025-0352-003 Tesoro - Salt Lake City, Utah Page 3-3
puldrrce
IfClllllClr.l GtlOLrF Source Test Report
Testing Methodologt
system response time and initial system bias were determined from these data. The System Bias was within 5.0
percent of the Calibration Span or 0.5 ppmv/% absolute difference.
High or Mid-Level gas (whichever was closer to the stack gas concentration) was intoduced at the probe. After the
analyzer response was stable, the value was recorded. Next, Low Level gas was intoduced at the probe, and the
analyzer value recorded once it reached a stable response. The System Bias was within 5.0 percent of the Calibration
Span or 0.5 ppmvlYo absolute difference or the data was invalidated and the Calibration Error Test and System Bias
were repeated.
Drift between pre- and post-run System Bias was within 3 percent of the Calibration Span or 0.5 ppmv/% absolute
difference. If the drift exceeded 3 percent or 0.5 ppmv/%, the Calibration Error Test and System Bias were repeated.
If the pollutant concenfration at each haverse point did not differ more than 5 percent or 0.5 ppmv/0.3% (whichever
was less restrictive) of the average pollutant concentration, then single point sampling was conducted during the test
runs. If the pollutant concentration did not meet these specifications but differed less than l0 percent or I .0 ppmv/O.5%
from the average concentration, then three (3) point sampling was conducted (stacks less than 7.8 feet in diameter -
16.7, 50.0 and 83.3 percent of the measurement line; stacks greater than 7.8 feet in diameter - 0.4, 1.0, and 2.0 meters
from the stack wall). If the pollutant concentration differed by more than l0 percent or 1.0 ppmv/O.S% from the
average concentration, then sampling was conducted at a minimum of twelve (12) traverse points. Copies of
statification check data can be found in the Quality Assurance/Quality Conhol Appendix.
An NOz - NO converter check was performed on the analyzer prior to initiating testing and at the completion of
testing. An approximately 50 ppm nitrogen dioxide cylinder gas was introduced directly to the NOx arLalyzer and the
inskument response was recorded in an electonic data sheet. The instrument response was within +/- l0 percent of
the cylinder concentation.
A Data Acquisition System with battery backup was used to record the instrument response in one ( I ) minute averages.
The data was continuously stored as a *.CSV file in Excel format on the hard drive of a computer. At the completion
of testing, the data was also saved to the Alliance server. All data was reviewed by the Field Team Leader before
leaving the facility. Once arriving at Alliance's office, all written and elechonic data was relinquished to the report
coordinator and then a final review was performed by the Project Manager.
AST-2025-0362-003 Tesoro - Salt Lake City, Uuh Page 3-4
=IAAI Example Calculations
IfirdoD
Soucr
Projet No.
RuNo.
Prrrmtcr(r)
Mctcr Pruruc @m), ll Bg
Pm
wh.rq
Md=
?h.rq
AH= Pb + 13f-
Pb 25.49 - buomtric prcrew, in. Hg
AH 1.900 = prdsuc diffcrcntial oforificc, ia HzO
Pm 25.63 - in. Hg
Abrolutc Strct Clr Prsruc (Pi), l|L Eg
PePs = Pb +:+. IJ.bwhcrctPb 25.49 : buomtric prclsuc, in. Hg
P8 0.33 = rtatic puruc, in- H2O
Ps 25.51 = i!. Hg
Strndrd Mctcr Volm (VEtd), drcf
l7.636xVmxPmxYvuEls---lm
wh.rc'Y 1.000 = mtcr corEtioo fsctorvmT3II-: mctcr volmq cf
Pm 25.63 = .blolutc mtcr prcssuc, in. Hgtm-3TiF= absotutc retcr tcry@hnre, oR
vmtd-?3il=drcf
SttDd.rd Wct VollE (Vf,ttd), 3cf
Vwstd= 0.04716xMc
rhcrc,
Mc 206.7 - wcight of H2O cotlcctc4 8v*stdTii--s"f
Moltturc tr'r.cdotr (BWSut). dlrrtlonl.li (thcorctlcd rt tstuntld condltlou)
1063?-(#:l)
whcrc, n^
Ts
-!&?-=
stack tcmpdatuc, oF
Pr4- absolutc rtack gs prcssuc, in. H8Bw$at 0.218 = dirensionlcss
Molrtuc Frecdon @lVS), dlmnrlodur
1063?-(#:l)
VwstdBWS =Altrrcld + llmctd'\
9.748 - rtandard wct voltm, scf43.7M = ttedard mtfi votw, &cf
-6.TEF= dimcnsionlcss
Molrtuc Fr.c6o[ (BWS), dlmBlorlsr
BWS = BWSmsd unless BWSsat < BWSmsd
whcrc,BWSet 0.218 = micturc fi'rtion (th@rctical at stunt d conditions)BWSsd_..]L!L= misnrc &rction (muucd)
BWSg
Molccdrr Wclgbt @RY) (Md),lMb-mlc
Vwrtd
Vmtd
BWS
(0.44 x o/oco) + (0.32 x o/oo2) + (0.28 (100 -
COr
-l]]9-
= carbon dioxidc concmrstion, %
O, L= oxygen coDccntration, o/o
Md 30.05 : lb/lb ml
VoCO2 - VoO2))
pul6rrpe
(j R (i U P
Ifirtio!
SoucG
Prolet Nc
RuNcPrrctcr(r)
Molcculr Wd3h (WET) (Mr[ llt/tbmlc
Ms = Md (1 - BWS) + 18.015 (BwS)
rbcrc,
-]!Q['
mloulu woight @RY), lb/lb ml
_..1[![- mirhrc frrctior, dimrionlcr27.86 -lb/lbml
AvcrrgG Vclclty (Vr), fi/rlc
_.-_-Vs = 85.49 x Cp x (APl/2)avg xrErqCp-..]qql--pitot nrbc ccffcimt
A P'o __.j,!]!- rvmgc prcbort tcrt vclcity hcad of rtrck gu, (in. H2O)ra
T, L- rmgc prchort trrt $6olut! stet trqcrrturc, oR
Pr 25.51 - rbrchlc ttek gu prcre, in HgMs 27.t6 " mleuh: wcight of rtack gu,lb/lb mlVr 53.4 - fl/scc
Avcrrgc SttcLGu I'lor.t Strchcoldtlou (Q.), rcftn
Qa=50xVsxAs
rhcrg
V. ::!!- - rtrck gar vclmity, ff/rcc
Ar 50.21 - crcs-ectioml ee of stacl, dQ@-*m
Avcnic Strclcu Flor rl Strndrrd Cmdldu (Qr)6 drtu
@ - 17.536 x Qa x (l - BWS) x
?harc,
a. _1ry_ - avcngc ract gu floy st ltrct mndition!, efuBWS 0.It2 -mistrrc frction, dimionlerPrE- rbdutc atrckgsprcre, in. HgTr 597.9 -svcngcprc&oltt ltsbslutcliettcqcntw,oRor-..EF-arca,
Dry Grr Mctrr Crllbrdor Ch.c& (Yqr), pGrccrt
Y-
xMd
Yqa =
vh:rq
g4-rotim.,min.
Vm 49.52t - tot l trtgr vohlE, dcfr*T - rbmluto Gtlrtc@oranrc, T'
AH@ 1.933 - orifcc rctd crlibntion cef6cimt, in. H2o
Pb
-!!1!!-
buoctic prcure, il Ifu
AHrvg-!ryg-- rvcragc prc!'W diffcmtid oforifcc, in H2O
Md
-!!1Q[-
mlccular wcight @RY), lMb ml
(A H)'o
-!.]!'
av@gc rqrre mt prcrre diffcrmtirl of orife, (in. H2O)r2
Yqr_!!_-pmat
Example Calculations
Md
BWS
Mr
P!
T!
9.
x
031
(;AH@
**-)/o
(,*
x 100
Example Calculations
Locetion: MPC-T"*oto
Source:
Run No. /ItlethodRun 1 / Method 3A
Or - Outlet Concentration (CsJ, Yo dry
co= (co6.-cs)x ,afftll
Cob. 4.39 : average analyzer value during test, % dry
C"-OF: average of pretest & posttest zero respoffles,Yo dry
Clar73F: actual concentration of calibration gas,%o dry
CM----00-: average of pretest & posttest calibration responses, o/o dry
CaViV: oz Concentation, % dry
Example Calculations
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project Xr.t
Run No. /lVlethod Run I / Method 6C
SOr - Outlet Concentration (C5s), ppmvd
cso,= (cou.-co)*( ctt'
' (Cu- Co
Cob. 0.13 : average analyzer value during test, ppmvd
C"
-0:T-:
average of pretest & posttest zero responses, ppmvd
CMA.T[5F: actual concentation of calibration gas, ppmvdCM-8T7F: averag€ of pretest & posttest calibration responses, ppmvd
Cso, -----0'56F : Soz Concentration, ppmvd
SOr - Outlet Concentration (C<SOrc0>), ppmvd @ioh O,
C<SOzcO>= Cso,X (
where,C<SOr> -0.060 : SO, - Outlet Concentration, ppmvdC6,ViT: oxygen concentation, o/o
C<SOzc0> -0.076 :ppmvd @0%O2
SOr - Outlet Emission Rate @R5sJ,lb/hr
C5s.xMWxQsx60ff x 2$2h
where,
where,
ERso,:
Cso,
MW
24.M ;#* 1.0E06 x453.59$
64.066
: SOz - Outlet Concentration, ppmvd: SOz molecular weigh! g/g-mole
-0.1
Qs 99,042 : stack gas volumetric flow rate at standard conditions, dsctnERso,.--T5s9, :lb/br
=raAI]EE)
, i.
Example Calculations
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source:ffi
Proiect Uo.:
Run No. /lVlethod Run I / Method 7E
NOx - Outlet Concentration (CNq), ppmvd
where,
cxo,= (co5.-cq)x , afft;)l
Cob, 0.00 = average analyzer value during test, ppmvd
C"-fF: average of pretest & posttest zero responses, ppmvd
CM^.-ffF: actual concentration of calibration gas, ppmvd
CM
-S0'2T-:
average of pretest & posttest calibration responses, ppmvd
CNo*-fF= NOx Concentation, ppmvd
NOx - Outlet Concentration (C<NOxcO>), ppmvd @0o/o O,
C<NOxcO>:
where,
CNo. x
Cro, 0.00 : NOx - Outlet Concentration, ppmvd
Cs,-i-: oxygen concenkation, o/o
CcNo*co,
-6]6T-
: ppmvd @oo/o o,
NOx - Outlet Emission Rate (ERNqJ,lb/hr
.L
oo _ _ CxonxMWxQsx60#x28.32 r;:Lr\Nox 24.04 ;h* l.oEo6 x453.592fi
where,
0.0C*o,
MW
: NOx - Outlet Concentration, ppmvd
: NOx molecular weight, g/g-mole
AIrl
Location: VtpC-feso.o - Salt L"ke Ciry
Source:ffi
Project Xr.t
Run No. /lllethod Run I / Method l0
CO - Outlet Concentration (Cqq), ppmvd
cco: (co6._c6)x ,"frfu;l
where,Cou. 5.38 : average analyzer value during test ppmvd
C"-trF: average of pretest & posttest zero responses, ppmvd
Cue700'5F: achral concentration of calibration gas, ppmvd
CM-3trt:fs-: average of pretest & posttest calibration responses, ppmvd
Cco.-.53-: CO Concentation, ppmvd
CO - Outlet Concentration (CcCOc0>), ppmvd @lYo Ot
C<COc0>:
where,
Cco x
Cco 5.53 : CO - Outlet Concentration, ppmvd
co,.7s-: oxygen concentration, o/o
C<Coco> T6T-: ppmvd @o% oz
CO - Outlet Emission Rate @fus),lb/hr
ERco:
mitr L
C66 x MW x Qs x 60; x28.32 O
24.04 ;*"* 1.0E06 x453.592ft
where,
5.5 : CO - Outlet Concentration, ppmvd: CO molecular weight, g/g-mole
Qs 99,M2 : stack gas volumetric flow rate at standard conditions, dscfrn
ERco-3-:lb/hr
Example Calculations
28.01
Cco
MW
=laAIIEE)SO2 Summary
MPC-Tesoro - Salt L^ake City Refinery, UTLocetion:
Source:
ProJect No.:
Wet Gas Scrubber - CEMS I
AST-2025-0362-003
Run
No.Dete Time Reference Method
SOr Concentrrtion
nnmvd
CEMS
SOr Concentretion
onmvd
Average
Difference
oomvdStertEnd
I
,,
3
4
5
6
7
8
9
2l
2t
2t
1t
)l
2l
2t
2t
.9t25
.9t25
.9125
,9t25
.9125
i9125
'.9125
t9t25
t9125
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:12
3:45
4:06
4:27
5:20
5:41
6:02
6:50
7:11
7:32
-0.060
-0.090
-0.1 l
-0.050
-0.r0
-0.10
-0.12
-0.1 I
-0.1 0
0.34
0.28
0.31
0.33
0.31
0.29
0.26
0.31
0.37
-0.40
-0.37
-0.42
-0.38
-0.41
-0.39
-0.38
-0.42
-0.47
Averase -0.093 0.31 -0.40
Standard Deviation (Sd)0.030
Applicable Source Standard (AS)L4
Confidence Coefficieirt (CC)0.023
Rehdve Accuncy (RA)3.O0 o/"
Performance Required - fuplicable Source Standard RA< t0%
Performance Specification Method PS2
Confidence Coefficient CC
cc = lto'It , sallVn I
where,
\.er L306 = degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd 0.030 : standard deviation ofdiflcrenceCC 0.023 = confidence coefficient
Relative Accurrcy, RA
ld l+ lcclRA =;3;;7pixloo
where,d -0.40 = average difference of Reference Method and CEMS
CC -6:dil = confi dence coelEcientAS_TaF-: applicable souce standard, ppmvd
RA 3.00 = relative accuracy, 7o
A/tGt SO2 Summary
Locetioo,
Source:
Project No.: AST-2025-0362-003
Confidence Coeflicient, CC
aa = lto'zt * rollVn I
where,
h9r L306 = degrees of frcedom value
n 9 = number ofruns selected for calculating the RASalTf+ = standard deviation of difference
CCTbx = confrdetrce coefficient
Reladve Accurecy, RA
ld I + lcclRA = 7ri;*pixloo
where,
d -0.51 = average differe,nce of Reference Method and CEMS
CC 0.026 = confidence coefficientAS 18.000 = applicable source standard, ppmvd @ 0 % Oz
RA 2.99 = relative accuracy, 7o
Run
No.Dete
Tlme Reference Method
SOr Concentredon
oomvd@07oOr
CEMS
S0: Concentndon
onmvd@0oloO,
Average
Difierence
oomvd@07oOrStrrtEnd
I
2
3
4
5
6
7
8
I
at
2l
1t
2l
2t
2l
2l
2l
2t
9t25
9t25
9125
9t25
9125
9t25
9t25
9125
9t25
13:25
13:46
14:07
15:00
l5:21
l5:42
16:30
l6:5 I
l7:12
13:45
l4:06
l4:27
l5:20
l5:41
l6:02
l6:50
l7:11
l'7:32
-0.076
-0.1I
-0.14
-0.064
-0.1 3
-0.13
-0.15
-0. l4
-0. l3
0.44
0.36
0.39
0.42
0.39
0.37
0.33
0.38
0.46
-0.52
-0.47
-0.53
-0.48
-0.52
-0.50
-0.48
-0.s2
-0.59
Average -0.12 0.39 -0.51
Standard Deviation (Sd)0.034
Applicable Source Standard (AS)l8
Confidence Coefficient (CC'0.026
Reladve Accurrcv (RA)2.99 y.
Performance Required - Applicable Source Standard RA< 10%
Performance Specification Method PS2
SO2 Summary
Locetion: MPC-Tesoro - Salt Lake Ciw Refinerv. UT
Srur.u,
ProJect No.: AST-2025-0362-003
Conlldence Coefficient CC
cc = lto'It , sallVn I
where,
h.sts-|[= degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd 0.032 = standard deviation ofdifference
CC 0.025 = confidsnce coefficient
Reletive Accuracy, RA
ld l+ lcclRA = 7s:;Tr:x 1oo
where,
d -0.40 = average difference of Reference Method and CEMS
CC 0.025 = confidence coefficient
AS 10.085 = applicable source standard, lb/br
RA 4.25 = relative accuracy, o/o
Run
No.Drte Time Reference Method
SOr Emicclon Rrte
lb/hr
CEMS
SO, Emisclon Rrte
lb/hr
Averege
Difference
lb/hrStrrtEnd
1
)
3
4
5
6
7
8
9
2fi9t25
2lt9l2s
2^9125
2lt9l2s
2119t25
2lt9l25
2tr9t25
2lt9l25
2n9t25
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
'l:12
,3:45
,4:06
,4:27
,5:20
t5:41
l6:02
l6:50
l7:ll
l7:32
-0.059
-0.089
-0.1 I
-0.05
-0.10
-0. l0
-0.t2
-0.1 I
-0.l0
0.3s
0.29
0.33
0.32
0.30
0.29
0.26
0.30
0.37
-0.41
-0.38
-0.44
-0.3'l
-0.40
-0.39
-0.38
-0.41
-0.47
Averasr -0.092 0.31 -0.40
Standard Dcviation (Sd)0.032
Applicable Source Standard (AS)l0
Conf dence Coeffi cient (CC)0_025
Reledve Accurecy (RA)4.25 o/.
Performance Required - Applicable Source Standard RA< l0%
Performance Specification Method PS2
NOx Summary
Locedon: MPC-Tesoro - Salt lake CiW Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
Run
No.Drte Tlme Reference Method
NOr Concenhedon
opmvd
CEMS
NOr Concentredon
nnmvd
Average
IXIerence
nnmvdStrrlEnd
I,
J
4
5
6
7
8
I
2^9t25
2/r9t25
2lt9l25
2n9125
2lt9l25
2n9125
yt9l25
2lt9l25
2n9t25
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:L2
3:45
4:06
4:27
5:20
5:41
6:02
6:50
7:ll
7:32
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
-0.01
0.00
0.00
0.00
0.00
0.00
0.00
Averagt 0.00 0.00 0.00
Standard Deviation (Sd 0.003
Applicable Source Standard (AS l6
Confidence Coefficient (CCl 0.003
Reladve Accurecy (RA)0.023./o
Performance Required - Applicable Source Standard RA< 10%
Performance Specifi cation Method PS2
Notc: Sincc abr(d) < CC, thc aystcm puscc thc biu tcst
Conlldence Coeflicient CC
cc = lto'?t, sallVn I
where,
h.e'zs
-|][
= degrees of freedom value
n 9 = nurnber ofruns selected for calculating the RA
Sd 0.003 = standard deviation ofdifferenceCC 0.003 = confidence coefficient
Rehdve Accuracy, RA
ld l+ lccltu{ - { ,')<1gg
where,
d 0.00 = average difference of Referei:ce Method and CEMS
CC T003 = confidence coefficient
AS-1534i-= applicable source standard, ppmvd
RA 0.02 _= relative acotracy,Yo
tIAAIIEE)NOx Summary
Locetion: MPC-Tesoro - Salt I.ake City Refinery, UT
Sror"",
ProJectNo.: AIT.ZQZ! Ql!2 QQ1
Conlldence Coefficient CC
cc = lto'3t r sallVn I
where,
to.ns L3O6 : degrees of freedom value
n 9 = number of runs selected for calculating the RA
Sd---616i-= standard deviation of difference
CC 0.003 = confidence coefficient
Reledve Accuncy, RA
ld l+ lcclRA : 7s;;TM xloo
whcre,
d 0.00 : average differe,nce of Reference Method and CEMS
CC -6:603-= confidence coefficient
As -rdT6q: applicable source standard, ppmvd @ 0 % or
RA 0O2 -= relative acatxacy,Yo
Run
No.Drte Tlme Reference Method
NOr Concentrrdon
oomvd@07oOr
CEMS
NOr Concentrrdon
oomvd@07nO,
Average
IXfference
opmvd@07cOrStrrtEnd
I
)
3
4
5
6
7
8
9
)t
2l
)t
2l
7l
)t
2l
2l
.ll
9t25
9t25
9t25
9125
9t2s
9t25
9125
9125
9t25
13:25
l3:46
l4:07
l5:00
l5.'21
l5:42
16:30
16:51
17:12
3:45
4:06
4:27
5:20
5:41
6:02
6:50
'1:ll
7:32
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
-0.01
0.00
0.00
0.00
0.00
0.00
0.00
Average 0.00 0.00 0.00
Standard Deviation (Sdl 0.003
Applicable Source Standard (ASl 20
Confi dence Coefficieirt (CC)0.003
Reletive Accurecy (RAl 0.018 %
Performance Required - Applicable Source Standard RA< 10%
Performance Specifi cation Method PS2
NOx Summary
Locedon: MPC-Tesoro - Salt take City Refinerv, UT
Sour""t
ProJect No.: AST-2025-0362-003
Conlidence Coefflclent, CC
cc = lto'gt r sallVn I
where,
\sts L306 = degrees offreedom value
n_2-=numberofrunsselectedforcalculatingtheRA
Sd 0.003 = standard deviation ofdifference
CC 0.003 = confidence coefficient
Reladve Accurecy, RA
ld I + lcclM = 73;ffix100
where,d 0.00 = average diference of Reference Method and CEMS
CC 0.003 = confidence coefficient
AS 11.206 = applicable source standard, lb/hr
RA 0.03 = relative accuracy, oZ
Run
No.Dete Time Reference Method
NOr Emission Rrte
lb/hr
CEMS
NOx Emlcsion Rrte
Ib/hr
Averrge
Dllfcrence
lb/hrStrrtEnd
I
2
3
4
5
6
7
8
9
2l
2l
1t
,,1
2l
2l
a
2t
2l
9t25
9t25
9t25
9125
9t25
9t25
9125
9t25
9t25
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:12
13:45
14:06
14:27
l5:20
15:41
l6:02
16:50
l7:l I
17:32
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
-0.01
0.00
0.00
0.00
0.00
0.00
0.00
Average 0.00 0.00 0.00
Standard Deviation (Sd)0.003
Applicable Source Standard (AS)ll
Confi dence Coeffi cient (CC)0.003
Reledve Accurecy (RA)0.033 %
Performance Required - Applicable Source Standard RA< 10%
Performance Specification Method PS2
Locetion: MPC-Tesoro - Salt lake CiW Refinerv. UT
Source: Wet Cas Scrubber - CEMS I
Project No.: AST-2025-0362-003
Run
No.Date Tlme Refcrence Mcthod
CO Concentrrtion
oomvd
CEMS
CO Concentredon
oomvd
Averrge
Dilference
oomvdStrrtEnd
I
a
3
4
5
6
7
8
9
2/r9t25
2lt9l25
2lr9t25
2n9t2s
2lr9t25
2^9t25
2^9t25
2lt9l25
2t19t2s
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:12
3:45
4:06
4:27
5:2O
5:41
6:02
6:50
7:ll
7:32
5.53
5.79
2.82
3.46
1.16
0.066
0.00
0.49
0. 15
8.87
9.14
6.76
7.30
4.59
3.25
2.38
3.35
2.77
-3.34
-3.35
-3.94
-3.84
-3.43
-3. 18
-2.38
-2.86
-2.62
Averasr 2.t6 5.38 aa1
Standard Deviation (Sd 0.521
Applicable Source Standard (AS'396
Confidence Coefficient (CC'0.401
Reletive Accurecy (RAl 0.91 o/"
Perfiormance Required - Applicable Source Standarc RA< 5%
Alternative Performance Re4uired (d + CC.<5pom
Performance Soecification Metho(PS 4A
Confidence Coefficient, CC
cc = lto'?'r sallVn I
where,
h3r 2.306 = degrees of freedom value
n 9 : number ofruns selected for calculating the RA
Sd......l.lil: standard deviation of difference
CC 0.401 = confidence coefficient
Relative Accuracy, RA
ld I + lcclRA =;3;;7pix1oo
where,
d, -f .22 : average difference of Reference Method and CEMS
CC -0-301- = confidence coefficient
AS 396.013 _=applicablesourcestandard, ppmvd
RA 0.91 -= relative accuracy, 7o
=laAITEE)CO Summary
Location: MPC-Tesoro - SAt Ut. Citv f.fi"".v, Uf
Souaaa,
ProJect No.: AST-2025-0362-003
Confidence Coeflicient CC
cc = lto'ut r sallVn I
whcre,
4.ns
-\=
degrees of freedom value
n 9 = numbcr ofruns selected for calculating the RA
Sd 0.686 = standard deviation ofdifference
CC 0.527 = confidence coefficient
Rehtive Accurecy, RA
ld l+ lcclfuq = ---l--:==--1199
where,d -4.08 = average difference of Reference Method and CEMSCC 0.527 = confidence coefficientAS 500.000 = applicable source sundard, ppmvd, @ 0 Yo Oz
RA 0.92 = relative accuracy, 7o
Run
No.Drte Time Reference Method
CO Concentredon
oomvd (O 0 7. O,
CEMS
CO Concentredon
oomvd tO 0 7o Or
AYerrg€
Dilference
oomvd tO 0 7. O,Strrl End
I
2
3
4
5
6
7
8
9
2tL9t25
2^9t25
2lt9l25
2tL9t25
2lt9l25
2n9125
2lt9l25
2n9t25
2lt9l25
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:12
3:45
4:06
4:27
5:20
5:41
6:02
6:50
7:ll
7:32
7.00
7.27
3.57
4.40
r.4't
0.084
0.00
0.61
0. l8
tr.26
11.49
8.60
9.12
5.85
4.t2
3.00
4.19
3.49
4.26
4.22
-5.03
4.92
*4.38
-4.04
-3.00
-3.58
-3.31
Averagt 2.73 6.81 -4.08
Standard Deviation (Sd 0.686
Applicable Source Standard (AS)500
Confi dence Coeffi cient (CC)0_527
Relrtive Accuncy (RA)0.92 o/"
Performancc Required - Applicable Source Standard RA< 5%
Performance Soecifi cation Method PS 4A
02 SummaryIEE)tlaAI
Locrtion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
Run
No.Date Time Reference Method
Or Concentredon
Vo dry
CEMS
O, Concentrrtion
c/" dw
Averrge
Dilference
o/. ilrvSt rt End
I
)
3
4
5
6
7
8
9
2t19l25
2^9t25
2lt9l25
2lt9l2s
2^9t25
2t19t25
2^9t25
2^9125
2^9t25
3:25
3:46
4:07
5:00
5:21
5:42
6:30
6:51
7:12
3:45
4:06
4:27
5:20
5:41
6:02
6:50
7:11
7:32
4.39
4.24
4.42
4.4't
4.47
4.39
4.29
4.16
4.29
4.M
4.29
4.48
4.52
4.50
4.4t
4.33
4.r9
4.33
-0.05
-0.05
-0.06
-0.05
-0.03
-0.02
-0.04
-0.03
-0.M
Av€rage 4.35 4.39 -0.04
Standard Deviation (Sd)0.013
Confidence Co€ffi cietrt (CC)0.010
Reletive Accurrcy (RA)l.l7 o/o
Performance Required - Mean Refer€nce Method RA< 20%
Performarce Specification Method PS3
Confldence Coelficient CC
cc = lto'I" sallVn I
where,
\.er
-!\=
degrees of freedom value
n 9 = number of runs selected for calculating the RA
Sd 0.013 = standard deviation ofdifference
CC 0.010 = conlidence coefficient
Reletive Accurecy, RA
ld l+ lc6lRA =;3;;;7:x1oo
where,
d -0.04 = average differeirce of Reference Method and CEMS
CC 0.010 = confidence coelficient
RM 4.347 = reference method,% dry
RA l.Ll -= relative accuracy, 7o
\IFR Summarypul6rrcEr
r, .., ,[] ) i:
ProJect No.: AST-2025-0362-003
Run
No.Drte Tlme Reference Method
Flow Rete
dscfm
CEMS
Flow Rrte
dscfm
Averrge
Difference
dscfmSttrtEnd
1
.,
3
4
5
6
7
8
9
2t
)l
2t
2l
2t
2t
)t
2l
2t
9/25
9t25
9t25
9125
9125
9t25
9t25
9t25
9t25
3:28
3:50
4:10
5:05
5:25
5:45
6:35
6:55
7:15
3:32
3:55
4:15
5:10
5:30
5:50
6:40
7:00
7:20
99,042
98,698
98,206
98,84 I
98,738
97,967
99,028
98,674
98.926
I 02,698
t02,659
106,55 I
99,692
99,545
rot,4t2
98,369
97,833
101.822
-3,656
-3,961
-8,345
-850
-808
-3,445
660
842
-2,896
Average 98,680 101,176 -2,496
Standard Deviation (Sd)2,860
Coafi deirce Coeffi cient (CC )2 198. I 15
Reledve Accurecy (RAl 4.76 Y.
Acceptability Critcria - Mean Rcfercnce Metho<s20%
Performance Specification Metho<PS5
Conlldence Coeflicieni CC
cc = lto'It , sallVn I
where,
ht t L= degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd 2.859.65 = standard deviation ofd.iffereirce
CC 2,198.1I = con-fidence coefficient
Reledve Accurecy, RA
ld I + lcclRA - ' '-:x100
where,
d -2,495.54 = average difference of Reference Method and CEMSCC 2,198.1I = confidencc coefficientRM 98,679.96 - refcrence metho4 dscfoRA 4.76 = relative accuracy, 7o
olUIrl
cl>t
a\
Eac
a
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Runl-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, IJT
Source: Wet Gas Scrubber - CEMS I
Project No.: A5T-2025-0362-003
Date:2119125
Time
Unit
Stetus
Uncorrected Run Average (Cour)
Cal Gas Concentrgtion (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run Averase (Co
13:25
13.,26
13:27
13:28
13:29
l3:30
l3:3 I
13:32
l3:33
13:34
l3:35
l3:36
13:37
l3:38
l3:39
l3:40
l3:41
13:42
13:43
13:44
13:45
Or - Outlet
%o dry
Valid
CO - Outlet
ppmvd
Valid
s.38
400.00
0.00
0.00
0.00
389.67
389.22
389.45
5.53
6.36
6.1
5.50
4.62
s.09
6. l9
4.91
s.44
4.87
4.92
5. l6
5.85
6.27
6.l3
s.99
s.49
5.40
5.23
4.62
4.55
4.32
NOx - Outlet
ppmvd
Valid
0.00
80.00
0.00
0.00
0.00
80.45
79.97
80.21
0.00
0.00
0.00
0.00
0.03
0.04
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
SOr - Outlet
ppmvd
Valid
4.39
4.00
0.00
0.00
0.00
4.01
3.99
4.00
4.39
0.13
80.00
0.20
0.18
0.19
81.37
82.02
81.70
-0.06
4.29
4.37
4.s8
4.71
4.81
4.44
4.50
4.51
4.4s
4.30
4.29
4.21
4.18
4.30
4.37
4.47
4.43
4.32
4.27
4.14
4.15
0.10
0.1I
0.1I
0.13
0.13
0.13
0.16
0.14
0.10
0.1I
0.10
0.18
0.14
0.t7
0.12
0.16
0.13
0.12
0.t7
0.10
0.10
AI =larEe Run2-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025 -03 62-003
Dtte:2/19/25
Time
Unit
Status
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Crvr)
Corrected Run A Corr
Or - Outlet
%o ilry
Valid
CO - Outlet
ppmvd
Valid
5.il
400.00
0.00
0.00
0.00
389.67
389.22
389.4s
5.79
4.14
4.12
4.44
4.95
5.72
4.92
4.87
4.07
6.72
7.t6
4.77
4.80
4.tt
4.42
4.71
4.84
6.36
t2.36
9.86
6.32
4.7s
NOx - Outlet
ppmvd
Valid
0.00
80.00
0.00
0.00
0.00
80.4s
79.97
80.21
0.00
SOr - Outlet
ppmvd
Valid
4.24
4.00
0.00
0.00
0.00
4.01
3.99
4.00
4.24
0.10
80.00
0.20
0.18
0.l9
8 1.37
82.02
81.70
-0.09
13:46
13:47
l3:48
13:49
l3:50
l3:51
13:52
l3:53
13:54
l3:55
l3:56
l3:57
l3:58
l3:59
l4:00
l4:01
l4:02
l4:03
l4:04
l4:05
l4:06
4.t7
4.23
4.r2
4.16
4.07
4.23
4.29
4.25
3.97
4.r4
4.36
4.s2
4.6t
4.60
4.42
4.2s
4.02
3.91
4.13
4.2s
4.3s
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.1I
0.17
0.17
0.16
0.06
0.10
0.10
0.14
0.04
0.07
0.02
0.1I
0.06
0.09
0.12
0.10
0.07
0.10
0.12
0.07
0.06
Run3-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: A5T-2025-0362-003
Dzte:2/19/25
Time
Unit
Status
Or - Outlet
u/o ilry
Valid
4.42
4.00
0.00
0.00
0.00
4.01
3.99
4.45
4.s4
4.56
4.s4
4.45
4.24
4.30
4.34
4.41
4.42
4.34
4.30
4.38
4.52
4.61
4.58
4.40
4.29
4.29
4.31
4.48
CO - Outlet
ppmvd
Valid
2.74
400.00
0.00
0.00
0.00
389.67
389.22
389.4s
2.82
3.67
3.21
2.99
2.76
2.78
3.51
3.22
3.s0
2.56
2.08
2.29
2.00
2.38
2.78
3.28
2.74
2.52
2.46
1.90
2.05
2.94
NOx - Outlet
ppmvd
Valid
0.00
80.00
0.00
0.00
0.00
80.4s
'19.97
80.2r
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
SOr - Outlet
ppmvd
Valid
0.07
80.00
0.20
0.18
0.19
81.37
82.02
81.70
0.07
0.02
0.r2
0.08
0.09
0.06
0.09
0.09
0.06
0.09
0.13
0.08
0.07
0.07
0.08
0.0s
0.08
0.07
0.04
0.05
0.09
Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
l4:07
l4:08
l4:09
l4:10
l4:ll
l4:12
l4: l3
l4:14
l4: l5
14:16
l4:17
l4:18
l4:19
l4:20
l4:21
l4:22
l4:23
l4:24
l4:25
l4:26
l4:27
4.00
4.42
AI =IAIGE)Run4-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No. : AST-2025 -03 62-003
D*ez 2ll9l25
Time
Unit
Status
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cp1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cel Response
Average Cal Response (Cru)
Corrected Run A
l5:00
15:01
15:02
l5:03
l5:04
l5:05
l5:06
l5:07
l5:08
l5:09
l 5:10
l5:l I
l5:12
15: l3
l5: l4
l5: l5
l5: l6
l5:17
l5:18
l5: l9
l5:20
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
3.37
400.00
0.00
0.00
0.00
389.22
389.24
389.23
3.46
5.37
5.24
4.76
3.95
3.50
3.44
3.40
2.61
2.71
3.53
3.27
4.68
4.06
3.21
3.22
2.63
2.89
2.46
2.04
2.12
1.65
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
4.45
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.47
0.00
80.00
0.00
0.00
0.00
79.97
78.58
79.33
0.00
0.13
80.00
0.18
0.17
0.18
82.02
81.68
81.85
-0.05
4.69
4.44
4.s2
4.s9
4.66
4.82
4.89
4.64
4.50
4.51
4.42
4.40
4.32
4.29
4.22
4.2s
4.l s
4.10
4.25
4.36
4.s3
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.15
0.16
0.12
0.13
0.12
o.t2
0.t2
0.16
0.14
0.13
0.1I
0.17
0.1I
0.09
0.1I
0.14
0.10
0.22
0.10
0.05
0.08
AI
-Ir
Locetion: MPC-Tesoro - Salt Lake City Refinerv, UT
Run5-RMData
Source: Wet Gas Scrubber - CEMS I
Proj ect No. : AST-2025 -03 62-003
Datez 2/19125
Time
Unit
Stetus
Uncorrected Run Average (Cou)
Cal Gss Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Averege Cal Response (CM)
Corrected Run A
Or - Outlet
Yo ilrl
Valid
CO - Outlet NOx - Outlet SOr - Outletppmvd ppmvd ppmvd
Valid Valid Valid
0.00 0.074.46
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.47
400.00
0.00
0.00
0.00
389.22
389.24
389.23
1.16
1.83
1.66
1.46
t.32
1.09
1.35
1.63
2.66
1.45
0.91
0.99
1.03
1.07
1.00
l.l0
1.02
0.45
0.58
0.31
0.41
0.38
80.00
0.00
0.00
0.00
79.97
78.68
79.33
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
80.00
0.18
0.t7
0.18
82.02
81.68
81.85
-0.10
l5:21
l5:22
l5..23
l5.,24
l5:25
l5:26
l5:2'l
l5:28
l5:29
15:30
l5:31
l5:32
l5:33
l5:34
l5:35
l5:36
l5:37
l5:38
l5:39
l5:40
l5:41
4.54
4.51
4.45
4.33
4.44
4.49
4.19
4.07
4.28
4.43
4.59
4.s0
4.s4
4.74
4.81
4.66
4.63
4.4s
4.35
4.37
4.24
0.07
0.09
0.09
0.05
0.0s
0.04
0.07
0.06
0.11
0.1I
0.09
0.05
0.08
0.08
0.06
0.03
0.07
0.10
0.07
0.06
0.t2
AI =lalEE)Run6-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
D*e;2119125
Time
Unit
Status
Or - Outlet
%o drl
Valid
CO - Outlet
ppmvd
Valid
0.06
400.00
0.00
0.00
0.00
389.22
389.24
389.23
0.07
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
4.38
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.39
0.00
80.00
0.00
0.00
0.00
79.97
78.68
79.33
0.00
0.07
80.00
0.18
0.17
0.18
82.02
81.68
81.85
-0.10
l5:42
l5:43
l5:44
15:45
l5:46
l5:47
l5:48
l5:49
15:50
15:51
l5:52
l5:53
l5:54
15:55
l5:56
l5:57
l5:58
l5:59
16:00
l6:01
l6:02
4.34
4.37
4.46
4.29
4.38
4.53
4.s4
4.47
4.0'7
4.19
4.29
4.32
4.31
4.40
4.32
4.20
4.37
4.44
4.42
4.60
4.64
0.08
0.08
0.06
0.1I
0.09
0.09
0.12
o.t2
0.06
0.10
0.05
0.08
0.07
0.06
0.02
0.08
0.07
0.05
0.08
0.0s
0.03
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.02
0.20
0.09
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.07
0.03
o.t2
0.49
0.34
0.00
0.00
0.00
0.00
0.00
0.00
plll6rrpE)
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
RunT-RMData
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
Dste:2119/25
Time
Unit
Status
O: - Outlet
Yo ilry
Valid
4.28
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.29
4.s9
4.46
4.49
4.49
4.s2
4.51
4.41
4.31
4.29
4.26
4.2t
4.19
4.09
4.12
4.t6
4.27
4.27
4.13
4.00
4.02
4.O4
CO - Outlet
ppmvd
Valid
0.00
400.00
0.00
0.00
0.00
389.24
388.00
388.62
0.00
NOx - Outlet
ppmvd
Valid
SO: - Outlet
ppmvd
Valid
Uncorrected Run Averege (Cour)
CaI Gas Concentretion (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zrro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Averege Cal Response (CM)
Corrected Run A
l6:30
l6:31
l6:32
l6:33
l6:34
l6:35
l6:36
l6:37
l6:38
l6:39
l6:40
l6:41
l6:42
l6:43
l6:44
l6:45
l6:46
l6:47
16:48
l6:49
l6:50
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.M
0.00
80.00
0.00
0.00
0.00
78.68
78.60
78.&
0.00
0.05
80.00
0.t7
0.17
0.17
81.68
82.2s
81.97
-0.12
0.06
0.08
0.03
0.07
0.06
0.04
0.04
0.03
0.06
0.06
0.02
0.07
0.0s
0.07
0.04
0.04
0.02
0.06
0.05
0.06
0.08
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Run8-RMData
Locetion: MPC-Tesoro - Salt Lake CiW Refinerv. UT
Source: Wet Gas Scrubber - CEMS I
Project No.: A5T-2025-0362-003
Dilez 2/19125
Time
Unit
Status
Uncorrected Run Average (Cou,)
Cel Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cnr)
Corrected Run A Corr
Or - Outlet
oh dry
Valid
CO - Outlet
ppmvd
Valid
0.48
400.00
0.00
0.00
0.00
389.24
388.00
388.62
0.49
0.00
0.00
0.00
0.00
0.01
0.22
l.l5
1.60
2.46
1.99
1.32
0.71
0.s7
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
NOx - Outlet
ppmvd
Valid
0.00
80.00
0.00
0.00
0.00
78.68
78.60
78.64
0.00
SOr - Outlet
ppmvd
Valid
4.ls
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.16
0.06
80.00
0.17
0.17
0.17
81.68
82.25
81.97
-0.1I
l6:51
l6:52
l6:53
l6:54
l6:55
l6:56
l6:57
l6:58
l6:59
l7:00
l7:01
17:02
l7:03
17:04
l7:05
17:06
17:07
l7:08
17:09
l7: l0
l7:ll
4.08
4.10
4.07
3.99
4.00
4.01
4.00
4.07
4.10
4.18a))
4.16
4.20
4.25
4.28
4.32
4.2r
4.07
4.20
4.3r
4.29
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.07
0.08
0.03
0.08
0.08
0.03
0.07
0.05
0.03
0.04
0.03
0.06
0.06
0.0s
0.05
0.06
0.04
0.05
0.05
0.08
0.09
=laAI!EE)Run9-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No. : AST-2025 -0362-003
D*e:2119125
Time
Unit
Status
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
0.14
400.00
0.00
0.00
0.00
389.24
388.00
388.62
0.00
0.00
0.00
0.00
0.00
0.00
0.43
1.82
0.00
0.00
0.00
0.00
0.00
0.32
0.04
0.00
0.04
0.17
0.15
0.02
0.00
NOx - Outlet
ppmvd
Valid
0.00
80.00
0.00
0.00
0.00
78.68
78.60
78.64
0.00
SOr - Outlet
ppmvd
Valid
0.07
80.00
0.17
0.17
0.17
81.68
82.25
8l.97
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
4.28
4.00
0.00
0.00
0.00
3.99
3.99
3.99
4.29
17:12
l7:13
17:14
l7:15
17:16
17:17
l7:18
17:19
17:20
17:21
17:22
17:23
l7:24
17:25
17:26
l7:27
17:28
l7:29
l7:30
l7:31
17:32
4.30
4.2s
4.27
4.30
4.31
4.43
4.43
4.32
4.2s
4.23
4.r6
4.23
4.20
4.03
4.19
4.33
4.40
4.38
4.38
4.27
4.18
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.03
0.03
0.05
0.10
0.07
0.06
0.02
0.05
0.04
0.09
0.04
0.08
0.08
0.07
0.09
0.07
0.06
0.13
0.11
0.07
0.06
pJ/lflrrpe
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Location MPC-Tesoro - Salt Lake Citv Refinery. UT
Source Wet Gas Scrubber - CEMS f
Project No. A5T-202$0362'003
D*e 2ll9l25
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tcE)=laAI SO2 Summary
Loce6on: MPC-Tesoro - Salt lake City Refinery, UT
Source,
Prolect No.: AST-2025-0362-003
Conlldencc Coefllclent CC
cc = lto'zt , sallVn I
where,
to.e75 2.306 - degrees offreedom value
n 9 = number of runs selectcd for calculating the RA
sd-dTil= standard deviation of differeEce
CC T.o'71 = confidence coefficient
Rehtive Accurscy, RA
ld I + lcclp.,q = *--#x100
where,
d -0.12 = avcrage difference of Reference Method and CEMS
CC 0.071 = confideace coefficient
AS 14.2'17 - applicable source standard, ppmvd
RA 1.35 = relative accuracy, oZ
Run
No.Drte Tlme Referencc Method
SOr Concentredou
oomvd
CEMS
SOr Concentredon
oomvd
Avenge
Difference
oomvdStrrtEnd
I
2
3
4
5
6
7
8
9
2t20t25
2t20t25
2l20l2s
2120125
2120125
2t20t25
2120125
2t20t25
u20t25
):10
):3 I
t..52
0:40
l:01
L:22
2:10
2:31
2:52
9:30
9:51
I0: l2
I l:00
Il:21
ll:42
I2:30
I2:5 I
I 3:12
-0.090
-0.r00
-0.080
-0.250
-0.050
0.010
0.120
0.070
-0.010
0.00
0.00
0.00
0.04
0.17
0.19
0.12
0.10
0. l0
-0.09
-0.10
-0.08
-0.29
-0.22
-0.18
0.00
-0.03
-0.1 1
Av€rag(-o.042 0.080 -0.1 2
Standard Deviation (Sdl 0.092
Applicable Sourcc Standard (AS L4
Confidence Coefficient (CCl 0.071
Relrtive Accuracy (BA)135 V"
Performance Required - Applicable Source Standard RAs l0%
Performance Specification Methm PS2
=raAI SO2 Summary
MPC-Tesoro - Salt I4ke Ciw Refinery, IJTLocetion:
Source:
ProJect No.:
W€t Gas Scrubber - CEMS 2
AST-2025-0362-003
Run
No.Dete Tlme Refercnce Method
SO, Concentrrdon
pomvd@0oloO,
CEMS
SOz Concentradon
pomvd@07nO:
Averege
Difference
npmvd@07nO,Strrt End
I
2
1
4
5
6
7
I
9
2t20t25
2t20t25
2t20/2s
2t20t25
2120125
2t20t25
2120t25
2120125
2t20t25
9: l0
9:31
9:52
t0:40
t l:01
ll:22
12:10
l2:31
l2:52
9:30
9:51
l0:1 2
I l:00
1l:21
ll:42
12:30
12:51
13:1 2
-0.1 I
-0.13
-0.r0
-0.32
-0.063
0.013
0.15
0.089
-0.0 l3
0.00
0.00
0.00
0.05
0.22
0.24
0.15
0.13
0.13
-0.1 t
-0. l3
-0.10
-0.37
-0.28
-0.23
0.00
-0.04
-0_ l4
Averagt -0.054 0.0 -0. l6
Standard Deviation (Sdl 0.1 l7
Applicable Sowce Stardard (ASl 18
Confidence Coefficient (CCl 0.090
Rehtive Accurecy (RAl 137 e/o
Performance Required - Applicable Source Standard RA< l0%
Performance Specifi cation Methoc PS2
Confidence Coeflicient CC
cc = lto'It r sallVn I
where,
h.er
-!{=
degrees of freedom value
n 9 = number of runs selected for calculating the RA
Sd-d,.lF= shndard deviation of diffcrence
CC 0.090 = confideirce coefficient
Relative Accurecy, RA
ld l+ lcclRA = 73;;77' xloo
where,d -0. I 6 = average differeirce of Reference Method and CEMSCC 0-090 = confidence coefficient
As
_-iI_.000-:
applicable source standard, ppmvd @ 0 Vo oz
RA 137 -= relative accuracy, 9ir
IEE!:-,:'=taAI SO2 Summary
Locedon:
Source:
ProJect No.: AIT2QZ! Q!2 9Q1
Conlldence Coefllcient, CC
cc = lto'3t, sallVn I
where,
h.e75 2.306 = degrees oftcedom valuc
n 9 = number ofruns selected for calculating the RA
Sd-dlil= standard deviation of difference
cc i-o-70-= confidence coefficient
Reletive Accuracy, RA
ld I + lcclRA = 73;ffix100
where,d -0.12 = average difference of Reference Method and CEMSCC 0.070 = confidence coefficient
AS 10.063 = applicable source standard, lbAr
RA 1.93 = relative acorrcy,Vo
Run
No.Drte Time Reference Mcthod
SOr Emission Rete
lb/hr
CEMS
SO: Emlsslon Rate
lb/hr
Averege
Dlfference
lb/hrStrrtEnd
I
2
3
4
5
6
7
8
9
2120125
2t20t25
2t20t25
2t20t25
2t20t25
2t20t25
2120125
2t20t25
2120l2s
9:10
9:31
9:52
l0:40
I 1:01
ll:22
l2: l0
l2:31
l2:52
9:30
9:51
l0:12
1 l:00
ll.,21
ll:42
l2:10
l2:51
13:12
-0.089
-0.099
-0.078
-0.24
-0.049
0.010
0.r2
0.068
-0.010
0.00
0.00
0.00
0.04
0.18
0.r9
0.12
0.11
0.1I
-0.09
-0.10
-0.08
-0.28
-0.23
-0.18
0.00
-0.04
-0.12
Averagt -0.M2 0.083 -0.12
Standard Deviation (Sd)0.091
Applicable Source Standard (AS)l0
Confdence Coefficient (CCl 0.070
Relrdve Accurecy (RA)1.93 Vo
Pcrformance Required - Applicable Source Standard RA< 10%
Performance Spccification Method PS2
FlaAI NOx
Locrtion: MPC-Tesoro - Salt Lake Citv Refinery, UT
Soraau,
Project No.: 4ST4a2l Q!2 aal
Notc: Siacc abs(d) < I ppD. thc syst@ pass.s thc biN tcst
Confldence Coefficlent, CC
cc = lto'3t, sallVn I
where,
h.sts
-|[=
degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd-d,F= standard deviation of difference
CC 0.172 = con-fidence coefficient
Reletive Accurecy, RA
ld I + lcclM = 73;;7p:x1oo
where,d 0.87 = average difference of Reference Method and CEMS
CC 0.172 = confidence coefficient
AS 15.863 = applicable source standard, ppmvd
RA 6.55 = relative acasacy,o/o
Run
No.Drte Tlme Reference Method
NOr Concentredon
nnrnvd
CEMS
NOr Concentrrtlon
oomvd
Averrge
IXfference
oomvdStrrtEnd
I
2
3
4
5
6
7
8
9
2120125
2120125
?/20t25
2t20t25
2120125
2t20125
2120125
2t20t2s
2t20t25
9: l0
9:31
9:52
I0:40
t l:01
ll:22
t2: l0
l2:31
l2:52
):30
):5 1
0:12
l:00
l:21
l:42
2:30
2:51
3:12
3.19
2.50
3.10
3.22
r.47
t.22
1.96
4.84
4.44
2.35
1.57
2.02
2.35
0.77
0.67
r.37
3.64
3.39
0.84
0.93
1.08
0.87
0.70
0.55
0.59
1.20
1.05
Averagr 2.88 2.01 0.87
Standard Dwiation (Sd)o.223
Applicable Source Standard (AS 16
Confi dence Coeffi cient (CC)0.172
Reledve Accuracy (RA)6.55 o/"
Performancc Required - Applicable Source Standard RA< 10%
Performance Specification Method PS2
NOx Summary
Locedon: MPC-Tcsoro - Sdt l*e Citv Refuay, m
Source:M
ProJect No.: AST-2025-0362-003
Conlldence Coelficlent, CC
cc = lto'I'" sallVn I
where,
h.er 2306 = degrees of freedom value
n 9 = number ofruns selected for calculating the RA
SdT = standard deviation of difference
cC i-.il = confi dence coeffi cient
Reledve Accurrcy, RA
ld I + lcclM = 7ri;7pix1oo
where,
d 1.09 = average difference of Reference Method and CEMS
cc -...'l.F = confidence coefficient
AS -rb'000 = applicable source standard, ppmvd @ 0 % OzRA 6.49 = relative accuracy, 7o
Run
No.Drte Time Reference Method
NOx Concenredon
oomvd tO 0 7. O'
CEMS
NOr Concentrrdon
onmvd@07oO,
Average
Difference
oomvd@07cOrStrrtEnd
I
2
3
4
5
6
7
8
9
2t20t25
2t20t25
2t20125
2t20125
2120125
u20t25
2t20125
2t20t25
2t20125
9:10
9:31
9:52
l0:40
ll:01
ll.,22
l2:10
l2:31
l2:52
9:30
9:51
t0: l2
t l:00
t1:21
ll:42
l2:30
t2:51
13:12
4.01
3.t4
3.89
4.10
1.86
1.54
2.46
6.t2
5.60
2.96
1.98
2.55
2.99
0.98
0.85
t.72
4.62
4.30
1.05
I.16
1.34
l.l I
0.88
0.69
0.74
1.50
1.30
Averaqe 3.U 2.55 1.09
Standard Deviation (Sd)0.277
Applicable Source Standard (AS)20
Confidence Coefficient (CC)0.213
Rehdve Accurrcy @A)6.49 Y.
Performance Required - Applicable Source Standard RA< l0%
Performance Specifi cation Method PS2
=TAAI NOx Summary
Locedon: MPC-Tesoro - S"lt t k" Citv R"fio".y, UT
Soraaat
Project No.: AST-2Q25-!!!2-!E
Confidence Coelliclent CC
cc = lto'xt * sallVn I
where,
h.e?5 2.306 = degrees offreedom value
n 9 = number ofruns selected for calculating the RA
Sd........-ffi= standard deviation of difference
CC 0.1 l5 = confidence coefficient
Reledve Accurecy, RA
ld l+ lcclRA = 73i;7p:x1oo
where.
d 0.54 = average difference of Reference Method and CEMSCC 0.115 = confidence coefficient
As -ffi= applicable source standard, lb/hr
RA 5.90 = relative accuracy, oZ
Run
No.Date Time Reference Method
NOr Emlsrlon Rete
lb/hr
CEMS
NOr Emlsclon Rete
lb/hr
Averrge
Difference
lb/hrStrrtEnd
I
2
3
4
5
6
7
8
9
2t20t2s
2120125
2t20t25
2t20t25
2t20t25
2120125
u20t25
2t20t25
2t20125
):10
):3 I
):52
0:40
I :01
l:22
2:10
2:31
2:52
9:30
9:51
t0: l2
t l:00
tl:21
ll:42
l2:30
l2:51
I3: l2
2.27
1;17
2.18
2.26
l.M
0.86
1.3 8
3.37
3.13
1.79
1.09
t.49
r.79
0.55
0.51
1.04
2.69
2.42
0.48
0.68
0.69
0.47
0.49
0.35
0.34
0.68
0.71
Averacr 2.03 1.49 0.54
Standard Deviation (Sd'0.1 50
Applicable Source Standard (AS'll
Confi dencc Coefficient (CC'0.1 15
Reletive Accuncy (RAl 5.90 V"
Performance Required - Applicable Source Standar<RA< 10%
Performance Spccification Metho<PS2
=laAI CO Summary
Locedon: MPC-Tesoro - Salt [ake City Re6aery, UT
Sor"aa,
Prolect No.: AST-2q25-0362-003
Confldence Coefficient, CC
]EE)
L ., F ) .l i
Run
No.Dete
Tlme Refercnce Method
CO Concentredon
onmvd
CEMS
CO Concentredon
nomvd
Average
Dilferencc
oomvdStrrtEnd
I
2
3
4
5
6
7
8
9
2t20t25
2t20t25
2t20t25
2t20t25
2t20125
2120125
2t20125
2120t25
2120125
9:10
9:31
9:52
t0:40
t1:01
ll:22
t2:10
l2:31
l2:52
9:30
9:51
l0:12
I l:00
I l:21
ll:42
I2:30
t2:51
13:12
t5.52
t5.77
13.67
15.05
22.75
22.35
14.22
t2.37
12.30
10.86
I 1.94
9.91
10.94
18.65
18.13
10.44
8.09
8.05
4.66
3.83
3.76
4.11
4.10
4.22
3.78
4.28
4.2s
Averaqe 16.00 I 1.89 4.11
Standard Deviation (Sdl 0.292
Applicable Source Standard (ASl 397
Confi dcnce Cocffi cicnt (CCl 0.224
Reledve Accurecv (RA 1.09 o/o
Performance Required - Applicable Soruce St ndard RAS 5%
Performance Specification Method PS 4A
cc=lff,sal
where,
h.er _\- degrees of freedomvalue
n 9 = number of runs selectcd for calculating the RA
Sd-d292 : standard deviation of differ€nce
ccT : confi dcnce coeffi cient
Reledve Accurrcy, RA
ld I + lcclRA = #x100
where,
d 4.11 = average difference of Reference Method and CEMS
CC O.2A = confidence coefficient
AS 396.5'll = applicable source stardard, ppmvd
RA 1"09 -= relative accuracy, o/o
CO Summary
ttatEE)AI
Locrtion: MPC-Tesoro - Salt lake Ciw Refinerv. UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025-0362-003
Run
No.Drte Tlme Reference Method
CO Concentradon
ppmvd@0%o,
CEMS
CO Concentrrtion
oomvd tO 0 7n O,
Averrge
Dilference
oomvd tO 0 7n OrStart End
I
)
3
4
5
6
7
8
9
v20125
420t25
2t20t25
2t20t25
2t20t25
2t20t25
2120/25
2120t25
2120125
9:10
9:31
9:52
10:40
1 1:01
ll:22
l2:10
l2:31
l2:52
9:30
9:51
l0:12
t l:00
ll:21
ll.42
t2:30
l2:51
t 3:12
19.51
t9.79
17.17
t9.r7
28.76
28.19
17.83
15.65
15.52
t3.69
t5.00
12.47
t3.96
t3.56
t-2.84
t3.l I
t0.24
t0.15
5.82
4.79
4.70
5.21
5.20
5.35
4.72
5.4t
5.37
Av€rage 20.1 8 5.00 5.t'7
Standard Deviation (Sd 0.372
Applicable Source Standard (AS 500
Confi dence Coeffi cient (CC 0.286
Rehdve Accurrcy (RA)1.09 o/o
Performance Requircd - Applicable Source Standard RA<5%
Performance Specifi cation Methm PS 4A
Confldence Coeflicient CC
cc = lto'3t r sallVn I
where,
h.e?j 2.306 = degrees offreedom value
n 9 = number of runs selected for calculating the RA
Sd -0'32 = standard deviation of difference
CC 0.286 = confidence coefficietrt
Reletive Accurrcy, RA
ld l+ lcclRA : ;s;;TM xloo
where,d 5.17 : average differ€ncc of Reference Method and CEMS
CC 0286 = confidence coefficient
AS 500.000 = applicable source standard, ppmvd @ 0 % Oz
RA 1.09 = relative accuracy, 7o
pulaAIEE)
Lo.rdoo,
Soo""a,
ProJect No.: el:2Q?lPl62 lQ1
Conlldcnce Coeffrcient, CC
cc = lto'I'x sallVn I
where,
h.er
-\=
degrees of freedom value
n 9 = number of runs selected for calculating the RA
sa -6.-o r s- = standard deviation of difference
cc lllil = confidence coefficient
Relrdve Accurecy, RA
ld l+ lcclrul = r3;;7p:xloo
where,d -0.016 : averags difference of Reference Method and CEMS
cC -6-015-= confidence coefficient
RM -F= refcrence method,% dry
RA 0.71 _= relative accuracy, o/o
02 Summary
Run
No.Drte Tlme Reference Method
Or Conccntrrdon
o/c ilrr
CEMS
0z Concentrrdon
o/o ilrt
Avenge
Dilference
Yc ilwStrrtEnd
I
2
3
4
5
6
't
8
9
2120/25
2t20125
?/20t25
2120125
2t20t25
2t20t2s
2120125
2t20t25
2t20t25
9:10
9:31
9:52
l0:40
ll:01
ll:22
l2: l0
l2:31
l2:52
9:30
9:51
10:12
11:00
lL:.21
ll:42
12:30
12:51
L3:12
4.27
4.25
4.26
4.49
4.37
4.31
4.24
4.37
4.33
4.32
4.28
4.29
4.s0
4.36
4.32
4.26
4.38
4.34
-0.05
-0.03
-0.03
-0.01
0.01
0.01
-0.02
-0.01
-0.01
Averagt 4.32 4.34 -0.02
Standard Dwiation (Sd)0.019
Confi deirce Coeffi cieirt (CC)0.015
Reledve Accurrcy @A)0.71 e/o
Performance Rcquircd - Mean Refcrence Mcthod RA< 20%
Performance Soecification Method PS3
=TAAIIEE!' |-: ,) '
\IFR Summary
Locedon: MPC-Tesoro - Salt [ake Ciw Refinerv, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025-0362-003
Run
No.Dete Time Reference Method
f,'low Rrte
dscfm
CEMS
Flow Rrte
dscfm
Avcrege
Difference
dscfmStrrtEnd
1
.,
3
4
5
6
7
8
9
2/20/25
2120t25
2t20/25
2t20/25
2/20t2s
2t20/25
2t20/25
2t20t25
2/20/25
9:10
9:35
9:55
l0:40
t l:05
t l:25
12:10
l2:35
l2:55
9: l5
9:40
l0:00
10:45
1 1:10
1l:30
L2:15
l2:40
13:00
99,363
98,993
98,1 8 1
98,091
98,278
98,045
98,343
97,234
98 338
06,548
02,108
01,513
06,259
02,217
02,370
06,547
02,4t3
02.082
-7, I 8s
-3,1 l5
-3,332
-8,168
-3,939
4,325
-8,2M
-5,179
-3;744
Averagr 98,3 18 03.562 -5,243
Standard Dwiation (Sd)2,063
Confidence Coefficient (CC)I,586. r 26
Relaffve Accuracv (RA)6.95 o/o
Acceotabiliw Criteria - Mean Reference Method <2ff/o
Performance Specifi cation Method PS6
Confidence Coelficient CC
cc : ltngs x sdllVn I
where,
\.trt L= deglees of freedom value
n 9 = number of runs selected for calculating the RA
sdl,0-63/-I-=standarddeviationof diff erence
CC 1,586.13 = confidence coefficient
Relrtive Accuncy, RA
ld l+ lcclp-,l =
-r____x100
where,
d -5,243.31 = average diference of Reference Method and CEMS
CC 1,586.13 = confidence coefficient
RM 98,3 18.44 = reference method, dscfin
RA 6.95 = relative accuracy,%io
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Runl-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025-0362-003
Dstez 2120125
Time
Unit
Status
Uncorrected Run Averege (Cou.)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Z.ero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
9:10
9:l I
9:12
9:13
9:14
9:15
9:16
9:17
9:18
9:19
9:20
9:21
9:22
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
4.41
4.00
0.09
0.10
0.10
4.14
4.14
4.14
4.27
15.96
400.00
0.93
0.92
0.93
387.85
388.70
388.28
15.52
3.27
80.00
0.18
0.08
0.13
79.19
79.16
79.17
3. l9
1.61
1.0s
2.32
4.83
4.89
s.93
s.32
4.79
0.25
3.43
2.s9
2.68
2.99
2.07
l.9l
2.32
1.92
2.93
4.55
5.35
5.03
0.04
80.00
0.02
0.24
0.13
84.49
82.24
83.37
-0.09
4.26
4.19
4.32
4.48
4.41
4.49
4.43
4.42
4.tt
4.46
4.35
4.42
4.46
4.41
4.40
4.46
4.37
4.49
4.55
4.60
4.55
14.89
15.2
13.54
12.54
1 1.89
12.20
12.01
12.83
29.89
13.97
r4.81
15.93
17.42
18.33
18.85
18.80
19.09
t7.23
15.26
14.72
15.66
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.01
0.26
0.10
0.04
0.08
0.08
0.04
0.05
0.07
0.02
0.02
0.03
0.03
0.00
Run2-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: A5T-2025-0362-003
D*ez 2/20/25
Time
Unit
Stetus
Uncorrected Run Averege (Cou,)
Cal Ges Concentration (Cy,)
Pretest System Zero Response
Posttest System Zero Response
Averege Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
9:31
9:32
9:33
9:34
9:35
9:36
9:37
9:38
9:39
9:40
9:41
9:42
9:43
9:44
9:45
9:46
9:47
9:48
9:49
9:50
9:51
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
16.19
400.00
0.93
0.92
0.93
387.85
388.70
388.28
15.77
NOx - Outlet
ppmvd
Valid
2.s9
80.00
0.18
0.08
0.13
79.19
79.16
79.17
2.s0
4.9s
4.56
5.23
4.42
4.21
2.29
2.6s
1.94
1.78
1.94
1.80
1.62
1.77
1.67
Ls0
1.99
2.38
1.92
1.51
1.87
2.48
SOr - Outlet
ppmvd
Valid
4.39
4.00
0.09
0.10
0.10
4.14
4.14
0.03
80.00
0.02
0.24
0.13
84.49
82.87
83.68
-0.10
4.14
4.2s
4.s3
4.50
4.58
4.52
4.47
4.35
4.4s
4.35
4.34
4.35
4.30
4.32
4.35
4.31
4.30
4.37
4.41
4.35
4.32
4.35
4.38
14.14
14.87
t4.77
16.91
15.68
17.46
17.11
17.50
1 8.14
16.93
15.80
16.29
17.05
ts.42
16.68
16.s8
1s.66
15.72
16.91
15.79
14.65
0.0s
0.03
0.03
0.05
0.05
0.02
0.02
0.01
0.01
0.00
0.00
0.00
0.00
0.01
0.00
0.00
0.01
0.04
0.09
0.06
0.0s
FraAI Run3-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No. : AST-2025 -03 62-003
Date:2/20125
Time
Unit
Status
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
9:52
9:53
9:54
9:55
9:56
9:57
9:58
9:59
l0:00
l0:01
l0:02
l0:03
l0:04
l0:05
l0:06
l0:07
l0:08
l0:09
l0: l0
10:l I
l0: l2
Oz - Outlet
Y" dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
3.19
80.00
0.18
0.08
0.13
79.r9
79.16
79.17
3. l0
SOu - Outlet
ppmvd
Valid
4.40
4.00
0.09
0.10
0.10
4.t4
4.r4
4.14
4.26
14. l6
400.00
0.93
0.92
0.93
387.85
388.70
388.28
13.67
0.04
80.00
0.02
0.24
0.13
84.49
82.24
83.37
-0.08
4.41
4.42
4.40
4.33
4.29
4.36
4.35
4.31
4.31
4.34
4.34
4.37
4.40
4.42
4.47
4.s2
4.45
4.42
4.44
4.44
4.6s
13.35
14.s5
14.42
14.35
15.67
15.58
15.88
14.81
14.58
14.34
13.74
13.50
12.67
12.68
13.41
12.93
13.63
14.1 8
14.84
14.87
13.46
3.00
2.94
2.66
2,27
1.93
2.00
2.20
2.07
1.84
1.88
2.26
2.89
3.39
4.20
4.39
5.tl
4.32
3.40
3.28
3.16
7.21
0.08
0.04
0.06
0.04
0.03
0.05
0.07
0.04
0.02
0.03
0.02
0.02
0.05
0.06
0.05
0.06
0.03
0.05
0.04
0.06
0.02
=laAIlEe Run4-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025-0362-003
D*ez 2l2ol25
Time
Unit
Stetus
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
15.05
400.00
0.92
0.00
0.46
388.70
387.s2
388. I I
15.05
NOx - Outlet
ppmvd
Valid
3.27
80.00
0.08
0.10
0.09
79.16
79.t6
79.t6
3.22
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou,)
Cal Gas Concentration (CMA)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
l0:40
l0:41
l0:42
l0:43
l0:44
l0:45
l0:46
l0:47
l0:48
l0:49
l0:50
l0:51
l0:52
l0:53
l0:54
l0:55
l0:56
l0:57
l0:58
l0:59
I l:00
4.62
4.00
0. l0
0.09
0.10
4.14
4.1l
4.12
4.49
0.14
80.00
0.24
0.54
0.39
82.24
82.8',t
82.56
-o.25
4.57
4.38
4.38
4.s2
4.s8
4.51
4.51
4.44
4.50
4.6r
4.66
4.73
4.79
4.6s
4.70
4.68
4.74
4.77
4.77
4.73
4.',|4
tl.43
12.64
13.99
14.72
1s.20
t3;13
13.57
13.4s
12.88
14.2t
1 6.16
t6.24
t6.s4
16.07
16.08
16.06
16.30
15.68
t6.02
17.78
17.35
l.6l
l.0s
2.32
4.83
4.89
5.93
s.32
4.79
0.25
3.43
2.s9
2.68
2.99
2.07
l.9l
2.32
t.92
2.93
4.55
5.35
5.03
0.10
0.t2
0.05
0.06
0.09
0.1I
0.12
0.09
0.12
0.r2
o.t2
0.14
0.12
0.10
0.18
0.19
0.19
0.20
0.21
0.21
0.24
=TAAI!EE}Run5-RMData
Locatlon: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No. : AST-2025 -03 62-003
Dfiez 2120125
Time
Unit
Stetus
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
1.55
80.00
0.08
0.10
0.09
79.16
79.t6
79.16
1.47
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
I l:01
I l:02
I l:03
I l:04
I l:05
I l:06
I l:07
I l:08
I l:09
I l:10ll:ll
ll:12
1 l:13
1 1:14
I l:15
I l:16
l l:17
I l:18
l l:19
I l:20
ll:21
4.49
4.00
0.10
0.09
0.10
4.14
4.tt
4.r2
4.37
22.51
400.00
0.92
0.00
0.46
388.70
387.52
388.1 I
22.7s
0.34
80.00
0.24
0.54
0.39
82.24
82.8',1
82.s6
-0.05
0.24
0.26
0.28
0.30
0.28
0.27
0.31
0.32
0.36
0.38
0.39
0.37
0.36
0.42
0.40
0.4'1
0.47
0.46
0.33
0.26
0.30
4.61
4.52
4.51
4.50
4.54
4.48
4.46
4.46
4.50
4.38
4.36
4.45
4.33
4.41
4.s0
4.50
4.49
4.54
4.57
4.61
4.63
t9.24
20.63
19.74
21.42
21.80
21.87
20.86
19.4t
20,40
20.94
24.29
21.99
26.48
27.81
25.72
23.07
22.2't
21.36
24.85
23.52
2s.01
3.80
2.39
2.t7
1.82
1.87
1.58
1.38
1.78
1.86
1.27
0.82
t.t7
0.69
0.s8
0.94
1.09
t.t4
1.64
1.09
t.64
1.75
AI =TATEE Run6-RMData
Location: MPC-Tesoro - Salt Lake CiWRefinery, UT
Source: Wet Gas Scrubber - CEMS 2
Proj ect No.: AST-2025 -0362-003
D*e:2120125
Time
Unit
Stetus
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
t.29
80.00
0.08
0.10
0.09
79.16
79.16
79.16
1.22
SOr - Outlet
ppmvd
Valid
0.40
80.00
0.24
0.54
0.39
82.24
82.87
82.s6
0.01
0.28
0.30
0.32
0.31
0.38
0.38
0.34
0.39
0.36
0.42
0.45
0.41
0.45
0.44
0.44
0.44
0.44
0.44
0.49
0.51
0.49
4.46
4.00
0.l0
0.09
0.10
4.14
4.1I
4.12
4.33
22.12
400.00
0.92
0.00
0.46
388.70
387.52
388. l I
22.35
ll.,22
ll:23
ll:24
ll:25
ll.,26
ll:27
I l:28
ll:29
I l:30
I l:31
ll:32
I l:33
I l:34
I l:35
1 1:36
I l:37
I l:38
I l:39
I l:40
I l:41
ll:42
4.59
4.56
4.57
4.57
4.48
4.52
4.s6
4.50
4.25
4.20
4.33
4.33
4.38
4.42
4.48
4.54
4.41
4.40
4.s0
4.5s
4.sL
24.78
21.67
19.71
19.26
18.46
20.06
21.06
23.10
2',t.33
32.38
26.28
23.69
22.39
20.45
20.93
21.43
21.00
22.94
20.21
19.51
17.90
1.74
r.67
2.30
2.41
1.65
1.78
1.78
l.l6
0.55
0.28
0.35
0.4s
0.65
0.95
l.l8
1.32
1.06
0.72
1.42
1.76
1.95
AI
i,
Location: MPC-Tesoro - Salt Lake CiE Refinery, UT
RunT-RMData
Source: Wet Gas Scrubber - CEMS 2
Project No. : AST-2025 -03 62-003
D*et 2120125
Time
Unit
Status
0r - Outlet
Yo dry
Valid
CO - Outlet NOx - Outlet SOr - Outlet
ppmvd ppmvd ppmvd
Valid Valid Validt3;76 2.32 0.40Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cnr)
Corrected Run Average (Corr
12: l0
l2:ll
12:12
12:13
l2:14
l2:15
l2:16
12:17
l2: l8
l2:19
l2:20
l2:21
l2:22
l2:23
l2:24
l2:25
l2:26
l2:27
l2:28
l2:29
l2:30
4.39
4.00
4.t5
4.24
0.09
0.10
0.09
4.1I
4.18
400.00
0.00
0.00
0.00
38',t.s2
386.82
387.17
14.22
80.00
0.10
0.68
0.39
79.16
79.17
'79.t7
1.96
0.80
0.53
0.77
0.78
0.7s
r.24
1.89
3.2s
3.62
3.36
3.8s
4.45
3.75
2.58
3.47
3.50
2.76
3. l3
2.26
0.77
t.2t
80.00
0.54
0.00
0.27
82.87
82.20
82.54
0.12
4.28
4.2s
4.3s
4.35
4.3r
4.36
4.44
4.s6
4.s4
4.54
4.53
4.53
4.52
4.39
4.42
4.4s
4.37
4.38
4.29
4.14
4.29
t5.75
16.98
t6.69
17.06
16.97
15.61
14.54
13.86
12.06
12.15
12.51
12.3t
13.56
12.63
I 1.80
t2.14
I 1.68
t0.74
I1.50
14.39
14.08
0.48
0.52
0.46
0.50
0.48
0.s0
0.48
0.50
0.48
0.49
0.31
0.35
0.29
0.29
0.29
0.31
0.29
0.34
0.34
0.36
0.34
AI
Locetion: MPC-Tesoro - Salt Lake Citv Refinery, UT
RunS-RMData
Source: Wet Gas Scrubber - CEMS 2
Project No. : AST-2025 -03 62-003
Date:2120125
Time
Unit
Stetus
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet SOr - Outletppmvd ppmvd
Valid Valid
5.15 0.35Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run Averase (Co
4.52
4.00
0.09
0. l0
0.09
4.tt
4.18
4.15
4.37
400.00
0.00
0.00
0.00
387.s2
386.82
387.1?
12.37
80.00
0.10
0.68
0.39
79.t6
79.17
79.t7
4.84
2.20
3.71
5.01
s.84
5.98
s.88
2.93
3.8s
4.06
3.04
4.90
6.42
7.75
8.67
7.tt
6.28
8.33
6.36
4.99
3.46
1.45
80.00
0.s4
0.00
0.27
82.87
82.20
82.54
0.07
l2:31
l2:32
l2:33
l2:34
l2:35
l2:36
l2:37
l2:38
l2:39
l2:40
l2:41
l2:42
l2:43
l2:44
l2:45
l2:46
l2:47
l2:48
l2:49
12:50
l2:51
4.41
4.50
4.s7
4.59
4.57
4.54
4.36
4.4s
4.46
4.40
4.57
4.63
4.68
4.71
4.57
4.54
4.66
4.55
4.52
4.38
4.21
13.39
t2.9s
12.03
tl.44
I 1.55
I 1.43
l l.7l
12.21
I 1.63
13.22
13.00
t2.77
I l.s6
11.43
tt.2t
10.90
12.19
I 1.54
11.41
l1.61
12.38
0.39
0.33
0.30
0.27
0.38
0.36
0.3'7
0.33
0.38
0.37
0.35
0.40
0.39
0.3s
0.37
0.36
0.41
0.38
0.35
0.25
0.23
AI =larEE)Run9-RMData
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025-0362-003
D*ez 2l2ol25
Time
Unit
Status
Or - Outlet
oh dry
Valid
4.48
4.00
0.09
0.10
0.09
4.11
4.18
4.15
4.33
CO - Outlet
ppmvd
Valid
NOx - Outlet SOr - Outlet
ppmvd ppmvd
Valid Valid
4.t6 0.26Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cpi
Pretest System Zero Response
Posttest System Zero Response
Average Zcro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
400.00
0.00
0.00
0.00
387.52
386.82
387.t7
12.30
tt.92
I1.48
I 1.37
tl.l7
10.62
I l.l6
10.68
tt.47
10.62
I l.2l
I 1.33
r1.23
I1.78
I 1.30
t4.07
14.18
13.82
t2.89
12.51
12.36
t2.90
80.00
0.10
0.68
0.39
79.16
79.17
79.r7
4.44
1.94
3.54
4.92
6.21
10.41
9.4s
4.73
3.51
5.50
6.40
6.85
7.21
7.06
6.86
3.20
1.99
1.98
2.23
2.t9
2.33
l.4s
80.00
0.54
0.00
0.27
82.87
82.20
82.54
-0.01
l2:52
l2:53
l2:54
l2:55
l2:56
l2:57
12:58
l2:59
l3:00
13:01
l3:02
l3:03
l3:04
l3:05
l3:06
l3:07
13:08
l3:09
l3: l0
l3:l I
13:12
4.27
4.44
4.st
4.s9
4.75
4.73
4.43
4.38
4.s2
4.s7
4.s7
4.61
4.66
4.6t
4.43
4.33
4.31
4.34
4.34
4.3s
4.27
0.26
0.23
0.23
0.22
0.22
0.22
0.24
0.28
0.26
0.27
0.28
0.24
0.26
0.30
0.2s
0.23
0.29
0.31
0.2s
0.29
0.31
AI =IATEE);'
Method I Data
t -.".. Mrc
G,.. wdtuSErtu.CP-\IS2
Prold Nd AST-r0r5-Ct6240Jbt a2llrlts
Ilrd Ortsudd: Vdiot
ooaootgot-ffi
Dhue tor Fr W.lI 6 Ortddc dPofr 105.00 h
xtppt" L.n1O, ---id- Io
XLtO o(Drc 95.00 l!
Crd S..ddrl Aru oflru& 50.27 ft'N. of Ta Pm: -----l-
Nubs of Radltr F. raor, -----J-
Irhuc. A: 35.0 n
Dlrtlc. A Dod DLD@, -----ii- 1ou ur > o.gurq* a, -----i6i- r
ttbaG. B lrtd Diu@., ---li- (.oo b.: 2,
Mblou ftub.r dT-"uc Poloc, -----]7-
Am.l Ntib.t of Tnv* raou,
-i7--Mdu6 gdttrl ed D.L): :!84i_Rdlffi onhld rd D.e), _E1l2g_
Tnve
Pdnt
Y.d
Ir.Dd6
Mrh!c.ts
o.tid. olrill
I
2
3
1
5
6
1
t
I
l0
ll
3.2
10.5
19.4
12.3
61.7
80.6
t9.5
':.'
1.07
10.0t
It.62
31.01
51.v9
n3a
t5.92
e2:3
t2 vt6
t9 t/t6
27 5/t
,40
14
t5 3/8
94 15^6
tot l5/16
Nt b.,cJrffiplri.r.tfu&
I
2
3
1
5
6
1
t
t
l0
ll
t
62I1 7 I 9 t0 lt l2
4.1
14.6
29.6
10.1
85.4
'1u
14.6
t5.4
6.1
25.0
15.0
93.1
3.2
10.5
19.4
32,3
61.1
t0.6
t9.5,1'
2.6
t.2
14.6
22.5
31.2
65.8
11.1
t5.4
91.8
t_,
- 2.1
- 6.7
- ll.8
- 17.7
- 25.0
- 3s.6
- 61.1
- 75.0
- 62.3
- tt.2
- 93.3
- 9?9
.PMt of tbc| diM.ur Irod i$idc nll b tMtt. poirt.
Sftl Dirgm
A-3Jn.
B- 20fi.
Dath of D(d - 96 ir
Crcs Sdioul AB D@naLam
Dl*u]b.n.G
oaaoaooa
UFtraamOtu.b.n..
=l TAI Cyclonic Flow Check
Location MPC-Tesoro - Salt Lake Clty Refinery, UT
Source lYet Ges Scrubber - CEMS 2
Project No. A5T-2025-0362-003
D*e 2ll9l25
Sample Point Angle (AFO)
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4HI!a(),,
ct+,c{e6tEo-+ac)E2
=laAIlEe,n
Method 4 Dalta
Lddor
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Comh Ualtr / Mcttod
la No.
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lbB
ihra TIE
IDd Tlc
lu Tle, d! (0)
t
2n0/25
VALID
9:10
t0:tl
63
MB-706
2
2no/25
VALID
t0:40
t l:41
61ltrM
3
zr20/25
VALID
l2:10
l3:13
63
llffi Cor*tloo trr.-tor (Y)
Ho.C.nHolvdw (AE@)
l{uVewE,|!Ei
t.000
1.913
8
0m3
1.000
t.931
8oml
1.000
1.933
8
ller Volle lll
0
5
l0
l5
20
25
30
35
10
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v)
55
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63
389.691
!91.165
l9?.t40
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405.990
410.060
414.t35
4lt.2l0
422.245
426.360
430.431
434.505
,138.580
439.251
,139.843
413.920
{48.005
152.45
,156.155
6.21s
,ltl.3 t5
,t6t.,O0
412.485
416.555
,r80.640
4U.720
488.805
489.478
190.254
494.350
498.,145
s02.54
506.540
510.735
514.820
518.915
523.015
521.t20
531.2r5
535.300
539.395
540. I 07
lo t<1
l.q.rrluq
0
5
l0
l5
20
23
30
35
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63
lv6a8c Taopcraturg 'F
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M.ta
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16
37
31
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38
38
39
39
39
39
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491
35
Prob.FILd Vruu
8
I
t
8
8
8
8
8
8
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8
8
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8
8
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{n
12
44
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53
52
52
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40
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11
31
37
38
38
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39
39
39
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11
Probc trIft.r Vra[u
8
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IEp. Ent
44
45
41
49
50
5l
5l
55
55
5,1
52
50
48
47
50
14
Mctd
39
39
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40
40
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4l
42
42
43
43
41
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39
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t
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8
8
8
8
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Et
8
tEp. EIlt
45
45
44
11
40
38
31
31
3t
38
19
39
4t
42
40
71
Nroffilc Praurg lL Et
lld6 orlic. Pr4u. , lD wC
llG Prsorq lE Et
(Pb)
(AE)
(h)
25.55
1.900
25.69
25.55
1.900
25.69
2s.55
1.900
2s.69
Alrty'& TyF
IEplngq I, Prrr'Po.t Tdt, 8
In{dntq a hdP6r Tdg 8lqh86 3, Prc/Po.t T6g I14146l, Prc/Pdt Tag I
VdlD w.td Co[.ct.4 iL (vlc)
Saudrrd wrE voluE , d fvrrtat
MoLm Fil{oo Mcrur.d (BwS)
G! MoLcdr W4iq lr'D-Dl. (dty) (Md)
Orrvis*ic
H20
H20
Etqty
149.2
751.6
656.8
915.9
175.1
6r.2.6
t6r.7
24.t
5.8
H20
H20
Eqty
7U.8
715.1
662.6
925.7
801.7
65E.9
160.9
26.0
6.3
l1.9
H20
H20
Eqtv
75t.1
742.9
56E.9
92t.3
768.2
615.5
t6t.2
25.3
6,6
141
209. I
9.86r
0.179
30.07
1'
205.1
9.611
0.176
30.08
201.E
9.800
0.178
30.08
10
AI =TAIEE)QA Data
Locetion MPC-Tesoro - Salt Lake Citv Refinerv. UT
Source Wet Gas Scrubber - CEMS I
Project Xo.
Parameter Or - Outlet CO - Outlet NOx - Outlet SO, - Outlet
Make
Model
SN
Oneretinp Rense
CAI
700
1908030
25
Horiba
vtA-510
UGTUOOB
1000
CAI
700
1908030
150
Teledyme
TIOOH
428
150
Cylinder ID
Z.ero
Low
Mid
Hish
NA
NA
880069884
cc403781
NA
NA
cc721736
cc403781
NA
NA
EB00l 1606
E8009s259
NA
NA
cc13s228
cc403781
Cylinder Certilied Values
Txro
Low
Mid
Hish
NA
NA
23.99
8.000
NA
NA
s19
798. I
NA
NA
501
r62.4
NA
NA
482
159.5
Cylinder Expiration Date
7*ro
Low
Mid
Hish
NA
NA
4/t/32
t2129/28
NA
NA
2t9t27
12t29t28
NA
NA
9/r6t3r
U22132
NA
NA
3/4/32
12129/28
fvoe of Samole Line Heated Line
=TAAI Response Times
Tfi)illrl,
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
seconds
Paremeter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
7*ro
Low
Mid
Averese
60
NA
60
60
NA
60
t20
NA
120
180
NA
180
60.0 60.0 120.0 180.0
=raAI Calibration Data
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025 -03 62-003
Datez 2ll9l25
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Exoected Averase Concentration s.00 200.00 50.00 32.00
Span Between
Low
High
Desired Snan
s.00
2s.00
8.00
200.00
1000.00
798.10
50.00
2s0.00
162.40
32.00
r60.00
159.s0
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
3.20
4.80
3t9.24
478.86
64.96
97.44
63.80
95.70
High Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Actual Concentration (7o or ppm)
7*ro
Low
Mid
Hish
0.00
NA
4.00
8.00
0.00
NA
400.00
798. I 0
0.00
NA
80.00
162.40
0.00
NA
80.00
1s9.50
Response Time (seconds)60.00 50.00 120.00 r 80.00
Uoscale Calibretion Gas (C-^)Mid Mid Mid Mid
Instrument Response (% or ppm)
Z,ero
Low
Mid
Hish
0.00
NA
4.06
8.01
0.00
NA
392.08
798.8s
0.00
NA
79.60
162.5s
0.10
NA
82.00
162.s8
Performance (% of Span or Cal. Gas Conc.)
Znro
Low
Mid
Hiph
0.00
NA
0.75
0.12
0.00
NA
0.99
0.09
0.00
NA
0.25
0.09
0.06
NA
1.25
1.93
Linearity (% of Span or Cal. Gas Conc.)
Status
Zaro
Low
Mid
Hish
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
AI =tarEE)Bias/Drift Determinations
Location: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025 -0362-003
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.00
0.00
4.01
3.99
0.00
0.00
389.67
389.22
0.00
0.00
80.4s
79.97
0.20
0.18
81.37
82.02
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.00
0.00
4.01
3.99
0.00
0.00
389.67
389.22
0.00
0.00
80.4s
79.9',7
0.20
0.18
81.37
82.02
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.00
0.00
4.01
3.99
0.00
0.00
389.6',t
389.22
0.00
0.00
80.4s
79.97
0.20
0.18
81.37
82.02
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.00
0.00
3.99
3.99
0.00
0.00
389.22
389.24
0.00
0.00
79.97
78.68
0.l8
0.t7
82.02
81.68
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale ResDonse
0.00
0.00
3.99
3.99
0.00
0.00
389.22
389.24
0.00
0.00
79.97
78.68
0.18
0.t7
82.02
81.68
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.00
0.00
3.99
3.99
0.00
0.00
389.22
389.24
0.00
0.00
79.97
78.68
0. l8
0.17
82.02
81.68
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.00
0.00
3.99
3.99
0.00
0.00
389.24
388.00
0.00
0.00
78.68
78.60
0.17
0.17
81.68
82.2s
Run 8
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.00
0.00
3.99
3.99
0.00
0.00
389.24
388.00
0.00
0.00
78.68
78.60
0.t'7
0.17
81.68
82.2s
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.00
0.00
3.99
3.99
0.00
0.00
389.24
388.00
0.00
0.00
78.68
78.60
0.17
0.t7
81.68
82.25
*Bias checked every 3 runs
=IATEEAI
T i- il
Bias/Drift Determinations
Locedon:
Source:
Project No.:AST-2025-0362-003
MPC-Tesoro - Salt Lake City Refinery, UT
Wet Gas Scrubber - CEMS I
Prremeter 0r - Outlet CO - Outlet NOr - Outlet SO, - Outlet
Run 1 Dete 2ll9l25
Span Value
Initial Instument Zero Cal Response
Initial Instument Upscale Ca[ Response
Final InstrumenlZqo Cal Response
Final Inshrment Upscale Cal Response
Pretest System Zero Response
Posttest Systern Zero Response
Pretest System Upscale Response
Posftesf Svstem I Inscale Resnonse
8.00
0.00
4.06
0.00
4.06
0.00
0.00
4.01
3.99
798.10
0.00
392.08
0.00
392.08
0.00
0.00
389.67
389.22
t62.40
0.00
79.60
0.00
79.60
0.00
0.00
80.45
79.97
159.50
0.10
82.00
0.10
82.00
0.20
0.18
81.37
82.02
3ias (%)
lretest Z€ro
Posttest Zero
Pretest Span
Posttest Soan
0.00
0.00
-o.62
-0.87
0.00
0.00
-0.30
-0.36
0.00
0.00
0.52
0.23
0.06
0.05
-0.39
0.01
Drift(%)
Zero
Mid
0.00
-0.25
0.00
-0.05
0.00
-0.30
-0.01
0.41
Run 2 Dete 2llgns
Span Value
Instrument Zero Cal Response
Instument Upscale Cal Response
Final InstnrmentZero Cd Responsc
Final Instnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
8.00
0.00
4.06
0.00
4.06
0.00
0.00
4.01
3.99
798.1 0
0.00
392.08
0.00
392.08
0.00
0.00
389.67
389.22
162.40
0.00
79.60
0.00
79.60
0.00
0.00
80.45
79.97
159.s0
0.10
82.00
0.r0
82.00
0.20
0.18
81 .37
82.02
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.00
0.00
-0.62
-0.87
0.00
0.00
-0.30
-0.36
0.00
0.00
0.52
o.23
0.06
0.05
-0.39
0.01
Drift (%)
Zero
Mid
0.00
-0.25
0.00
-0.06
0.00
-0.30
-0.01
0.41
Run 3 Dete 2l9ns
Span Value
lnstrumetrt Zero Cal Response
lnstrumetrt Upscale Cal Response
Final lnstument Zero Cal Response
Final Instument Upscale Cal Response
Praest System Zero Response
Posttest Syst€m Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
E.00
0.00
4.06
0.00
4.06
0.00
0.00
4.01
3.99
798.10
0.00
392.08
0.00
392.08
0.00
0.00
389.57
389.22
162.40
0.00
79.60
0.00
79.60
0.00
0.00
80.45
79.97
159.50
0.10
82.00
0. l0
82.00
0.20
0.18
81.37
82.02
lias (%)
lretest Zero
losuest Zero
ketest Span
)osttest SDan
0.00
0.00
-0.62
-0.87
0.00
0.00
-0.30
-0.36
0.00
0.00
0.52
0.23
0.06
0.05
-0.39
0.01
)rift(%)
Zero
\i[id
0.00
-0.25
0.00
-0.06
0.00
-0.30
-0.01
0.41
=I TAI Bias/Drift Determinations
Locetion: MPC-Tesoro - Salt Lake Citv Refinerv. UT
Source: Wct Gas Scrubber - CEMS I
ProJect No.: AST-2025-0362-003
Prremeter 0r - Outlet CO - Outlet NOr - Outlet SO: - Outlet
Run 4 Dete 2l0ns
Spao Value
Instrument Zero Cal Response
Instnrment Upscale Cal Response
Final InshrmentZ,ero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Postlest Svstem I Inscale Resnonse
8.00
0.00
4.06
0.00
4.06
0.00
0.00
3.99
3.99
798.10
0.00
392.08
0.00
392.08
0.00
0.00
389.22
389.24
t62.40
0.00
79.60
0.00
79.60
0.00
0.00
79.97
78.68
159.50
0.10
82.00
0.10
82.00
0.l8
0.17
82.02
81.68
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.36
0.00
0.00
0.23
0.57
0.05
0.04
0.01
0.20
Drift (%)
Zero
Mid
0.00
0.00
0_00
0.00
0.00
4.79
-0.01
-0.21
Run 5 Dete 2ll9l25
Span Value
Instrument Zero Cal Response
Instnrment Upscale Cal Response
Final Instrument Zero Cal Response
Final Instnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstern Uoscale Resoonse
8.00
0.00
4.06
0.00
4.06
0.00
0.00
3.99
3.99
798.1 0
0.00
392.08
0.00
392.08
0.00
0.00
389.22
389.24
t62.40
0.00
79.60
0.00
79.60
0.00
0.00
79.97
78.68
159.50
0.10
82.00
0.10
82.00
0.18
0.17
82.02
81.58
Bias (%)
Pretest Zso
Posttest Zero
Pretest Span
Posttest Snan
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.36
0.00
0.00
0.23
0.57
0.05
0.04
0.01
0.20
Drift(%)
Zero
Mid
0.00
0.00
0.00
0.00
0.00
-o.79
-0.01
-0.21
Run 5 Dete Algns
Span Value
Instrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstumentZero Cal Response
Final Instrumerxt Upscale Cal Response
Prete.st System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
8.00
0.00
4.06
0.00
4.06
0.00
0.00
3.99
3.99
798.10
0.00
392.08
0.00
392.08
0.00
0.00
389.22
389.24
t62.40
0.00
79.60
0.00
79.60
0.00
0.00
79.97
78.68
159.50
0.10
82.00
0.10
82.00
0.18
0.17
82.02
81.68
Bias (%)
Pretest Z€ro
Posttest Zero
PrAest Span
Posttest SDan
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.36
0.00
0.00
0.23
0.57
0.05
0.04
0.01
0.20
Drift(%)
Zqo
Mid
0.00
0.00
0.00
0.00
0.00
-0.79
-0.01
-0.21
pJ/l6rrpEr
i - . l1 ^. l \l
Bias/Drift Determinations
Locrdon: MPC-Tesoro - Salt Lake City Refurery, UT
Source: Wet Gas Scrubber - CEMS I
Project No.: AST-2025-0362-003
Perrmeter O, - Outlel CO - Outlet NOr - Outlet SOr - Outlet
Run 7 Drte 2lDn5
Span Value
Instrumetrt Zero Cal Response
Instument Upscale Cal Response
Final Instrument Zerc Cal Response
Final lnstnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Syst€m Upscde Response
8.00
0.00
4.06
0.00
4.06
0.00
0.00
3.99
3.99
798. I 0
0.00
392.08
0.00
392.08
0.00
0.00
389.24
388.00
t62.40
0.00
79.60
0.00
79.60
0.00
0.00
78.68
78.60
159.50
0.10
82.00
0. l0
82.00
0.17
0.17
81.68
82.25
Bias (%)
Pretest Zero
Posttest Zero
Pret€st Span
Posttest Soan
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.51
0.00
0.00
0.57
0.62
0.04
0.04
0.20
0.16
Drift(%)
Zero
Mid
0.00
0.00
0.00
-0.r6
0.00
-0.05
0.00
0.36
Run 8 Date 2ll9l2s
lpan Value
hstnrment Zero Cal Response
hstrument Upscale Cal Response
jinal Instument Zero Cal Response
linal Instnrment Upscale Cal Response
lraest System Zero Response
losttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
8.00
0.00
4.06
0.00
4.05
0.00
0.00
3.99
3.99
798_10
0.00
392.08
0.00
392.08
0.00
0.00
389.24
388.00
162.40
0.00
79.60
0.00
79.60
0.00
0.00
78.68
78.60
159.50
0.10
82.00
0.10
82.00
0.17
0.17
81.68
82.25
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Snen
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.51
0.00
0.00
0.57
0.62
0.04
0.04
0.20
0.16
Drift (%)
Zero
Mid
0.00
0.00
0.00
-0.16
0.00
-0.05
0.00
0.35
Run 9 Date 2l|9n5
Span Value
lnstrument Zero Cal Response
Instunrent Upscale Cal Response
Final lnstnrmenlZero Cal Response
Final lnstrument Upscale Ca[ Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale ResDonse
8.00
0.00
4.06
0.00
4.05
0.00
0.00
3.99
3.99
798.1 0
0.00
392.08
0.00
392.08
0.00
0.00
389.24
388.00
162.40
0.00
79.60
0.00
79.60
0.00
0.00
78.68
78.50
159.50
0.10
82.00
0.10
82.00
o.l7
0.17
81.68
82.25
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.00
0.00
0.87
0.87
0.00
0.00
0.36
0.51
0.00
0.00
0.57
0.62
0.04
0.M
0.20
0.16
Drift(%)
Zqo
Mid
0.00
0.00
0.00
-0.16
0.00
-0.05
0.00
0.36
pd/l6rrrcE)
- :' ,, \. , '. i . a. i 1 a.
QA Data
Locetion MPC-Tesoro - Salt Lake City Refinery, UT
Sou"au
Project No. AST-2025-0362-003
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Make
Model
s/N
Onerrtins Rense
CAI
700
1908030
25
Horiba
vLA-sl0
UGTUOOB
1000
CAI
700
1908030
ls0
Teledlme
TIOOH
428
ls0
Cylinder ID
7*ro
Low
Mid
Hish
NA
NA
EB0069884
cc403781
NA
NA
cc12t736
cc403781
NA
NA
EB00l 1606
EB009s2s9
NA
NA
cc13s228
cc40378r
Cylinder Certilied Values
7*ro
Low
Mid
Hish
NA
NA
23.99
8.000
NA
NA
s19
798. I
NA
NA
501
162.4
NA
NA
482
159.s
Cylinder Expiration Date
7*ro
Low
Mid
Hish
NA
NA
4/U32
12129128
NA
NA
2t9t27
12129/28
NA
NA
9n613t
U22/32
NA
NA
314132
12t29/28
fvoe of Samole Line Heated Sample Line
=raAIIEE)
Li i' ::
Response Times
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST-2025 -03 62-003
seconds
Parameter Or - Outlet CO - Outlet NOx - Outlet SO" - Outlet
7*ro
Low
Mid
Hish
60
NA
60
60
NA
60
120
NA
120
180
NA
,-t-o
Averase 60.0 60.0 120.0 180.0
puIATEE)
t.
Calibration Data
f-i r-l
MPC-Tesoro - Salt Lake City Refinery, UTLocetion:
Source:
Project No.:
Wet Gas Scrubber - CEMS 2
AST-2025-0362-003
Date:2120/25
Paremeter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Exoected Average Concentration s.00 200.00 50.00 32.00
Span Between
Low
High
Desired Soan
s.00
25.00
8.00
200.00
1000.00
798. I 0
s0.00
250.00
162.40
32.00
160.00
159.50
Low Renge Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Mid Renge Gas
Low
Hish
3.20
4.80
319.24
478.86
64.96
97.M
63.80
9s.70
High Range Ges
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Actual Concentration (Yo or ppm)
Tnro
Low
Mid
Hiph
0.00
NA
4.00
8.00
0.00
NA
400.00
798.10
0.00
NA
80.00
r62.40
0.00
NA
80.00
ls9.s0
Response Time (seconds)60.00 60.00 120.00 180.00
Upscale Calibration Ges (CMr)Mid Mid Mid Mid
lnstrument Response (% or ppm)
7*ro
Low
Mid
Hioh
0.00
NA
4.10
8.01
0.00
NA
391.54
797.',70
0.00
NA
79.77
162.6s
0.27
NA
82.02
158.06
Performance (% of Span or Cal. Gas Conc.)
7*ro
Low
Mid
Hish
0.00
NA
1.22
0.12
0.00
NA
1.06
0.05
0.00
NA
0.14
0.15
0.t7
NA
1.27
0.90
Stetus
7*ro
Low
Mid
Hish
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
=raAI Bias/Drift Determinations
t-a ',i:lEe
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: 4$2Q2!:Q!!?:QQ1
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
0.09
0.10
4.14
4.14
0.93
0.92
387.85
388.70
0.18
0.08
79.19
79.t6
o.02
0.24
84.49
82.24
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.09
0.10
4.14
4.14
0.93
0.92
387.85
388.70
0.18
0.08
'79.19
79.16
0.02
0.24
84.49
82.87
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.09
0.10
4.14
4.t4
0.93
0.92
387.85
388.70
0.18
0.08
79.19
79.16
0.02
0.24
84.49
82.24
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.10
0.09
4.t4
4.1 I
0.92
0.00
388.70
387.52
0.08
0.10
79.16
79.16
o.24
0.s4
82.24
82.87
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale ResDonse
0.10
0.09
4.14
4.tt
0.92
0.00
388.70
387.52
0.08
0.10
79.16
79.16
0.24
0.54
82.24
82.87
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0. l0
0.09
4.14
4.rt
0.92
0.00
388.70
387.52
0.08
0.10
79.16
79.t6
0.24
0.54
82.24
82.87
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.09
0.10
4.1I
4.18
0.00
0.00
387.s2
386.82
0. l0
0.68
79.16
79.t',t
0.54
0.00
82.87
82.20
Run 8
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.09
0. l0
4.1I
4.18
0.00
0.00
387.52
386.82
0.10
0.68
79.t6
79.17
0.s4
0.00
82.87
82.20
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.09
0.10
4.1I
4.18
0.00
0.00
387.s2
386.82
0.10
0.68
79.t6
79.t7
0.54
0.00
82.87
82.20
=laAI Bias/Drift DeterminationsIEE)
t.
Locedon: MPC-Tesoro - Salt Lake Ciw Refincrv. UT
Source: Wet Gas Scrubber - CEMS 2
Project No.: AST2Q2! Q162 !Q!
Peremeter O, - Outlct CO - Outlet NOr - Outlet SOr - Outlet
Run 1 Dete 2l20ns
Span Value
Initial lnstument Zero Cal Response
Initial Instnrment Upscale Cal Response
Final Instnrment Zero Cal Response
Final lnstnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
8.00
0.00
4.10
0.00
4.10
0.09
0. l0
4.14
4.t4
798.10
0.00
391.54
0.00
391.54
0.93
0.92
387.85
388.70
t62.40
0.00
79.77
0.00
79.77
0.18
0.08
79.t9
79.16
159.50
0.27
82.02
0.27
82.02
0.02
0.24
84.49
82.24
Bias (%)
Pretest Zero
Posttest Zero
Fretest Span
Posttest Span
l.l9
r.24
0.55
0.48
0.t2
0.12
-0.46
-0.36
0.11
0.M
-0.36
-0.37
-0.16
-0.02
1.55
0. l4
Drift(%)
Zerc
Mid
0.06
-0.07
0.00
0.1 I
-0.05
-0.01
0.14
-1.41
Run 2 Dete 2l20ns
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final Instrument Zerc Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Pnsftest Svsfm I Jnscele Resmnse
8.00
0.00
4.10
0.00
4.10
0.09
0. l0
4.t4
4.t4
798.10
0.00
39t.54
0.00
391.54
0.93
0.92
387.85
388.70
t62.40
0.00
79.77
0.00
79.77
0.18
0.08
79.19
79.16
159.50
0.27
82.02
0.27
82.02
0.02
0.24
84.49
82.87
Bias (%)
Pretest Zef,o
Posttest Zero
Pretest Span
Posttest Soan
1.19
t.24
0.55
0.48
0.12
0. l2
-0.46
-0.36
0.r I
0.04
-0.36
-0.37
-0.16
-0.02
1.55
0.54
Drift(%)
Zero
Mid
0.05
-0.07
0.00
0.1 1
-0.06
-0.01
0. t4
-1.02
Run 3 Dete 2l20ns
Span Value
Instnrment Zero Cal Response
Instnrment Upscale Cal Response
Final lnstument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
8.00
0.00
4.10
0.00
4.10
0.09
0. l0
4.t4
4.t4
798. 1 0
0.00
391.54
0.00
391.54
0.93
0.92
387.85
388.70
162.40
0.00
79.77
0.00
79.77
0. t8
0.08
79.19
79.16
159.50
0.27
82.02
0.27
82.02
0.02
0.24
84.49
82.24
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
1.19
1.24
0.55
0.48
0.12
0.t2
-0.46
-0.36
0.1l
0.04
-0.36
-0.37
-0. l6
-0.02
1.55
0. 14
Drift(%)
Zero
Mid
0.06
-0.07
0.00
0.1 I
-0.06
-0.01
0. l4
-1.41
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Wet Gas Scrubbet - CEMS 2
Project No.: A5T-2025-0362-003
Peremeter Or - Outlet CO - Outlet NOr - Outlet SO, - Outlet
Run 4 Dete A20ns
Span Value
lnstrum€nt Zero Cal Response
lnstument Upscale Cal Response
Final Instrument Zero Ca[ Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest Systan Zero Response
Pretest System Upscale Response
Posttest Svstern Uoscale Resoonse
8.00
0.00
4.10
0.00
4. t0
0.10
0.09
4.14
4.tl
798.10
0.00
391.54
0.00
391.54
0.92
0.00
388.70
387.52
t62.40
0.00
79.77
0.00
79.77
0.08
0.10
79.16
79.16
1s9.50
0.27
82.02
0.27
82.02
0.24
0.54
82.24
82.87
Bias (%)
Pretest Zero
Posttest Zero
Pretest Spatr
Posttest Soan
t.24
1.18
0.48
0.17
0.12
0.00
0.36
0.50
0.04
0.06
0.31
0.38
0.02
0. l7
0.14
0.54
Drift(%)
Zero
Mid
-0.07
-0.31
-0.12
-0.15
0.02
0.00
0.19
0.39
Run 5 Date A20ns
Span Value
lnstrument Z€ro Cal Response
Instnrmeat Upscale Cal Response
Final lnstrumentZero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstefi llnscale Resnonse
8.00
0.00
4.10
0.00
4.10
0.10
0.09
4.14
4.11
798.1 0
0.00
391.54
0.00
391.s4
0.92
0.00
388.70
387.52
t62.40
0.00
79.77
0.00
79.77
0.08
0. l0
79.t6
79_t6
159.50
0.27
82.02
0.27
82.O2
0.24
0.54
82.24
82.87
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Postkst Span
t.24
l.l8
0.48
0.17
0.12
0.00
0.36
0.50
0.04
0.06
0.37
0.38
0.02
0.t7
0.14
0.54
Drift(%)
Zerc
Mid
-0.07
-0.31
-0.t2
-0.15
0.02
0.00
0.19
0.39
Run 5 Dete 2l20ns
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final Instument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest Systexn Upscale Response
Posttest Svstem UDscale Resoonse
8.00
0.00
4.10
0.00
4. l0
0.10
0.09
4.14
4.1 I
798.10
0.00
391.s4
0.00
391.54
0.92
0.00
388.70
387.52
t62.40
0.00
79.77
0.00
79.77
0.08
0.10
79.16
79.16
159.50
0.27
82.02
0.27
82.02
0.24
0.54
82.24
82.87
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
1.24
1.18
0.48
0.t7
0.12
0.00
0.36
0.50
0.04
0.06
0.37
0.38
0.02
0.17
0.14
0.54
Drift(%)
Zero
Mid
-0.07
-0.31
-0.12
-0.15
0.02
0.00
0.19
0.39
Bias/Drift DeterminationspllIATEE)
Locedon: MPC-Tesoro - Salt Lake Ciw Refurery. UT
Source: W€t Gas Scrubber - CEMS 2
Project No.: A5T-2025-0352-003
Prrrmetcr O: - Outlct CO - Outlet NOr - Outlet SOu - Outlet
Run 7 Dete 2l20ns
Span Value
lnstnrment Zero Cal Response
lnstument Upscale Cal Rcsponse
Final Instnrment Zero Cal Responsc
Final Instnrment Upscale Cal Response
Pracst System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Rcsponse
8.00
0.00
4.t0
0.00
4.10
0.09
0.10
4.t I
4.18
798.10
0.00
391.54
0.00
391.54
0.00
0.00
387.52
386.82
t62.40
0.00
79.77
0.00
79.77
0.10
0.68
79.r6
79.17
159.50
0.27
82.02
0.27
82.02
0.54
0.00
82.87
82.20
Bias (%)
Praest Zero
Posttest Zero
Pretest Span
Posttest SDan
1.18
l. l9
0.17
1.07
0.00
0.00
0.50
0.59
0.06
0.41
0.38
0.37
0.17
0.t7
0.54
0.12
Drift(%)
Zero
Mid
0.01
0.90
0.00
-0.09
0.36
0.01
-0.34
-0.42
Run E Date 2l20ns
Span Value
Instnrment Zero Cal Response
Instrument Upscale Cal Response
Final Instrument Zerc Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
8.00
0.00
4.10
0.00
4.10
0.09
0. l0
4.l l
4.18
798.10
0.00
391.54
0.00
391.54
0.00
0.00
387.s2
386.82
162.40
0.00
79.77
0.00
79.77
0. r0
0.68
79.t6
79.17
I 59.50
0.27
82.02
0.27
82.02
0.54
0.00
82.81
82.20
Bias (%)
Pretest Z€ro
Posttest Zero
Praest Span
Postrcst Span
l.l8
l. l9
0.t7
1.07
0.00
0.00
0.50
0.59
0.06
0.41
0.38
0.37
o.t7
0.17
0.54
0.12
Drift(%)
Zero
Mid
0.01
0.90
0.00
-0.09
0.36
0.01
-0.34
-0.42
Run 9 Dete 2120n5
Span Value
Instrument Zero Cal Response
Instnrment Upscale Cal Response
Final lnstrumentZero Cal Response
Final lnstnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Pn<tfcst Svsfm I Insclle Ilesmnse
8.00
0.00
4.10
0.00
4.10
0.09
0.10
4.1 I
4.18
798.10
0.00
391.54
0.00
391.54
0.00
0.00
387.52
385.82
162.40
0.00
79.77
0.00
79.77
0.10
0.68
79.t6
79.17
159.50
0.27
82.02
0.27
82.02
0.54
0.00
82.87
82.20
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Pnstlest Snan
l.l8
l.l9
0.17
1.07
0.00
0.00
0.50
0.59
0.06
0.41
0.38
0.37
0.17
0.17
0.54
0.t2
Drift (%)
Zero
\,Iid
0.01
0.90
0.00
-0.09
0.36
0.01
-0.34
-0.42
Airgas
an Air Liquide company
Airgas SpecidtyGases
Airgas USA LLC
525 Nor0r Inilustrial Loop Road
Tooele, W 84074
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certilication Date:
153401989376-1
145.1 CF
2015 PSIG
660
Dec29,2020
Expiration Date: Dec 29. 2028
CERTIFICATE OF AI{ALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
E04Nr91E15A0025
cc403781
124 -Tooele (SAP)- UT
872020
co,02,s02,BALN
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
6OO/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction foranalytical 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 otheMise noted. The results relate only to the items tested. The reporl shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below 100 psiq, i.e. 0.7
ANALYTICAL RESULTS
Actual Protocol Tota! Relative
SULFUR D|OX|DE 160.0 PPM 159.5 PPM Gl +l- 1.0o/o NIST Traceable 1212212020, 1212912020
CARBON MONOXIDE 8OO.O PPM 798.1 PPM Gl +l- 0.9% NIST Traceable 1212212020
oxycEN 8.000 % 8.000 % Gl +l- 0.6% NIST Traceable 1212312A20
NITROGEN Balance
CALIBRATION STANDARDS
Lot lD Cylinder No Concentration UncertalnQl
NTRM
NTRM
NTRM
't6010210
1 5060547
1 I 06071 7
KA1003217
cg53s71
cc338451
O.8Yo
O.60/o
0.4%
Dec23,2O2'l
Jan 08,2021
97.69 PPM SULFUR DIOXIDE/NITROGEN
491.9 PPM CARBON MONOXIDE/NITROGEN
4.861 o/o OXYGEN/NITROGEN
ANIALYTICAL EQI.IIPMENT
Nov 24, 2020
Dec01,2020
Dec 16,2020
Nicolet 6700 AHR0801550 CO MCO
Horiba MPA-510 W603MM58 02
Nicolet 6700 AHR0801550 SO2 MSO2
FTIR
02 Paramagnetic (Mason)
FTIR
L
Triad Data Available Upon Request
Sionatrrra on file
Approved for Release Page 't of I
PJL/tffi-Ea
Accreditation #62754
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 71107
800-55r -81 50
PGVP Vendor lO # G12024
EPA PROTOGOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
E80069884
127907
,I9OO PSIG
E80069884.20240320-0
Certification Date:
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certification Dates:
04to3t2024
04t01t2032
E80069E84.20240320
08421271',1
his per the May 2012 EPA Traceability Protocol, Oocument EPA-600/R-121531 ,
G2
-t
Concentration Unceftalnty Analytlcal Principlo Assayed On
!O.1 o/o
10.06 %
cc520205.202301 08
EBOO22009 20201022
20 01 vo
24 76 0/o
Ana lytical lnstrumentation
02
co2
MPA
FTIR
Themo
MKS
410i
MKS 2031 DJG2EKVSl 3T
I 162980025 03l1AnO24
017146467 Un2nO24
SMART-CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
ryQtu,-.
Brittany Johnson
Analytlcal Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revised on 2018-09-17
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, A 71107
800-551 -81 50
PGVP Vendor lD # G'|2019
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
)c721736
124234
1900 PS|G
)c721736.20190207-0
Certification Date:
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certification Dates :
)2t11t2019
)2t0912027
-shrevenod-lA
'JCt2'1736.2019020t
198493836
has been per Protocol. Oocument EPA-600/R-12/531
G1
-t
Concentrauon Uncertalnty Analytlcal Prlnciple Assayed On
E80014759 E80014759 20180't02 ',t',119n026 Gt rS N2
MKS MKS 2031DJG2EKVS13T 017146467 02n7D019
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the deflned specirications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a companson of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMrse noted. This calibration certiflcate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
ry/'-
Anthony Cyr
Assistant Operations Manager
Assay Laboratory: Red Ball TGS
Versron 02-J. Revrs€d on 2018-09-17
Aitgas
an Air Liquide company
Airgac SpecidtyGases
Airgas USALLC
525 North Industrial toop Road
Tooele, Vl 84o74
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
153-402939526-1
144.0 CF
201s PS|G
660
Jan22,2024
Expiration Date: Jan22,2032
CERTIFICATE OF AIYALYSIS
Grade of Product: EPA PROTOCOL STAI\IDARI)
E02Nt99E15A1183
E80095259
124 - Tooele (SAP) - UT
872024
NO,NOX,BALN
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certificatlon of Gaseous Calibration Standards (May 2012)" document EPA
600/R-1 2/531 , using the assay procedures listed. Analytical Methodology does not require conection for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no signiflcant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otheMise 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 below 100 psig, i.e. 0.7 megapascals
ANALYTICAL REST.JLTS
Actual Protocol Total Relative
Concentration Method Uncertalnty
Component Requested
Concentration
Assay
Dates
NOX
NITRIC OXIDE
NITROGEN
160.0 PPM
160.0 PPM
Balance
+l- 0.5o/o NIST Traceable
+l- 0.5o/o NIST Traceable
o 1 I 1 5 12024, 01 t22t2024
0 1 I 1 5t 2024, 01 t22t2024
162.4 PPM
't62.4 PPM
G1
G1
CALIB RATION STAIYDARDS
Type Lot !D Cyllnder No Concentratlon Uncertaintyr Expiration Date
O.4o/o
o.3Yo
0.4%
1.5o/o
1.60/o
Apr 25, 2031
Feb28,2025
Apr 25, 2031
Feb 17,2023
Jun 15,2025
GM|S 2023042513PRM 12414GM|S 202304252',1PRM '.12409
GMIS 153/,012021103
CC7il287 98.47 PPM NITRIC OXIDE/NITROGEN
APE,I514048 lOO.,I9PPMNITRICOXIDE/NITROGENCC7g372 98.40 PPM NITRIC OXIDE/NITROGEN
,I5.O,I PPM NITROGEN DIOXIDE/AIR
4.956 PPM NITROGEN DIOXIDE/NITROGEN
D913660
ND73012
The SRM, NTRM, PRM, or RGM noted abov6 is only in roforenc€ to the GMIS used in the assay and not part of tho analysis.
lnstrumenUMake/Model
ANALYTI CAL E QI.IIPMENT
Analytical Prlnclple Last Multipolnt Callbratlon
Nicolet iS50 AUP2010228 NO LNO
Nicolet iS50 4UP2010228 NO2 impurity
FTIR
FTIR NO2 impurity
Jan 17,2O24
Jan 18,2O24
Triad Data Available Upon Request
Sionatura on file
Approved for Release Page 1 of I
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 71107
80o-sst -8't 50
PGVP Vendor lO # G12023
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lO Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
:B001 '1506
124235
r900 PS|G
-8001 1 606.20230906-0
Certiflcation Date:
Expiration Oate:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certifi cation Dates :
)9t18t2023
)9t16t2031
-shrevenori-lA
=8001 1606.20230906
125274839
This calibration standard has been certified per the May 2012 EPA-600/R-1 2/531 ,
G1
, Oo Not Use This Cvlinder Below 100 osiq (0.7 Meqapascal). I
Certified Concentration(s)
Concentratlon Uncertalnty Analytlcal Prlnclple A3sayed On
501 PPM t3 PPM Chemiluminescence O9n1no23,o9n9n023
otal Oxides of Nitrogen 503 PPM
Balance
Analytical Measurement Data Available Online.
41-M-50
E80059947 202301 17
sx32691 202301 1 7
996 7 PPM
280 PPM
279 8 PPM
1 152610017 0A29DO23
SMART-CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined speciflcations. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternalional System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approxamate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
,furrtt lhrrhL
Aaron Varelas
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revised on 2018-09-17
&
--t3!s-.Accreditation #62754
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, A 71107
800-551 -81 50
PGVP Vendor lO # G12024
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lo Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
4c735224
123897
1900 PsrG
Certification Date:
Expiration Oate:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certlfication Dates:
)3to6t2024
)3t04t2032
- Shreveport - LA
JC t35224.20240221
I 01 360650
This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-1 2/531 ,
G1.
-t
Concentratlon Uncortalnty Analydcal Prlnclple Assayod On
1920 PPM
514 PPM
vtA-510 so2
vtA-510 so2
SMART-CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined speciflcations. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
,/arrt* thrrhu
Aaron Varelas
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J. Revised on 201 8-09-1 7
pul6rrEE)
Location: MPC-Tesoro - Salt Lake City Refinery, UT
NOx Converter Check
Project No.: AST-2025-0362-001
NO2 Converter Check - Outlet
Analyzer Make Thermo
Analyzer Model 42iQ
Serial Number 12327730521
Cylinder ID Number CC77O7T
Cylinder Exp. Date 4116127
Cvlinder Concentration. DDm 49.7
Pre-Test Dete 2ll7l25 Time 13:32
Pre-Test CooceotEI6i-, ppm 46^01
Pre-Test Efficiency. 7o 93
Post-Test Date 2ll7l25 Time 17:38
Post-Test coo."oE-tioo, pp- 46"08
Post-Test Efficiencv. o/o 93
is >90 %.
PJLTffi-Ea
Accreditation ,16275.4
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 7't107
800-551 -81 50
PGVP Vendor lD # G12O24
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
2C770777
174 t31
1E5O PSIG
4c770777 .20240212-O
Certification Date:
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certification Dates:
)4t16t2024
)4t1612027
=c770777 .20240212
108893227
has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-1 2/531 ,
ino orocedure G2
-t
Certified Concentration(s)
Dioxide
Concentratlon Uncertalnty An.lyflcal Prlnclple
4A
Asmyed On
o2t16no2434fi6n}%
Balance
Analytical Measurement Data Available Online
Reference Standard(s)
29 22 PPM
94.5 PPM
63 3 PPM
c2190301 02
c2190301 02
c2 1 90301.02
MKS 2031DJG2EKVS13T
MKS 2O31GPPPlAsZK1XX
SMART-CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparason of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the unceriainty of calibrations are available upon request and were taken into account
when determining pass or fail.
n-M.*u
_-4Z^
Timothy Davis
Analytical Chemist
Assay Laboratory: Red Ball TGS
Version 02-J. Revised on 2018-09-17
M205 QA Data
Vlcthod Crltcdr EPA
PrroGtcr o-
MUI
Modcl
vN
Shrh
sflomcx
4900
1002692to
llrdcr Numblr ID
Zcto
Mld
ElaI
NA
RRO253E
FEnnrotta
lltrdcr Ccrtflcd vrlu6
ufo
t\dtd
Eloh
U.U
l 1.00
23.99
ritrumatrt Rmonlc l'l. ol DDml'Izto
Mldqlrh
0.00
I 1.02
7A nn
G{ S.lc.tlon {./. a
Mtd
Hteh 96.0
tzto
Mtd
Eloh
U.U
0.1
0.0
v (7. of Ruqc)
0.1
Analyza Ma}c:
AnelfzrModcl:
AnalYza SN:
Environics ID:
Componmt/Balmcc Ou:
Cylinda Gu ID @ilution):
Cylinda Gr Concentratiotr (Dilution), ppm:
Cylinder Gs ID (Mid-kvcl):
Cylindo Gr Concmtmtion (Mid-L:vcl), ppm:
8029
Anrlfrcr
Conccntrrdon
Inlccfor I
Error
( !2./.1
InJccdon 2
Error
I *2./.r
Injecflon 3
Error
I * 7.Ar
19.31 O-2o/o "0.t%-O.l%o
t2.o't o.20/"-o.t%4.t%
4 0-4 -O.4o/o o.0%
7 -0.O.lo/a 0.4o/o
Mld-Lcvcl SuDDlv G$ Cdlbredon Dlret to
CillbrrlloD
Grs
Conccrtrrdotr
IDledoD I
Anrllzr
CoDccntndon
hj.cdor 2
Alrlyzc
ConcGtrtndon
lnlEuon J
Atrrlyzrr
ConcGntnflon
Avcngc
Anlyzcr
Cotrccntndon Dlllcrencc
Avcngc
Error
( !2./.1
I t.00 lo 99 IO.99 l0_99 -0.01 4.tvo
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 71'107
800-551 -81 50
PGVP Vendor lD # G12023
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
tR02538
12537'l
'1900 PstG
1R02538.20230831 -0
Certification Date;
Expiration Date:
MFG Facility:
Lot Number:
Tracking Number:
Previous Certifi cation Dates
)9t21t2023
0911912031
RR02538.2023083'l
103925725
This calabration standard has been certtfied per the May 201 .'t2t53'.t,
G1,
Concantratlon Unce(alnty Analytlcal Prlnclple Arsayed On
10.9 %
11.O0 olo
cc737012
EB,0022021
cc737012.20230228
880022021.20140323
1 162980025 09t18t2023
017146{67 09D1DO23
SMART-CERT
This is to certity the gases referenced have been calibrated/tested, and verified to meet the defined specrfications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specifled or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confldence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determaning pass or fail.
WA"rh
Jasmine Godfrey
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J. Revised on 2018-09-'17
Alr6tre
SOURCE TESTING
Mass Flow Controller Calibration
Note: The mass flow controller's calibration values are used by the dilution system's operating software to improve accuracy. These calibrations are not
necessarily indicative of the systems overall performance. Performance is verified by conducting a Method 205 prior to each field use.
Calibration Performed By JFT
Dllutlon System Make:
Dllutlon System Model:
Dllutlon System S/l{:
Callbratlon EqulpmGnt Make:
Callbratlon Equlpment Model:
Callbratlon Equlpment 5/N:
Flow Cell S/il:
Flow Cell S/N:
Callbratlon Gas:
Earometrlc Pressure, mmHg:
Amblent femperature,'F:
t Scientific
-10sLPD/5M M-D/sM, M-15LPM-D/5
272t2L
72L20
72t2t
25.559
70.7
Mass Flow Controller lD
Slze, ccm:
Make:
Model:
5/N:
#1
10,000
Environics
4040
455242003
#2
10,000
Environics
4040
455242004
#3
1,000
Environics
4040
455242002
Set Flow True Flow Dlfference
cc/mln cc/mln
Set Flow True Flow Difference
cc/mln cc/mln
Set Flow True Flow Dlfference
cc/min cc/mln
5%
to%
20%
30%
40%
50%
60%
70%
80%
90%
100%
500 489 2.2%
1,000 987 L.3%
2,000 L,970 7.5%
3,000 2,985 0.5%
4,000 4,014 0.4%
5,000 5,034 0.7%
6,000 6,053 0.9%
7,000 7,084 L.2%
8,000 8,119 1.5%
9,000 9,156 L.7%
10,000 L0,202 2.o%
500 454 9.2%
1,000 9s9 4.L%
2,000 1,989 0.5%
3,000 3,003 0.L%
4,000 4,oL4 0.4%
5,000 5,033 0.7%
6,000 6,055 0.9%
7,000 7,093 L.3%
8,000 8,123 L.5%
9,000 9,150 1.8%
10,000 10,196 2.O%
50 47 6.0%
100 97 3.0%
200 196 2.O%
300 298 0.7%
400 400 0.0%
500 502 0.4%
600 602 0.3%
700 705 0.9%
800 810 t.3%
900 914 t.6%
1,000 1,020 2.o%
Date 4/19124
FrcrAIIEE),., n
Method 3l3A Data
T a.'LI:
Locadon MPC-Tesoro - Sdt Lrke Cttv Relinerv. UT
Source Wet Ges Scrubber - CEMS I
ProJect No. ASr-2Q?AQ!{? Q9!
02 Drtr CO2 Date
Date/Tlme Date/Tlme 2lt9l25 1t:05
Meke/ModeUSN Servomer 4900 100259
Premeter Cylinder ID Cyllnder
Concentretlon, 7o
Anelyzer
Concentretion, 7o Cyllnder ID Cyllnder
Concentretion, 7o
Analyzer
Concentrrtion, 7o
Zcro Gas Nitrogen 0.00 -0.02
High Renge Ges EB0069884 23.9 23.88
Mid Range Ges RRO253E 10.9 I 1.15
Concentration Span, 7o 23.9
Accuracy 0.5
Run No.Run I Run 2 Run 3
Prremeter O2c/o CO2YI OzY" CO2o/o O2e/o CO2c/o
Dete/Timc 21t912025 l 8:12 2n912025 I 8:13 2/t9/2025 l8:14
Analysis #l
Analysis #2
Andysis #3
Averege
I l.8l I 1.69 t[.67
tt.76 I 1.69 tl.71
tt_74 I 1.69 I1.68
tt _77 I 1.69 11.69
The tmaining consistuut b dssumed to be nitrogen.
AlIarEE)
I l ' 'l r I
Locedon MPC-Tesoro - Srlt Lrke Clty Reflnery, UT
Method 3/3A Data
Source lYet Ges Scrubber - CEMS 2
ProJect No. A5T-2025-0362-003
02 Dete CO2 Dete
Dete/Time Dete/Time 2t20125 13:47
Make/1!lodeUSN Servomer 4900 100269
Peremeter Cyltnder ID Cyllnder
l^nncenfrlflnn- o/^
Analyzer
Concenfnflon- o/^Cylinder ID Cyltnder
Concentntlon- o/"
Andyzer
l-nnnenfrlflnn o/^
Zero Ges Nitrogen 0.00 -0.02
Illgh Renge Gas EB0069884 23.90 23.92
Mld Range Ges RR02538 10.90 I l.l3
Concentretion Spen, 7o 23.9
Accurecy 0.5
Run No.Run I Run 2 Run 3
Parameter OzYo CO1Y"Oz"/, CO2o/o O2c/o CO2Y"
Dete/Time 212012025 l4.,29 2t20t2025 l4:30 2/2012025 14:31
Anelysls #1
Analysls #2
Analysis #3
Averrge
I 1.84 tt.92 tt.92
I1.85 I 1.89 I1.95
I 1.93 I 1.90 11.94
I 1.87 11.90 l 1.94
The remaining coreistual is 8flmed to be nitmga.
QA Data
Locedon MPC-Taoro - Selt Leke Clty Retrnery, III
Source Wct Grs Scrubber - CEMS I
ProJect No A5I:202S0362-003
Penmeter(s) VFR
Drte Pltot ID Evldence of Evldence of Crllbredon or
2tL9t2s P-l 107 no uo no
Fleld Belence Check
Dete 02n9t25
Balance ID:SCALE 76
Ccrtified Wcight ID:59952
Ccrtificd Wcisht (g):200.0
Mcasurcd Wcight (g)199.9
Wcight Differeoce (g):0.1
Dete BeromeHc Evideuce of
drmrpa?Reeding Verlfied uluDraEon or
D---t- ----t,-1,IVeether Stedon Locedon
2^9t25 Wcathcr Station NA NA NA Salt l^ake City, UT
Drte Meter Bo! ID Posldve Prersure Leek Check
2t19t25 MB-706 Pass
Rergent Lot#Field Prep
nerformed Fleld Lot Drte By
Dl Water 231106
QA Data
Locrtion MPC-Tecoro - Selt Lekc Clty Refrnery. UT
Source Wet Grr Scrubbcr - CEMS 2
Project No. A!29219!{2 a01
Prremeter(s) VFR
Dete Pitot II)Evldence of Evidence of Cdibredon or
Damll ;aanl;od
2^9t25 P-llu no no tro
Fleld Belruce Check
I)rte 02t20t25
Balancc ID:SCALE 76
Certificd Wcight ID:69952
Certilicd Wcight (g):200.0
Mcasurcd Wcight (g):199.9
Wcight Differcncc (g):0.1
Detc Brrometric
Prarrrrta
Evidence of
tlrfrroa2 Reeding Vcrified Calibn0on or
DoaoL ranrriral?We.ther St don Locetion
2/20/25 Weather Station NA NA NA Salt Lrke City, UT
Drte Meter Bor II)Posldve Pressure Leek Check
2/19t25 MB-706 Pass
Resgent Lot#Field Prep Field Lot Dete By
Dl Water 231105
,=Alianrce DGM Calibration-Orifices
Document l[620.004
Revisior 24.0
Effective Dat( 1/31/24
lssuinq Department Tech Services Paq(1of1
Equipment Detail - Dry Gas Meter
Console lD: M8706
Meter S/N: 909032
Critical Orifice S/N: SH73-55
Calibration Detail
nitial Barometric Pressure, in. Hg (Pb)
:inal Barometric Pressure, in. Hg (PbF)
Averaoe Barometric Pressure, in. Ho (Pb)
25.67
25.67
25.67
lritifcal Orifice lD m
(' Factor, ft3.R12 / in. Wc.min (K )
y'acuum Pressure, in. Hg (Vp)
nitial DGM Volume, ft3 (Vm)
:inal DGM Volume, ft3 (Vmr)
l-otal DGM Volume. ft3 (Vm)
sH-73
0.7864
11.0
674.000
689.380
15.380
sH-73 SH-63
0.6007
14.0
723.500
739.*fi
15940
sH-63 sH-55
0.4524
Ib.U
756.000
nl151
.15.151
sH-55
0.786/0.601 0.452
11.0
706.880
722.387
15.507
14.0
739.600
755.570
15.970
tb.u
n1.800
786.730
14.930
{mbient Temperature, 'F (Ta)
nitial DGM Temperature, 'F (Tmr)
:inal DGM Temperature,'F tl-mr)
\veraoe DGM Temoerature, 'F ( Tm)
80
70
80
79
81u
86
85
82
86
87
87
82
87
89
88
82
89
89
89
82
89
90
90
Elapsed Time (O)
Meter Orifice Pressure, in. WC (AH)
Standard Meter volume, ft3 (Vmstd)
Standard Critical Orifice Volume, ft3 (Vcr)
Meter Correctron Factor m
Tolerance
Orifice Calibration Value (AH @)
Tolerance
Orifice Cal Check
15.00
2.90
13.0357
13.0343
1.000
0.000
1.831
0.102
15.00
2.90
12.9986
13.0223
1.002
0.001
1.814
0.119
20.00
1.80
13.2832
13 2507
0.998
0 003
1.922
0.011
20.00
1.80
13.2717
13.2507
0.998
0.002
1.917
U.U Ib
25.00
1.10
12.5431
12.4742
0.995
0.006
2.057
0.125
25.00
1.10
12.34t]9
12.4742
1.010
0 010
2.056
0.123
0.29 0.43 0.44
Veter Correction Factor m 1.000
frifice Calibration Value ( H @)1.933
)ositive Pressure Leak Check Yes
Equipment Detail - Thermocouple Sensor
Reference Calibrator Make: Omega Engineering
Reference Calibrator Model: CL23A Calibrator
Reference Calibrator S/N: T-197207
Calibration Detail
Reference Temp Display Temp.Accurary Absolute
Difference
OF x oF oR %OF
0
68
100
460
528
560
2
67
99
462
527
559
-0.4
0.2
0.2
2
1
1
223
248
273
683
708
733
224
249
274
6U
709
734
-0.1
-0 1
-0.1
1
1
'I
300
400
500
600
700
800
900
'1,000
1,100
1,200
760
860
960
1,060
1,160
1,260
1,360
1,460
1,560
1,660
300
399
498
599
701
800
900
1,001
1,101
1,200
760
859
958
1,059
1,161
1,260
1,360
1,461
1,561
1,660
0.0
01
0.2
0.1
-0.1
0.0
0.0
-0.1
-0.1
0.0
0
1
2
1
1
0
0
1
1
0
Personnel
XGK
Calibration By:
Calibration Date:
Reviewed By:
6rc/2024
All6rce Pitot Calibration-Wind Tunnel
Document lI 620.002
Revisior 23.0
Etfective Dat(wsn023
lsuing Departmenl Tech Seruices P"qe toTt
Equipment Detail
Model:
ID:
Iype S
P-'1104
Calibration Detail
Time
Ts
Pb
Std Pitot lD
Co'ta
13:28
73.8 'F
24.28 in. Hg
DEN-,I
o990
Flow
fps
APstd Hioh Side - "A"Low Side - '8"
Standard Start End APs
in. WC cp(a)
o
Deviation
APs
in. WC Cpb)
a
Deviationin. WC in. WC in. WC
20 0.07 0.07 0.07 0.'10 0.828 -0.012 0.10 0.828 -0.013
30 0.11 o.17 0.17 0.23 0.851 0.011 0.23 0.851 0.010
40 029 0.29 0.29 0.40 0.843 0.003 0.40 0.843 0.002
50 0.46 0.46 047 065 0.837 -0.003 0.u 0.844 0.003
60 0.66 066 065 0.92 0 835 -0.00s 0.93 0 831 -0.010
70 0.90 090 091 1.20 0 860 0.020 1.20 0 850 0.019
80 117 1.20 1.20 170 0 832 -0 008 170 0.832 -0.009
qn 1.49 150 150 210 0.837 -0.003 z.tu 0.837 -0.004
EPA Method 2 Section 10.1.3 QA/QC
50 0.46 0.46 0.45 n6\0 828 -0.012 0.64 0 835 -0 006
50 0.46 045 046 064 0.835 -0 005 055 0.828 -0.013
Averao( 0.840 0.008 0.841 0.009
Acceptability Criterii < 0.01 < 0.01
lCp(a)-Cp(b)l< 0 01 cp(a)-cp(b)l=0.001
Personnel
Calibrated By: Zach Clannin
Cali bration Date: 9/17 /2024
Reviewed ay:
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DMSION OF AR OI,IAUWlare
L_ GNOUP
RATA Report
Tesoro Refining and Marketing Company
Salt Lake City Refinery
474 West 900 North
Salt Lake ciry, uT 84103
Source Tested: COB Bypass & Regen
Test Dates: February 25 & 26,2025
Proj ect No. AST-2025 -037 7
Prepared By
Alliance Technical Group, LLC
3683 W 2270 S, Suite E
West Valley City, UT 84120
A/lElpeTICI]T.,JICAt GRCTJF Sourcc Tcsl Rcporl
Test Propram Summarv
Regulatory Informetion
Permit No.
Regulatory Cintions
Source Information
IIDAQ Permit No. DAQE-AN I 03350075- I 8
40 CFR 60, Appendix B, PS 2, 3, and 4
Source Name
COB Bypass
Regen
Contact Information
Target Parameters
Oz, SOz, NOx, CO
Oz. COz, CO
Test Location
Tesoro Refining and Marketing Company
Salt Lake City Refinery
474 West 900 North
salt Lake ciry, uT 84103
Facility Contact
f,fugannon Schaefer
Rschaefer@marathonpetroleum. com
[phone]
Test Company
Alliance Technical Group, LLC
3683 W 22705, Suite E
WestValley City, UT 84120
Project Manager
Charles Horton
[e-mail]
(3s2) 663-7s68
Field Team Leader
Alan Jensen
alan j ensen@alliancetg. com
[phone]
QA/QC Manager
Kathleen Shonk
katie. shonk@alliancetg. com
(8r2) 4s2-478s
Report Coordinator
Delaine Spangler
[e-mail]
Report Reviewer
Sarah Perry
sarah.perry@alliancetg. com
AST-2025-0377 Tesoro - Salt Lake City, LJ"f Page i
pJ/ldlEE)
laCt:l"l ICAL GnOtlP Source Tesl Reporl
C e rtifi c atio n S t at eme n t
Alliance Technical Group, LLC (Alliance) has completed the source testing as described in this report. Results
apply only to the source(s) and operating condition(s) that were tested during the specific test date(s) and time(s)
identified within this report. All results are intended to be considered in their entirety, and Alliance is not
responsible for use of less than the complete test report without written consent. This report shall not be reproduced
in full or in part without written approval from the customer.
To the best of my knowledge and abilities, all information, facts and test data are correct. Data presented in this
report has been checked for completeness and is accurate, error-free and legible. Onsite testing was conducted in
accordance with approved internal Standard Operating Procedures. Any deviations or problems are detailed in the
relevant sections of this test report.
This report is only considered valid once an authorized representative ofAlliance has signed in the space provided
below; any other version is considered draft. This document was prepared in portable document format (.pd| and
contains pages as identified in the bottom footer of this document.
41112025
Dateharles Horton, QSTI
Alliance Technicel Group, LLC
AST-2025-0377 Tesoro - Salt Lake City, u"I Page ii
AllErrEE)rICIlNICAL GNC[ 'Source Test Report
Table ofContentt
TABLE OF CONTENTS
1.3 Site Specific Test Plan & Notification.................. ....................... l-2
3.1 U.S. EPA Reference Test Method 3A - Oxygen/Carbon Dioxide........ ............ 3-l
3.2 U.S. EPA Reference Test Method 6C - Sulfur Dioxide........ ....... 3-l
3.3 U.S. EPA Reference Test Method 7E - Nihogen Oxides ............ 3-l
3.4 U.S. EPA Reference Test Method l0 - Carbon Monoxide.... ......3-2
3.5 U.S, EPA Reference Test Method 205 - Gas Dilution System Certification ......................... 3-2
3.6 Quality Assurance/Quality Control - U.S. EPA Reference Test Methods 3A, 6C, 7E and 10................... 3-2
LIST OF TABLES
Table2-l: Summaryof PerformanceSpecificationTestResults-COBBypass-PrimaryAnalyzer....................2-l
Table2-2: Summary of Performance Specification Test Results - COB Bypass - Redundant Analy2er................2-2
Table 2-3: Summary of Performance Specification Results - Regen - Primary.... ........2-2
Table 2-4: Summary of Performance Specification Results- Regen - Redundant... ......2-3
APPENDICES
Appendix A Sample Calculations
Appendix B Field Data
Appendix C Quality Assurance/Quality Control Data
Appendix D CEMS Data
AST-2025-0377 Tesoro - Salt Lake City, UT Page iii
pilt6rpe
Source Test Report
IntmductionTECHNICAL GROUP
1.0 Introduction
Alliance Technical Group, LLC (Alliance) was retained by Marathon Petoleum Corporation (NPC) to conduct
performance specification (PS) testing at the Tesoro Refining and Marketing Company (Tesoro) Salt Lake City,
Utah refinery. Portions of the facility are subject to provisions of 40 CFR 60, Appendix B, PS 2, 3, and 4 and the
Utah Deparhent of Environmental Quality, Division of Air Quality (UDAQ) Permit No. DAQE-AN103350075-18.
Testing was conducted as outlined in Table l-1 below.
Teble 1-1: Test Metrix
1.1 CEMS Descripdons
COB Bypass
Parameter:
Make:
Model:
Serial No.:
Pollutant
Oz / SOz /NOx / CO -Primary
Horiba
GI.76ICU
N2O3PGW
0-25%Oz
0-200 & 0-1,000 ppmvd SOz
0-200 & 0-1,000 ppmvd NOx
0-1,000 ppmvd CO
Pollutant
Oz / SOz / NOx / CO - Redundant
Horiba
GI-761CU
Y4WEOJGY
0-25%Oz
0-200 & 0-1,000 ppmvd SOz
0-200 & 0-1,000 ppmvd NOx
0-1,000 ppmvd CO
Span:
Parameter:
Make:
Model:
Serial No.:
Span:
Oxygen (Oz), Sulfur Dioxide (SOz), Nitogen Oxides
(NOx), Carbon Monoxide (CO)COB Bypass (Primary and Redundant)
Oxygen (Oz), Carbon Dioxide (COz), Carbon Monoxide
(co)Regen (Primary & Redundant)
AST-2025-0377-001 Tesoro - Salt Lake City, UT Pagc 1-1
AI =ta Source Test Report
Introduction
Regen
Parameter:
Make:
Model:
Serial No.:
Span:
Parameter:
Make:
Model:
Serial No.:
Span:
1.2 Project Team
Pollutant
OzlCOzlCO-Primary
Horiba
CMA.467H
EASVUCN2
0-5 YoOz
O-2OYoCOz
0-s%co
Pollutant
OzlCOzlCO-Redundant
Horiba
cMA-467H
xu2F2W0
0-5 YoOz
0-20%COz
0-s%co
Personnel involved in this project are identified in the following table.
Table 1-2: Project Team
MPC Personnel Rheannon Schaefer
Alliance Personnel Alan Jensen
Supilani Mailei
1.3 Site Specific Test Plan & Notification
Testing was conducted in accordance with the Site Specific Test Plan (SSTP) that was submitted to UDAQ by MPC.
1.4 Test Program Notes
EPA Methods I and 4 were enoneously included in the submitted test plan; however, these methods were not
applicable to the test program and were not included in testing.
AST-2025-0377-001 Tesoro - Salt Lake City, UT Page l-2
Source Tesl Reporl
Summary of Results
2.0 Summary of Results
Alliance conducted PS testing at the MPC facility in Salt Lake City, Utah on February 25 and 26,2025. Testing
included conducting a RATA to determine the RA of the Oz, SOz, NOx and CO CEMS serving the COB Bypass
primary and redundant CEMS, and to determine the RA of the Oz, COz, and CO CEMS serving the Regen primary
and redundant CEMS.
Tables 2-l through 2-4 provide summaries of the RA results in comparison to the applicable RA requirements. Any
difference between the summary results listed in the following tables and the detailed results contained in
appendices is due to rounding for presentation.
Table 2-l: Summary of Performance Specification Test Results - COB Bypass - Primary Analyzer
'Calculated using the applicable source standard for the pollutant. See Appendix B for the applicable standard used.
2 Calculated using the mean reference method.
CEMS
Per{ormence Test Datr RehdveAccuracy
Rcference
Method
Drtr
CEMS
Date
Per{ormence
Requireil
Performance
Demonstrrted
Carbon Monoxide Data
Concentration, ppmvd @ 0% Oz 21.09 21.42 <5Yo 0.10 Yo I
Nitrogen Oxides Data
Concentration, ppmvd @ 0% Oz 29.83 31.81 s20%15.09 yoz
Sulfur Dioxide Data
Concentration, ppmvd @ 0% Oz 95.07 91.51 s20%5.t0 %2
Oxygen Data
Concentration, % (dry)0.67 0.69 <20 0 15.15 Yo2
AST-2025-0377-001 Tesoro - Salt Lake City, tIT Page 2-l
Source Test Report
Summarv of Results
Table 2-22 Summary of Performance Specification Test Results - COB Bypass - Redundant Analyzer
t Calculated using the applicable source standard for the pollutant. See Appendix B for the applicable standard used
2 Calculated using the mean reference method.
Table 2-3: Summary of Performance Specification Results - Regen - Primary
I Calculated using the applicable source standard for the pollutant. See Appendix B for the applicable standard used
2 Calculated using the mean reference method.
CEMS
Per{ormence Test Dete Rehdve Accurecy
Reference
Method
Dete
CEMS
Dete
Per{ormance
Required
Performance
Demonstreted
Carbon Monoxide Data
Concentration, ppmvd @ 0% Oz 37.89 48.12 s5%2.28 Yo I
Nitrogen Oxides Data
Concenhation, ppmvd @ 0% Oz 53.31 59.43 s20%12.$ Yo2
Sulfur Dioxide Data
Concentration, ppmvd @ 0% Oz 88.04 85.33 <20 Yo 6.41 Yo2
Oxygen Data
Concentratior.,% (dry)1.52 1.56 a20%2.99 Yo2
CEMS
Per{ormence Test Drtr Relstive Accurecy
Reference
Method
Dete
CEMS
I)ate
Performence
Requlred
Performence
Demonstreted
Carbon Monoxide Data
Concentration, ppmv (dry)20.42 0.00 s5%0.048 % '
Oxygen Data
Concenhation, % (dry)o.67 0.61 s20%12.77 Yoz
Carbon Dioxide Data
Concentration,% (dry)16.48 t7.tI s20%4.47 Yoz
AST-2025-0377-001 Tesoro - Salt Lake City, UT Page 2-2
pul6rpe
TECHNICAL GROUP Source Test Repon
Sutmuryof Rerll,lrs
Trble 2-f : Summery of Per{ormance Speclficrdon Resultr Regen - Redundent
I 1a[sufttrd rrring thc 4,plicablc sourcc ctalrdard fff the pollutaot Scc Appcodix B for thc aplicablc sbrdad uscd.
2 Calorlatcd using thc mcan rcfcrcncc mcrhod"
Cerbon Monodde Dete
Concentration" ppmv (dry)
Orygen Dete
Concentration,% (ey)
Cerbon Dlorlde Detr
Concentration, % (dry)
AST-2025-0377-001 Tcsoro - Salt Lakc Crty, Uf
Source Test Reporl
Testing Methodologt
3.0 Testing Methodology
The emission testing program was conducted in accordance with the test methods that are listed in Table 3-1.
Method descriptions are provided below, and quality assurance/quality control data is provided in Appendix C.
Table 3-1: Source Testing Methodology
3.1 U.S. EPA Reference Test Method 3A - Oxygen/Carbon Dioxide
The oxygen (O:) and carbon dioxide (COz) testing was conducted in accordance with U.S. EPA Reference Test
Method 3A'. Data was collected online and reported in one-minute averages. The sampling system consisted of a
stainless-steel probe, Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas
conditioning system was a non-contact condenser used to remove moisture from the stack gas. If an unheated
Teflon sample line was used, then a portable non-contact condenser was placed in the system directly after the
probe. Otherwise, a heated Teflon sample line was used. The quality control measures are described in Section 3.3.
The relative accuracy of the Oz and COz CEMS was determined based on procedures found in 40 CFR 60,
Performance Specifi cation 3.
3.2 U.S. EPA Reference Test Method 6C - Sulfur Dioxide
The sulfrr dioxide (SOz) testing was conducted in accordance with U.S. EPA Reference Test Method 6C. Data was
collected online and reported in one-minute averages. The sampling system consisted of a heated stainless steel
probe, Teflon sample line(s), gas conditioning system and the identified analyzer. The gas conditioning system was
a non-contact condenser used to remove moisture from the sowce gas. If an unheated Teflon sample line was used,
then a portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon
sample line was used. The quality control measures are described in Section 3.6.
The relative accuracy of the SOz CEMS was determined based on procedures found in 40 CFR 60, Performance
Specihcation 2.
3.3 U.S. EPA Reference Test Method 7E - Nitrogen Oxides
The nitrogen oxides (NOx) testing was conducted in accordance with U.S. EPA Reference Test Method 7E. Data
was collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe,
Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas conditioning system was a
non-contact condenser used to remove moisture from the stack gas. If an unheated Teflon sample line was used,
then a portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon
sample line was used. The quality control measures are described in Section 3.6.
Peremeter U.S. EPA Reference
Test Methodc NoteslRemarkc
Oxygen / Carbon Dioxide 3A Instrumental Analysis
Sulfur Dioxide 6C Instrumental Analysis
Nitrogen Oxides 7E Instrumental Analysis
Carbon Monoxide l0 Instumental Analysis
Gas Dilution System Certification 205
AST-2025-0377 Tesoro - Salt Lake City, UT Page 3-l
pul6rpEr
r I c t] t.J I c A 6; p 1; l.rP Source Test Report
Testing Methodologt
The relative accuracy of the NOx CEMS was determined based on procedures found in 40 CFR 60, Perfonnance
Specification 2.
3.4 U.S. EPA Reference Test Method 10 - Carbon Monoride
The carbon monoxide (CO) testing was conducted in accordance with U.S. EPA Reference Test Method 10. Data
was collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe,
Teflon sample line(s), gas conditioning system, and the identified gas analyzer. The gas conditioning system was a
non-contact condenser used to remove moisture from the gas. If an unheated Teflon sample line was used, then a
portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample
line was used. The quality contol measures are described in Section 3.6.
The relative accuracy of the CO CEMS was deterrnined based on procedures found in 40 CFR 60, Perforrnance
Specification 4.
3.5 U.S. EPA Reference Test Method 205 - Gas Dilution System Certification
A calibration gas dilution system field check was conducted in accordance with U.S. EPA Reference Method 205.
An initial three (3) point calibration was conducted, using individual Protocol I gases, on the analyzer used to
complete the dilution system field check. Multiple dilution rates and total gas flow rates were utilized to force the
dilution system to perform two dilutions on each mass flow controller. The diluted calibration gases were sent
directly to the analyzer, and ttre analyzer response recorded in an electronic field data sheet. A mid-level supply gas,
with a cylinder concentration within l0% of one of the gas divider settings described above, was introduced directly
to the analyzer, and the analyzer response recorded in an electonic field data sheet. The cylinder concentation and
the analyzer response agreed within 2%. These steps were repeated three (3) times. The average aralyzer response
agreed within 2Yo of the predicted gas concentration. No single injection differed more than 2Yo from the average
instrument response for that dilution. Copies of the Method 205 data can be found in the Quality Assurance/Quality
Contol Appendix.
3.6 Quality Assurance/Quality Control - U.S. EPA Reference Test Methods 3A, 6C, 7E and l0
Cylinder calibration gases used met EPA Protocol I (+l- 2%) standards. Copies of all calibration gas certificates can
be found in the Quality Assurance/Quality Contol Appendix.
Low Level gas w.rs introduced directly to the analyzer. After adjusting the analyzer to the Low-Level gas
concentration and once the analyzer reading was stable, the analyzer value was recorded. This process was repeated
for the High-Level gas. For the Calibration Error Test, Low, Mid, and High Level calibration gases were
sequentially introduced directly to tle analyzer. All values were within 2.0 percent of the Calibration Span or 0.5
ppmv I Yo absolute difference.
High or Mid-Level gas (whichever was closer to the stack gas concentration) was introduced at the probe and the
time requked for the analyzer reading to reach 95 percent or 0.5 ppmv/% (whichever was less restrictive) of the gas
concentration was recorded. The analyzer reading was observed until it reached a stable value, and this value was
recorded. Next, Low Level gas was intoduced at the probe and the time required for the analyzer reading to
decrease to a value within 5.0 percent or 0.5 ppmv/% (whichever was less restrictive) was recorded. If the Low-
Level gas was zero gas, the response was 0.5 ppmv/%o or 5.0 percent of the upscale gas concentration (whichever
was less restrictive). The analyzer reading was observed until it reached a stable value and this value was recorded.
AST-2025-0377 Tesoro - Salt Lake City, UT Page3-2
pul6rrrcE)
r-l tl i-r Source Test Report
Testing Methodologt
The measurement system response time and initial system bias were determined from these data. The System Bias
was within 5.0 percent of the Calibration Span or 0.5 ppmv/% absolute difference.
High or Mid-Level gas (whichever was closer to the stack gas concentration) was introduced at the probe. After the
analyzer response was stable, the value was recorded. Next, Low Level gas was intoduced at the probe, and the
analyzer value recorded once it reached a stable response. The System Bias was within 5.0 percent of the
Calibration Span or 0.5 ppmvlYo absolute difference or the data was invalidated and the Calibration Error Test and
System Bias were repeated.
Drift between pre- and post-run System Bias was within 3 percent of the Calibration Span or 0.5 ppmv/% absolute
difference. If the drift exceeded 3 percent or 0.5 ppmv/%, the Calibration Error Test and System Bias were repeated.
If the pollutant concentration at each traverse point did not differ more than 5 percent or 0.5 ppmv/0.3% (whichever
was less restrictive) of the average pollutant concentration, then single point sampling was conducted during ttre test
mns. If the pollutant concenhation did not meet these specifications but differed less than l0 percent or 1.0
ppmvl0.SYo from the average concentration, ttren three (3) point sampling was conducted (stacks less than 7.8 feet in
diameter - 16.7,50.0 and 83.3 percent of the measurement line; stacks greater than 7.8 feet in diameter - 0.4, 1.0,
and 2.0 meters from ttre stack wall). If the pollutant concentation diffsred by more than l0 percent or 1.0
ppmv/O.SYo from the average concenhation, then sampling was conducted at a minimum of twelve (12) traverse
points. Copies of stratification check data can be found in the Quality Assurance/Quality Conhol Appendix.
An NOz - NO converter check was performed on the analyzer prior to initiating testing and at the completion of
testing. An approximately 50 ppm nitrogen dioxide cylinder gas was inhoduced directly to the NOx analyzer and
the instrument response was recorded in an electonic data sheet. The instrument response was within +/- 10 percent
of the cylinder concenhation.
A Data Acquisition System with battery backup was used to record the instrument response in one (l) minute
averages. The data was continuously stored as a *.CSV file in Excel forrnat on the hard drive of a computer. At the
completion of testing, the data was also saved to the Alliance server. AII data was reviewed by the Field Team
Leader before leaving the facility. Once arriving at Alliance's offrce, all written and electonic data was
relinquished to the report coordinator and then a final review was performed by the Project Manager.
AST-2025-0377 Tesoro - Salt Lake City, I-J"t Page 3-3
AI
lr
MPC-Tesoro - Salt Lake
Run No. /IVlethod Run I / Method 3A
Or - Outlet Concentration (C6), o/o dry
Co": (Cou.-Co)* ( fr;t
where,Cob" 0.70 : average analyzervalue during test, % dryC"-:66-: average of pretest & posttest zero responses,Yo dry
CM
-TfTF:
actual concentation of calibration gas,ohdry
CM-TI:OF: average of pretest & posttest calibration responses, 0/o dry
C6,-E[-: Oz Concenhation, % dry
COr - Outlet Concentration (C6e), o/o dry
Cco: (Cou.-Co)x ( fr;)
where,Cou. 16.84 : average analyzer value during test, % dryC".Ttr-: average of pretest & posttest zero responses,oh dryCMA-TIEF: actual concentration of calibration gas,Yo dryCM-Tffi4-: average of pretest & posttest calibration responses, 0/o dryCco,-V-: CO, Concentration, % dry
Example Calculations
=]aAIlEE!
I i: :'
Example Calculations
MPC-Tesoro - Salt Lake
Source: COB Bwass -
Project No.: AST-2025-0377
Run No. /Itlethod Run I / Method 6C
SOr - Outlet Concentration (Cse), ppmvd
Cso,: (Cou.-Co)*( ffO
where,Cob, 89.81 : average analyzer value during test, ppmvdC"-.4,-: average of pretest & posttest zero responses, ppmvd
CMA-0'0'5F: acflral concentration of calibration gas, ppmvd
CM.7967I- = average of pretest & posttest calibration respoffies, ppmvd
Cso,
-9TZT-
= SO, Concentation, ppmvd
SO: - Outlet Concentration (C56,"s), ppmvd @0o/o Ot
Cso."o: Cso,x (
where,Cso, 91.21 : SOz - Outlet Concenffation, ppmvd
Ce, --.8[- = oxygen concentration, o/o
Cro,"o To8- : ppmvd @o% oz
AI =taIGE>Example Calculations
Location: MPC-Tesoro - Salt Lake
Run No. /IVlethod Run I / Method 7E
NOx - Outlet Concentration (CNq), ppmvd
cNo,: (co6,-ce)x ( ({"-cfuJ)
where,Cor. 26.09 : average analyzer value during tesl ppmvd
C..-.41-: average of pretest & posttest zero responses, ppmvd
CM^-T6'650-: actual concentration of calibration gas, ppmvd
CM.-7T-: average of pretest & posttest calibration responses, ppmvd
CNo*
-633-
= NOx Concentration, ppmvd
NOx - Outlet Concentration (CNs,a), ppmvd @ 0yo O,
\.NOrc0 -
CNo,
cNo*x (#
where,26.33 : NOx - Outlet Concentration, ppmvd
Cs, .-.EI- : oxygen concentration, o/o
c***- :ppmvd @o%o,
Example Calculations
Location: MPC-T..oro - S"lt L"ke Ci
Source:ProjectNo.:ffi
Run No. ilVlethod Run I / Method l0
CO - Outlet Concentration (C6s), ppmvd
where,
cco= (co5.-ce)x 1 ffil
Core 19.39 : average analyzer value during test, ppmvd
C".-[.d-: average of pretest & posttest zero responses, ppmvd
CMA--5[0F: actual concentration of calibration gas, ppmvd
CM--E3-: average of pretest & posttest calibration respoffies, ppmvd
Cco-TfZT-: CO Concentation, ppmvd
CO - Outlet Concentration (Csq"6), ppmvd @lyo O,
Cco"o: Ccox (-#
where,Cco 19.61 : CO - Outlet Concentation, ppmvd
Co,
-IIE[-
: oxygen concenhation, 7o
Cco"o 20.23 :ppmvd @0%O2
CO Summary
Loce6on: MPC-Tesoro - Salt Lake City Refinery, UT
Sooaa"t
Project No. : AST -2025 -O37 7
Run
No.Dete Time Rcference Method
CO Concentredon
oomvd @.0 7o O,
CEMS
CO Concentredon
oomvd@07oO:
Averrge
Dllferencc
oomvd@07nO,Strrt End
I
2
3
4
5
6
7
8
9
2t25t25
2125t25
2t25125
2125/2s
2/25t25
2t25t2s
2t25t25
2/2512s
2t25t25
l:50
2:ll
2:32
3:30
3:51
4:12
5:05
5:26
5:47
2:10
2:3L
2:52
3:50
4:l I
4:32
5:25
5:46
6:07
20.23
21.02
21.44
22.95
21.15
2t.62
20.78
20.21
20.42
20.55
21.77
2r.99
23.04
2t.29
2t.69
2r.20
20.62
70 66
-0.32
-0.75
-0.55
-0.09
-0.14
-0.07
-0.42
-0.41
-0.24
Average 21.09 21.42 -0.331
Standard Dwiation (Sd 0.227
Aoolicable Source Standard (AS'500
Con-fi dence Coefficient (CCl 0.t74
Reledve Accurecy @A)0,10 vo
Performance Requircd - Applicable Source Standard RA< 5%
Performance Soecilication Method PS4
Conlldence Coellicienl CC
cc=lff,.sal
where,
h.czs
n
sd
CC
2.306 : degrees offreedom value: number ofruns selected for calculating the RA: standard deviation ofdifference: confidence coefficient
0.227
o.tu
Reladve Accurecy, RA
ld I + lcclM = 7ri;;pixloo
where,
d -0.33 = average difference of Reference Method and CEMS
ccT = confi dence coeffi cient
AS 500.000 = applicable source standard, ppmvd, @ 0 %o OzRA 0.10 = relative accuracy, 7o
NOx Summary=rarEE>AI
Locrdon:
Source:
Project No.:
MPC-Tesoro - Salt lake
COB Bvpass -
Run
No.Drte Time Reference Method
NOr Coucentredon
ppmvd@07oOr
CEMS
NOr Concen&rdon
nomvd tO 0 7" O,
Averege
I)iffercnce
Dpmvd@07oOrStsrtEnd
I
2
3
4
5
6
7
8
9
2t25t25
u2st25
u25/25
2t2st2s
2125t25
2125t25
2t25t2s
2125125
2t25t25
l:50
2:ll
2:32
3:30
3:51
4:12
5:05
5:26
5:47
2:10
2:31
2:52
3:50
4:ll
4:32
5:25
5:46
6:07
27.16
28.26
26.61
26.56
35.54
34.62
29.60
29.23
30.89
3 1.66
35.83
32.35
26.44
35.87
31.91
30.63
30.72
30.89
-4.50
-7.57
-5.74
0.r2
-0.33
2.71
-1.03
-t.49
0.00
Averagt 29.83 31.81 1.982
Standard Deviation (Sd 3.276
Con-fi dence Coeffi cient (CC'2.5 18
Rehtive Accuncv (RA'1s.09 vo
Performance Required - Mean Refercnce Metho<RA< 20%
Performancc Specifi cation Metho<PS2
Confidence Coelficlenl CC
cc = lto'Zt, sallVn I
where,
hgr 2.306 = degrees of freedom value
n 9 = number ofruns selected for calculating the RASd.TU-= standard dcviation of diffcrcnce
CC TJI-= confidence coefficient
Reledve Accurecy, RA
ld l+ lcclRA = 7r;;77ix 1oo
where,d -1.98 _= average difference of Refere,nce Method and CEMS
cC TJI-- confidence coefficientRM 29329 -= reference metiod, ppmvd @ 0 % O:
RA-136f = relative accuracy, 7o
AI Fla SO2 Summary
Locedon: MPC-Tesoro - Salt lake ur
Source:.1@.!ry!
Project No. : AST -2025 -037'l
Run
No.Dete Time Reference Method
SO: Concentredon
oomvd (O 0 7o O,
CEMS
SOr Concentrrdon
nomvd tO 0 7n O,
Averrge
Dlfference
onmvd@07oOrStrrtEnd
I
1
3
4
5
6
7
8
9
2t25t25
2t25l2s
2t25t25
2125l2s
2/25t25
2/25125
2t25t25
2125125
2l25l2s
1 l:50
12:11
12''32
13:30
13:51
l4:12
15:05
L5:26
l5:47
2:10
2:31
2:52
3:50
4:l I
4:32
5:25
5:46
6:0'1
94.08
92.29
98.1 8
106.14
90.31
95.63
94.95
94.42
89.65
87.95
90.40
94.30
101.30
86.33
90.s6
92.33
91.62
88.84
6.13
1.89
3.88
4.84
3.98
5.07
2.62
2.80
0.81
Averagt 95.07 91.51 3.559
Standard Dwiation (Sd)r.682
Confi dence Coeffi cient (CC)1.293
Reladve Accurecv (RA)5.103 Y"
Performance Requircd - Mean Refer€nce Method RAs 20%
Performance Specification Method PS2
Conlldence Coeflicienl CC
cc : lto'3t * sallVn I
where,
h.srs
-!][
= degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd l.6-6r-= standard deviation of diflerence
CC 1.293 = conlidence coefficient
Reledve Accurecy, RA
ld l+ lcclM = ;3;;;7' xloo
where,
d 3.56 : averaSe difference of Reference Method and CEMS
CCT = confidence coeffi cient
RM 9-5J-73 = reference method, ppmvd @ 0 %o Oz
RA 5.10 = relative acoracy,Vo
02 SummarylEe=TAAI
Locetion: MPC-Tesoro - Salt Lake UT
Source:
Project No. : AST -2025 -037 7
Run
No.Drte Time Reference Method
Or Concentretlon
o/o dry
CEMS
O: Concentredon
o/o ilw
Avcnge
Dlfference
o/o ilwStrrtEnd
I
2
3
4
5
6
7
8
9
2t25t25
2125125
2t25t25
2t25t25
2t25t25
2t25t25
2125t2s
2125t25
2t2st2s
l:50
2:ll
2:12
3:30
3:51
4:12
5:05
5:26
5:47
2:10
2:31
2:52
3:50
4:11
4:32
5:25
5:46
6:07
0.64
0.70
0.62
0.60
0.77
0.64
0.63
0.66
0.76
0.69
0.82
0.69
0.42
0.90
0.69
0.66
0.69
0.69
-0.05
-0.t2
-0.0'7
0.18
-0. 13
-0.05
-0.03
-0.03
0.07
Averagr 0.67 0.69 -0.026
Standard Deviation (Sd'0.098
Confi dence Coeffi cietrt (CC'0.075
Reledve Accuncv (RA'15.15 V"
Performance Required - Mean Reference Metho<RA< 20%
Performancc Soecifi cation Metho<PS3
Conlldence Coefficicnt CC
cc=lff.sal
where,
= degrees offreedom value
= number ofruns selected for calculating the RA
= standard deviation ofdifference
0.075 = confidence coelEcient
Rehdve Accurrcy, RA
ld l+ lcclRA = 73i;7p:x 1oo
where,
d -0.03 = average difference of Reference Method and CEMS
CC 0.075 = con-fidence coelEcient
RM 0.669 : reference metho(% dry
RA 15.15 =relative acasacy,Yo
2.306
9
h.s'rs
n
sd
cc
0.098
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II(
=taAI Runl-RMData
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-0377
Dste:2/25125
Time
Unit
Stetus
Or - Outlet
%o ilry
Valid
0.70
I 1.00
0.06
0^06
0.06
I l.0l
10.98
I1.00
0.64
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Ges Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
19.39
50.00
0.00
-0.12
-0.06
50.00
49.08
49.s4
19.6t
20.12
19. I
r 9.33
19.03
18.88
19.85
19.41
19.93
19.s9
19.70
19.63
18.91
18.66
18.82
19.16
19.82
19.96
t9.45
19.51
I 8.81
t9.s4
26.09
100.00
0,55
0.31
0.43
97.7s
98.02
97.89
26.33
89.81
500.00
0.s0
0.36
0.43
490.4t
490.42
490.42
9t.2t
I l:50
I l:51
ll:52
I l:53
I l:54
I l:55
I l:56
I l:57
I l:58
I l:59
l2:00
l2:01
l2:02
l2:03
l2:04
l2:05
l2:06
l2:07
l2:08
l2:09
l2: l0
0.70
0.64
0.70
0.71
0.72
0.77
0.72
0.69
0.69
0.69
0.68
0.63
0.67
0,67
0.66
0.70
0.66
0.72
0.72
0.70
0.76
26.14
2s.40
26.11
26.69
26.55
27.59
26.27
26.26
25.87
25.67
2s,59
25.15
25.72
26.06
2s.36
26.10
25.35
26.18
26.68
2s.98
27.16
90.50
92.t4
91.63
88.68
86.87
83.1 4
85.99
90.26
87.28
91.90
93.08
90.53
9l .s8
90.45
93.36
92.60
92.0t
90.03
87.59
89.27
87.10
AI =TAIEE)Run2-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bwass - Primary Analyzer
Project No.: AST-2025-0377
Dste:2/25/25
Time
Unit
Stetus
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
Yo dry
Valid
0.75
I 1.00
0.06
0.06
0.06
ll.0l
10.98
I1.00
o.'70
27.0s
100.00
0.55
0.31
0.43
97.75
98.02
97.89
27.31
87.86
s00.00
0.50
0.36
0.43
490.41
490.42
490.42
89.22
CO - Outlet NOx - Outlet SOr - Outletppmvd ppmvd ppmvd
Valid Valid Valid
s0.00
0.00
-o.12
-0.06
50.00
49.08
49.54
20.32
l2:ll
12:12
12:13
l2:14
l2:15
l2:16
l2:17
12: l8
12:19
l2:20
l2:21
l2:22
l2:23
l2,,24
l2:25
l2:26
l2:27
l2,,28
l2,,29
l2:30
l2:31
0.73
0.'74
0.72
0.76
0.70
0.74
0.67
0.69
0.72
0.76
0.79
0.8s
0.82
0.78
0.79
0.75
0.76
0.76
0.77
0.75
0.76
19.31
20.87
20.08
20.16
19.61
19.59
19.68
I 8.81
19.65
19.97
20.66
20.55
20.80
20.00
20.13
20.67
19.88
20.s9
20.52
20.49
20.04
26.88
26.83
26.50
26.99
26.41
26.85
2s.86
26.17
26.34
26.81
27.50
28.68
28.44
27.65
2',7.56
26.80
27.24
27.33
27.43
26.6s
27.t0
86.80
8s.84
89.41
86.27
87.51
87.96
91.55
9t.69
90.70
88.87
8',7.33
82.93
82.99
86.92
87.29
88.52
88.48
87.71
87.62
89.76
88.79
=laAI Run3-RMData
MPC-Tesoro - Salt Lake City Refinery, UTLocation:
Source:
Project No.:
COB Bypass - Primary Analyzer
AST-202s-0377
D*e:2/25125
Time
Unit
Status
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cs,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
%o ilry
Valid
0.68
I 1.00
0.06
0.06
0.06
I l.0l
10.98
I 1.00
0.62
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
20.58
50.00
0.00
-0.t2
-0.06
s0.00
49.08
49.54
20.80
25.60
100.00
0.55
0.31
0.43
97.75
98.02
97.89
25.82
93.79
s00.00
0.50
0.36
0.43
490.41
490.42
490.42
9s.27
l2:32
l2:33
l2:34
l2:35
l2:36
l2:37
l2:38
l2:39
l2:40
l2:41
l2:42
l2:43
l2:44
l2:45
l2:46
l2:47
l2:48
l249
l2:50
12:51
12:52
0.62
0.s0
0.57
0.70
0.78
0.83
0.88
0.81
0.71
0.69
0.57
0.s7
0.58
0.62
0.62
0.66
0.68
0.68
0.75
0.68
0.72
21.01
28. l0
20.69
22.32
20.64
20.23
20.91
20.20
19.2s
t9.24
19.4r
22.27
20.89
18.79
t9.47
18.70
20.38
19.22
20.90
19.96
19.53
25.11
22.00
23.6s
26.14
27.24
28.38
28.71
28.29
26.38
26.t1
23.98
23.7t
23.94
24.40
24.64
2s.39
2s.60
2s.64
26.36
25.79
26.08
97.26
I 10. l8
t03.47
94.09
88.70
84.68
81.22
81.49
87.01
92.20
97.t0
101.05
l0l.s9
99.87
98.23
94.71
94.03
93.29
89.54
89.s5
90.32
AI =la Run4-RMData
Locetion: MPC-Tesoro - Salt Lake CiW Refinery, UT
Source: COB Bypass - Primary Anallzer
Project No.: AST-2025-0377
D*ez 2125125
Time
Unit
Status
Or - Outlet
o/o dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou.)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
0.66
l 1.00
0.06
0.06
0.06
10.98
10.97
10.98
0.60
21.92
50.00
-0. l2
0.27
0.08
49.08
49.06
49.07
22.29
2s.63
100.00
0.31
0.64
0.48
98.02
97.9s
97.99
25.79
101.34
s00.00
0.36
0.15
0.26
490.42
490.68
490.ss
Corrected Run A
l3:30
l3:31
13:32
l3:33
13:34
l3:35
l3:36
13:37
l3:38
l3:39
l3:40
l3:41
13:42
l3:43
13:44
13:45
13:46
13:47
l3:48
13:49
l3:50
0.61
0.64
0.74
0.77
0.76
0.74
0.74
0.69
0.6s
0.65
0.56
0.s4
0.5s
0.60
0.56
0.70
0.64
0.68
0.68
0.57
0;13
28.04
19.01
19.73
19.59
23.67
21.66
18.80
2r.27
22.89
21.05
23.67
2s.48
24.38
27.28
22.28
18.62
22,20
21.23
19.50
22.12
17.83
25.23
2s.71
27.05
27.71
27.15
26.87
27.25
26.14
2s.66
25.M
24.04
23.43
23.74
24.42
24.27
26.09
2s.16
25.'19
26.28
23.99
26.76
103.79
101.06
98.62
9s.02
96.94
96.84
96.06
99.47
101.60
100.71
104.54
108.09
107.72
106.97
105.27
99.90
101.92
100.60
100.46
104.79
97.69
Run5-RMData
Location:
Source:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
COB Bypass - Primary Analrzer
AST-202s-0377
Date:2125125
Time
Unit
Status
Or - Outlet
Vo ilry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Averege (Com)
Csl Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
0.82
I1.00
0.06
0.06
0.06
10.98
10.97
10.98
0.77
20.04
50.00
-0.12
0.27
0.08
49.08
49.06
49.07
20.37
33.86
100.00
0.31
0.64
0.48
98.02
97.95
97.99
34.24
85.56
500.00
0.36
0.15
0.26
490.42
490.68
490.s5
86.99Corrected Run A
l3:5 I
13:52
l3:53
l3:54
l3:55
l3:56
13:57
l3:58
l3:59
l4:00
l4:01
l4:02
l4:03
l4:04
l4:05
l4:06
l4:07
l4:08
l4:09
l4: l0
l4:ll
0.84
0.88
L00
1.00
0.78
0.74
0.'73
0.74
0.76
0.88
0.89
0.88
0.87
0.90
0.87
0.81
0.81
0.78
0.74
0.69
0.67
18.38
19.02
t9.4s
20.61
r 9.36
19.29
19.16
19.06
t9.75
20.55
20.94
21.34
20.93
21.59
21.s3
21.26
20.09
20.t9
19.'t6
19.61
18.94
28.24
29.10
30.81
30.76
30.20
29.35
32.72
34.37
34. l5
37.07
37.20
37.29
37.00
37.16
37.17
35.56
36.58
35.1 5
34.68
33.42
33.06
91.94
88.38
84.67
83.71
85.38
87.52
89.36
88.69
89.62
82.8s
82.27
80.42
79.49
81.85
80.73
81.01
80.97
85.85
87.04
91.73
93.23
Run6-RMData=TATEE)AI
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-031'7
D*ez 2/25125
Time
Unit
Status
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
O: - Outlet
o/o dry
Valid
0.69
I 1.00
0.06
0.06
0.06
10.98
10.97
10.98
0.64
0.67
0.63
0.73
0.78
0.82
0.81
0.83
0.79
0.74
0.60
0.s6
0.s4
0.52
0.53
0.s6
0.61
0.71
0.79
0.83
0.76
0."11
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
20.62
50.00
-0.t2
0.27
0.08
49.08
49.06
49.O7
20.97
33.20
100.00
0.31
0.64
0.48
98.02
97.95
97.99
33.s6
91.18
s00.00
0.36
0.15
0.26
490.42
490.68
490.55
92.72
l4:12
l4:13
l4:14
l4:15
l4:16
l4:17
l4:1 8
l4:19
l4:20
l4:21
l4:22
l4,,23
l4:24
l4,,25
l4,,26
l4,,27
l4:28
l4:29
l4:30
l4:3I
l4:32
19.16
20.92
19.65
19.70
20.51
20.48
20.41
20.1 8
20.68
2r.39
2t.92
19.92
28.38
22.7s
20.12
18.57
19.03
19.90
20.3s
19.76
t9.23
33.09
31.92
34.14
3s.04
36.24
35.69
36.s9
35.36
34.47
3r.23
30.29
30.09
28.92
29.s9
30.2s
3t.7t
33.30
35. l6
35.54
35.04
33.55
92.26
96.2t
92.01
87.2s
83.41
83.55
81.85
82.75
85.96
9s.92
99.33
101.03
103.81
100.76
99.68
97.17
9r.82
85.68
83.80
82.66
87.82
=IAAIlEE}RunT-RMData
Location: MPC-Tesoro - Salt Lake CiW Refinery. UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-0377
D*e:2/25125
Time
Unit
Stetus
Or - Outlet
Yo llry
Valid
0.68
I1.00
0.06
0.06
0.06
10.97
10.98
10.98
0.63
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou.)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
19.89
s0.00
0.27
0.24
0.26
49.06
48.84
48.95
20.16
28.48
100.00
0.64
0.34
0.49
97.95
97.99
97.97
28.7t
90.55
s00.00
0.15
0.29
0.22
490.68
490.49
490.59
92.t0
98.36
103.98
101.56
94,99
88.1 I
98.1 8
99.69
9s.20
86.28
80.74
76.65
77.33
'19.22
84.42
86.88
89.94
90.03
94.97
90.40
92.s9
91.9s
l5:05
l5:06
l5:07
l5:08
l5:09
l5: l0
l5:l I
l5:12
l5: l3
l5: l4
l5: l5
l5: l6
l5:17
l5:18
l5: l9
l5:20
l5:21
l5:22
l5:23
l5:24
l5:25
0.58
0.49
0.s2
0.63
o.7l
0.s3
0.58
0.65
0.80
0.87
0.87
0.86
0.84
0.74
0.69
0.71
0.68
0.59
0.66
0.66
0.65
21.47
21.24
19.06
17.77
18.36
22.14
19.58
l9.l I
18.88
t9.96
20.07
20.72
20.39
19.50
18.76
19.02
19.84
20.27
20.4s
20.21
20.88
30. l3
28.78
2s.49
26.86
28.s7
25.54
26.00
27.26
29.94
31.55
31.43
31.01
30.86
29.40
28.45
28.03
28.20
26.42
28.38
27.89
27.81
AI FTATEE)RunS-RMData
Location: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-0377
Dilez 2/25/25
Time
Unit
Stetus
Uncorrected Run Average (Cou,)
Cal Ges Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Averege Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
u/o dry
Valid
0.72
I1.00
0.06
0.06
0.06
t0.97
10.98
10.98
0.66
0.64
0.67
0.68
0.76
0.74
0.68
0.71
0.67
0.72
0.71
0.72
0.74
0.84
0.81
0.81
0.74
0.'14
0.66
0.65
0.73
0.69
CO - Outlet
ppmvd
Valid
19.31
50.00
0.27
0.24
0.26
49.06
48.84
48.9s
19.57
t7.89
18.50
18.97
19.74
t9.96
18.26
18.68
20.76
19.53
18.88
19.07
18.97
18.75
19.27
t9.42
19.30
19.72
21.64
18.36
19.57
20.29
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
28.08
100.00
0.64
0.34
0.49
97.9s
97.99
97.97
28.30
89.88
500.00
0.1s
0.29
0.22
490.68
490.49
490.s9
91.42
l5:26
l5:27
l5:28
l5:29
l5:30
15:31
l5:32
l5:33
l5:34
l5:35
l5:36
l5:37
l5:38
l5:39
l5:40
l5:41
l5:42
l5:43
l5:44
l5:45
l5:46
28. t0
28.32
28.72
29.90
29.63
26.91
27.87
26.51
27.97
27.43
27.55
28.s3
29.46
29.19
29.33
27.97
27.70
26.',|0
26.7t
27.92
27.20
90.s2
89.37
88.22
84.19
84.13
92.52
92.86
96.24
90.35
89.94
9t.t7
90.08
85.05
83.81
8s.62
88.98
90.86
94.46
9s.89
90.56
92.65
AI =TATEE}Run9-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-0377
D*e:2125125
Time
Unit
Status
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou.)
Cal Gas Concentration (CnoJ
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
0.82
I1.00
0.06
0.06
0.06
10.97
10.98
10.98
0.76
19.42
s0.00
0.27
0.24
0.26
49.06
48.84
48.95
t9.67
29.50
100.00
0.64
0.34
0.49
97.95
97.99
97.97
29.76
84.93
500.00
0.15
0.29
0.22
490.68
490.49
490.s9
86.37Corrected Run Averase (Corr
l5:47
l5:48
l5:49
l5:50
l5:51
l5:52
l5:53
l5:54
l5:55
l5:56
l5:57
15:58
l5:59
l6:00
l6:01
l6:02
l6:03
l6:04
l6:05
l6:06
l6:07
0.68
0.73
0.75
0.'75
0.77
0.86
0.87
0.88
0.84
0.86
0.79
0.82
0.83
0.74
0.7r
0.81
0.91
0.96
0.98
0.90
0.74
r8.77
19.50
18.79
18.44
18.54
19.07
19.3 I
19.30
19.21
19.61
20.52
r9.96
19.05
19.07
19.13
18.73
19.48
19.84
21.29
20.70
19.41
27.30
27.63
28.42
28.49
28.45
30. l4
30.39
30.73
30.28
30.05
28.9s
29.60
29.56
28.s9
27.23
29.t8
30.84
31.81
32.49
30.92
28.38
93.s0
91.s9
89.1 8
87.62
90.07
82.73
79.86
78.42
81.34
83.19
86.52
85.29
85.94
87.87
90.59
87.42
80.96
'79.23
75.05
79.89
87.1 8
AI =TATEE CO Summary
Locedon: MPC-Tesoro - Salt lakc City Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Run
No.Dete Tlme Reference Method
CO Concentretion
ppmvd@0%Or
CEMS
CO Concentretion
ppmvd@07cOr
Average
Dilference
ppmvd@07oOrStrrtEnd
I
2
3
4
5
6
7
8
9
2t26t25
2t26t25
2t26t25
2126125
2t26t25
2t26t25
2t26125
2t26t25
2t26t25
0:30
0:51
l:12
2:00
2:21
2:42
3:30
3:51
4..12
0:50
l:ll
1:32
2:20
2:41
3:02
3:50
4:1 I
4:32
39.09
38.94
38.75
37.1O
37.05
37.78
36.74
36.39
39.1 5
4'.t.13
47.05
47.34
48.02
48.1'l
48.72
48.72
48.05
49.89
-8.04
-8.1 I
-8.59
-10.92
-tt.t2
-10.94
-11.98
-1 1.66
-10.74
Averag<31.89 48.r2 -r 0.233
Standard Deviation (Sd'1.547
Aoplicable Source Standard (AS 500
Confdence CoefEcient (CC'I .189
Reladve Accuracv (RAl 2.28 e/o
Performance Reouired - Aoolicable Source Standart RA< 5%
Performance Specilication Methoc PS4
Confidence Coeflicienl CC
cc=lff,sal
where,
h.srs
n
sd
CC
9
L547
tl89
2.306 = degrees offreedom value
= number ofruns selected for calculating the RA
= standard deviation ofdifference: confidence coefficient
Relative Accurrcy, RA
ld l+ lcclRA = 73;;77ix1oo
where,
d -10.23 = average difference of Reference Method and CEMS
CC 1189 = confidence coefficient
AS 500-000 - = applicable source standard, ppmvd @ 0 % O:
RA TI- - relative accuracy, %o
AI =la NOx Summary
Locrdon: MPC-Tesoro - Salt lake City Refinery. UT
Source:
Prolect No.: AST-20254377
Conlidence Coeflicien! CC
cc = lt"3t, sallVn I
where,
\.ns
-!\=
degrees of freedom value
n 9 : number ofruns selected for calculating the RASd 0.667 = standard deviation ofdifference
cC -d.il = con.fi dence coeIfi cient
Reletive Accuracy, RA
ld l+ lcclRA = ..........._x100
where,d -6.11 = average difference of Reference Method and CEMS
CC -6'Jl3 = confidence coefficientRM-314-= reference metho4 ppmvd @ 0 % OuRA 12.43 = relative accuracy, 7o
Run
No.Dete Time Reference Method
NOr Concentrrtion
onmvd @.0 7. Or
CEMS
NOr Concentretion
oomvd@07nOr
Average
IXlference
oomvd@07oO,Strrt End
I
)
3
4
5
6
7
8
9
2126125
2t26t25
2t26t25
2t26t2s
2t26/25
2126125
2t26/25
2t26/25
2126t25
0:30
0:51
l:12
2:00
2:21
2:42
3:30
3:51
4:12
0:50
1:1 1
l:32
2:20
2:41
3:02
3:50
4:lL
4:32
52.84
54.09
53.96
54.39
53.51
52.35
52.47
5t.20
55.02
58.37
60.03
59.83
60.19
59.07
5't.77
59.56
58.1 6
6l .88
-5.53
-5.94
-5.87
-5.80
-5.56
-5.42
-7.09
-6.96
-6.86
Averagt 53.31 s9_43 -5.115
Standard Deviation (Sd)0.667
Confidence Coefficient (CC)0.513
Rehdve Accurecv (RA)12.43./.
Performance Required - Mean Reference Method RA<20Yo
Performance Specification Method PS2
A/t6rtre SO2 Summary
a: : \. I '\L ,-,t )i
Locedon: MPC-Tesoro - Salt l.ake Citv Refincry, UT
Soor"a,
ProJect No.: AST4025-0371
Conlldence Coefflclent CC
aa = lto'It * rollVn I
where,
h.e?5 2.306 = degrees offreedom value
n 9 = number ofruns selected for calculating the RA
sdTIJI-= standard deviation of differenceccT = confidence coefficient
Relrdve Accuncy, RA
ld l+ lcclM = 73;;79 x 1oo
where,
d 2 .7 L = average difference of Reference Method and CEMS
CC 2.934 : confidence coefficicntRM 88.0,14 = reference metho4 ppmvd @0%OzRA 6.4L = relative accuracy, o/o
Run
No.Drte Tlme Reference Method
SOr Conccntredon
oomvd tO 0 7. O,
CEMS
SO' Concentrrdon
nomvd@07oOr
Averege
Difference
oomvd (@ 0 7o OrStrrtEnd
I
,,
3
4
5
6
7
8
9
2t26t25
2126125
2t26t25
2126125
2t26t25
2126t25
2126125
2t26t25
2t26t25
10:30
10:51
I l:12
12:00
L2:21
l2:42
13:30
13:51
l4:12
0:50
l:ll
l:32
2:20
2:41
3:02
3:50
4:ll
4:32
88. l5
86.85
87.33
84.73
87.35
90.08
88.74
92.t4
87.M
78.s 1
80.35
83.22
82.36
84.70
86.76
89.55
94.49
88.04
9.64
6.50
4.1l
2.37
2.65
3.32
-0.81
-2.35
-1.00
Averacc 88.04 85.33 2.7t3
Standard Deviation (Sdl 3.818
Conf dence Coeffi cient (CC)2.934
Reledve Accurrcy (RA)5.41 Y.
Performance Required - Mean Reference Method RA< 20%
Pcrformance Specifi cation Mcthm PS2
AI =ralEE)02 Summary
Locrdon: MPC-Tesoro - Salt [:ke City Refinery, UT
Sourc.,
Project No.: AST -20254377
Conlldence Coeflicient CC
cc = lto'=t r sallVn I
where,
\.sts
-\=
degrees of freedom value
n 9 = number ofruns selectcd for calculating the RA
Sd 0.01 I = staodard dcviation ofdiffcrence
CC 0.008 : confidence coefficient
Reledve Accurecy, RA
ld l+ lcclRA = ;i:;Tr:xloo
where,
d -0.M = average difference of Reference Method and CEMS
CC 0.008 = confidence coefficient
RM.........i.il= reference method, % dry
RA 2.99 = relative tccuracy,Yo
Run
No.Dete Tlme Reference Method
O: Concenhrtion
o/o ilw
CEMS
Or Concentredon
o/o iln
Averrge
Difference
o/o ilwStrrtEnd
I
2
3
4
5
6
7
8
9
2t26t25
2126125
2t26t25
2126125
2t26t25
2126125
2126t25
2t26t2s
2t26t25
10:30
l0:51
I l:12
l2:00
l2,'21
l2:42
l3:30
l3:51
l4:12
10:50
11:11
ll:32
l2:20
L2:41
13:02
13:50
14:11
L4:32
.48
.54
.53
.57
.52
.48
.49
.44
.63
.52
.59
.55
.62
.55
.52
.54
.46
_67
-0.04
-0.05
-0.02
-0.05
-0.03
-0.04
-0.05
-0.02
-0.04
Averagc .52 .56 -0.037
Standard Deviation (Sd)0.011
Confi dence Coeffi cient (CC)0.008
Reletive Accurecy (RA)2.99 Y.
Performance Required - Mean Referqrce Method RA< 20%
Performance Specilication Method PS3
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Runl-RMData
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - f,sdundant Analyzer
Project No.: AST-2025-0377
Dztez 2/26125
Time
Unit
Status
0r - Outlet
o/o dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Averege (Cou,)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
l.s3
11.01
0.06
0.07
0.07
10.91
10.91
10.91
1.48
36.31
50.00
0.23
0.00
0.12
49.94
49.9s
49.9s
36.32
48.24
100.00
0.15
0.31
0.23
98.08
97.98
98.03
49.09
81.05
s00.00
0.73
0.82
0.78
489.18
492.s6
490.87
81.90Corrected Run A
l0:30
l0:31
l0:32
l0:33
l0:34
l0:35
l0:36
l0:37
l0:38
l0:39
l0:40
l0:41
l0:42
l0:43
l0:44
l0:45
l0:46
l0:47
l0:48
l0:49
l0:50
t.67
1.s5
1.45
1.10
1.39
l.6l
l.6s
t.67
1.77
1.80
1.81
1.87
l.8l
1.62
1.43
L30
1.20
1.02
1.24
t.49
1.59
38.34
34.s
37.50
37.58
34.28
34.81
3s.62
36.07
37.32
38. l0
38.30
39.23
39.54
37.02
35.24
33.68
33.91
39.92
32.32
34.40
34.85
50.1 6
48.96
48.21
41.71
46.ts
49.46
s0.1 8
50. l6
51.14
51.77
51.70
52.55
52.t9
49.00
47.30
4s.06
44.50
41.21
44.0t
48.1 1
49.54
78.38
79.98
81.37
94.55
86.08
79.35
77.00
77.26
73.85
73.69
'12.28
7t.68
71.55
76.80
82.38
85.24
89.s5
96.s9
92.04
83.64
78.78
Run2-RMData
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Date:2/26/25
Time
Unit
Status
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
S0r - Outlet
ppmvd
Valid
Uncorrected Run Average (Crur)
CaI Gas Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
1.58
I l.0l
0.06
0.07
0.07
10.91
10.91
10.91
1.54
36.07
50.00
0.23
0.00
0.t2
49.94
49.9s
49.9s
36.07
49.24
100.00
0.l s
0.31
0.23
98.08
97.98
98.03
50.1 I
79.64
500.00
0.73
0.82
0.78
489. I 8
492.s6
490.87
80.4sCorrected Run A
l0:51
l0:52
l0:53
l0:54
l0:55
l0:56
l0:57
l0:58
l0:59
I l:00
I l:01
I l:02
I l:03
I l:04
I l:05
I l:06
I l:07
I l:08
I l:09
I l:10ll:ll
L89
1.98
1.79
1.67
1.47
L4l
1.55
1.63
1.60
1.62
1.62
1.66
1.73
1.86
1.56
1.33
1.35
t.32
t.28
1.38
1.48
37.6s
40.31
38. t4
37.15
34.58
33.82
34.95
36.14
35.73
35.76
35.45
36.66
37.38
38.40
38.88
37.36
3s.1 8
33.51
33.31
33.1 I
33.92
53.01
54.25
52.37
51.13
47.7t
46.90
48.',t3
49.88
49.52
50.12
50.1 I
s0.08
s 1.39
52.53
49.9s
45.08
4s.68
4s.39
45.46
46.s8
48. l6
73.57
69.48
73.00
'75.77
80.99
84.61
80.61
79.78
78.98
76.50
77.23
75.97
74.74
72.76
77.22
86.s8
89.14
88.38
86.84
87.35
82.85
FlaAI Run3-RMData
Locstion: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Dste:2126/25
Time
Unit
Status
Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cy,)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cnr)
Corrected Run A'
Or - Outlet
%o dry
Valid
1.57
I l.0l
0.06
0.07
0.07
10.91
10.91
r0.91
1.53
l.s6
t.62
1.63
1.53
l.s9
1.52
1.45
l.l0
1.20
l.3s
1.57
1.62
1.75
1.77
1.69
1.52
t.52
1.70
t.?t
1.74
1.82
CO - Outlet
ppmvd
Valid
35.91
50.00
0.23
0.00
0.12
49.94
49.9s
49.95
3s.92
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
49.1s
100.00
0.15
0.31
0.23
98.08
97.98
98.03
50.02
80.1 I
s00.00
0.73
0.82
0.78
489. I 8
492.s6
490.87
80.94
ll:12
I l:13
I l:14
I l:15
I l:16
ll:17
l l:18
I l:19
I l:20
ll:21
ll:22
ll:23
ll:24
Il:25
ll:26
ll:27
1 l:28
ll:29
1l:30
I l:31
ll:32
35.1 1
36.78
36.75
36.21
35.13
3s.21
34.93
34.86
37.30
33.88
34.44
35.45
36.48
37.26
36.6s
35.05
34.67
36.80
36.62
37.06
3'1.51
49.01
49.99
49.93
48.s0
49.3s
48.52
48. l3
42.62
43.1 1
46.36
48.91
49.58
s2.06
51.70
st.47
48.70
47.96
50.74
51.15
s 1.63
52.66
82.22
78.82
78.32
79.83
78.84
81.38
82.s0
93.03
92.06
8s.89
81.38
78.12
'73.90
74.s2
75.49
79.30
81.91
78.32
75.28
77.80
73.50
=!aAI Run4-RMData
Location: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: COB Bypass - RedundantAnalyzer
Project No.: AST-2025-0377
Date:2/26125
Time
Unit
Status
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zcro Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Crrr)
Corrected Run A
l2:00
l2:01
l2:02
l2:03
l2:04
l2:05
l2:06
l2:07
l2:08
l2:09
l2:10
l2:ll
l2:12
12:13
l2:14
l2:15
12:16
l2:17
l2:18
l2:19
l2:20
0r - Outlet
%o dry
Valid
I l.0l
0.07
0.06
0.07
10.91
10.91
10.91
1.57
1.68
t.'70
1.79
1.66
1.7 |
1.57
1.49
1.49
1.58
l.s9
1.64
1.62
1.59
1.68
1.69
1.37
1.52
1.65
t.73
1.88
l.3l
CO - Outlet
ppmvd
Valid
34.28
50.00
0.00
0.10
0.0s
49.95
49.91
49.93
34.31
34.04
34.83
3s.97
34.56
35.34
33.98
32.53
32.41
33.32
34.30
33.90
33.70
33.47
34.3s
35.33
32.98
33.34
34.'.l0
35.05
36,77
34.93
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
49.37
100.00
0.31
0.60
0.46
97.98
97.47
97.73
50.29
49.63
50.38
51.69
49.23
50.22
49.03
47.99
47.53
48.36
49.24
50.1 1
49.71
49.16
50.1 3
50.96
4s.56
47.66
50.01
51.06
53.01
46.13
77.45
500.00
0.82
-0.06
0.38
492.56
491.98
492.27
78.35
78.s8
75.78
72.25
7s.74
'16.23
76.25
78.32
79.58
78.56
78.32
76.27
76.71
78.28
75.74
76.57
83.48
82.30
77.9t
74.45
72.89
82.33
AI =tarEE)Run5-RMData
Locetion: MPC-Tesoro - Salt Lake Citv Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Date:2/26/25
Time
Unit
Status
Uncorrected Run Average (Cour)
CaI Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
Or - Outlet
Y" dry
Valid
I l.0l
0.07
0.06
0.07
10.91
10.91
10.91
1.52
CO - Outlet
ppmvd
Valid
34.32
50.00
0.00
0.10
0.05
49.9s
49.91
49.93
34.35
33.38
32.'18
34.1 I
36.45
35.',t7
32.66
33.1 8
33.28
35.03
36.48
36.88
34.15
34.38
34.76
33.22
33.55
32.48
32.01
34.15
36.05
3s.88
NOx - Outlet
ppmvd
Valid
SO, - Outlet
ppmvd
Valid
48.71
100.00
0.31
0.50
0.46
97.98
97.47
9',1.73
49.6r
80.05
500.00
0.82
-0.06
0.38
492.s6
491.98
492.27
80.98
l2:21
l2:22
l2:23
l2:24
l2,,25
l2:26
l2:27
l2.,28
l2:29
l2:30
l2:31
l2:32
l2:33
l2:34
l2:35
l2:36
l2:37
l2:38
l2:39
l2:40
l2:41
1.36
1.55
l.7s
t.7t
r.44
1.48
l.s7
l.6l
l.t5
1.85
l.7s
1.40
l.l8
1.43
1.55
1.57
1.33
1.47
1.67
t.'77
1.67
45.27
48.46
5 l.l5
51.24
46.77
47.43
48.65
49.3t
51.70
52.83
5t.23
46.58
42.97
46.51
48.s6
49.24
45.97
47.31
50.30
51.48
50.00
87.66
81.08
77.33
74.69
82.91
82.86
79.6t
79.36
75.69
73.00
73.29
80.57
89.21
84.65
79.50
79.r4
84.26
83.86
78.04
't5.75
78.57
Run6-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Dstez 2126125
Time
Unit
Status
Or - Outlet
oh ilry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cnr)
t.52
I l.0l
0.07
0.06
0.07
10.91
10.91
10.91
r.48
35.07
s0.00
0.00
0.10
0.05
49.95
49.91
49.93
35.1 I
47.77
100.00
0.31
0.60
0.46
97.98
97.47
97.73
48.65
82.72
500.00
0.82
-0.06
0.38
492.56
491.98
492.27
83.70Corrected Run A
l2:42
l2:43
l2:44
l2:45
l2:46
l2:47
l2:48
l2:49
l2:50
l2:51
l2:52
l2:53
l2:54
l2:55
l2:56
l2:57
l2:58
l2:59
l3:00
l3:01
l3:02
1.70
1.75
t.73
1.79
1.74
1.28
1.34
1.42
1.49
t.74
1.80
1.77
1.62
l.3l
1.32
1.44
l.4l
1.35
l.l6
t.34
1.48
35.2s
3s.76
35.88
36.81
37.01
34.23
37.33
33.7t
34.05
35.00
37.22
37.0t
36.1 s
36.35
31.72
33.37
32.'t9
33.95
36.35
32.91
33.65
49.89
50.90
50.76
51.05
51.03
45.14
45.1 1
46.48
47.75
50.91
5t.s7
51.07
48.99
45.43
44.6s
46.79
45.86
46.10
41.70
44.77
47.27
76.17
75.32
77.12
77.08
74.2s
86.30
89.68
8s.31
83.55
'79.6s
7s.t3
75.93
80.00
86.28
86.59
84.82
85.25
87. l3
93.91
90.91
86.79
RunT-RMData
Location: MPC-Tesoro - Salt Lake CiW Refinery. UT
Source: COB Bwass - Redundant fuialrzer
Project No.: AST-2025-0377
D*e:2/26125
Time
Unit
Status
Uncorrected Run Average (Cou.)
Cal Ges Concentration (Cy,)
Pretest System Zero Response
Posttest System Zero Response
Average Zrro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A Corr
Or - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
33.92
s0.00
0.10
0.20
0.15
49.91
49.38
49.6s
34.12
33.48
32.90
33.t4
34.44
34.60
33.42
34;12
34.26
33.65
34.07
34.73
34.63
3s.06
35.41
35.55
34.71
33.77
33.08
32.83
31.60
32.3s
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
80.98
500.00
-0.05
0.00
-0.03
491.98
490.9s
491.47
82.41
1.53
I l.0l
0.06
0.06
0.06
10.91
10.92
10.92
t.49
47.8r
100.00
0.60
0.63
0.62
97.47
97.50
97.49
48.72
l3:30
l3:3 I
13:32
l3:33
13:34
l3:35
l3:36
13:37
l3:38
l3:39
l3:40
l3:41
13:42
l3:43
13:44
13:45
13:46
13:47
l3:48
13:49
l3:50
1.46
1.43
1.48
1.60
l.s9
1.53
1.56
l.s6
l.s l
1.59
1.72
1.62
t.7l
1.63
1.67
t.s4
1.44
1.44
t.34
1.35
t.37
46.38
46.',|6
46.',|7
48.s0
48.82
48.06
48.t2
48.06
47.44
48.69
50.36
49.34
50.45
49.4s
49.67
48.1 1
46.55
46.2s
45.34
44.92
46.02
82.s2
81.97
83.84
80.64
78.96
79.16
8t.42
80.69
81.92
'19.05
77.21
't8.4s
77.67
77.2r
77.99
77.93
81.82
83.82
85.05
86.08
87.14
AI =raTEE)RunS-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Redundant Analper
Project No. : AST-2025 -037 7
Dilez 2/26125
Time
Unit
Status
Or - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SO: - Outlet
ppmvd
Valid
Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
1.48
I l.0l
0.06
0.06
0.06
10.91
10.92
10.92
1.44
33;10
50.00
0.10
0.20
0.15
49.9t
49.38
49.6s
33.89
46.80
100.00
0.60
0.63
0.62
97.47
97.50
97.49
47.67
84.31
500.00
-0.06
0.00
-0.03
491.98
490.95
491.47
85.80Corrected Run A
l3:51
13:52
l3:53
13 54
l3:55
l3:56
13:57
l3:58
l3:59
14:00
l4:01
l4:02
l4:03
l4:04
l4:05
l4:06
l4:07
l4:08
l4:09
l4:10
l4:1 1
t.3l
1.08
0.99
1.29
1.44
1.55
l.s6
1.61
1.67
1.69
1.68
1.67
1.28
l.l8
1.34
l.4l
1.57
t.s2
1.62
t.72
1.84
31.67
34.46
38.31
30.79
32.82
33.37
33.75
32.71
34.s9
3s.87
35.28
3s.04
34.05
32.53
31.21
31.7 5
33.13
33.45
33.31
34.24
35.27
44.66
41.8s
39.47
43.97
46.28
47.39
48.&
48.23
49.65
49.36
49.40
49.57
44.98
42.10
44.79
4s.99
47.73
48.20
48. l0
50.52
51.87
88.51
93.62
100.61
91.69
86.73
83.01
79.76
8l.56
77.66
79.47
80.29
78.56
86.39
93.80
91.04
86.36
81.60
80.00
79.62
'76.82
73.41
AI =laTEE>Run9-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Redundant Analyzer
Project No.: AST-2025-0377
Date:2/26/25
Time
Unit
Status
Or - Outlet
oh dry
Valid
CO - Outlet
ppmvd
Valid
NOx - Outlet
ppmvd
Valid
SOr - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cnr,r)
Pretest System Zero Response
Posttest System Zero Response
Averege Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
1.67
11.01
0.06
0.06
0.06
10.91
r0.92
r0.92
1.63
3s.88
s0.00
0.10
0.20
0.ls
49.91
49.38
49.6s
36.09
49.84
100.00
0.60
0.63
0.62
97.47
97.84
97.66
50.73
78.92
500.00
-0.06
0.16
0.05
491.98
490.95
49t.47
80.2sCorrected Run A
l4:12
l4:13
l4:14
l4: l5
l4:16
l4:17
l4:18
l4:1 9
l4:20
l4:21
l4..22
l4:23
l4:24
l4:25
l4.,26
l4:2'l
l4,,28
l4.,29
l4:30
l4:31
l4:32
1.96
r.94
t.s9
1.58
1.70
1.66
l.7l
1.80
1.88
t.70
1.84
1.88
t.73
t.46
l.s8
1.64
1.42
l.t4
1.43
1.57
1.83
37.32
38.22
37.16
33.96
35.21
35.1 8
35.97
36.12
37.56
36.93
36.75
37.22
38.67
34.63
34.82
35. l3
34.s9
32.55
35.01
33.75
36.63
53.09
53.02
48.94
47.98
50.36
49.62
50.68
51.54
52.2t
s0.36
51.86
s2.94
51.78
46.79
48.81
49.86
47.60
42.16
46.t3
48.97
st.94
72.21
71.76
78.22
82.33
79.r3
78.84
'17.'75
77.48
73.55
'1s.79
'76.28
73.07
75.89
84.'.|7
82.09
79.21
83.01
93.35
87.38
80.04
75.14
=laAIlEE)CO Summary
MPC-Tesoro - 5x1 rrke Citv Refincrv. UTLocrtion:
Source:
Project No.:
Req€n - Primary Analyzer
LST-2025-0377
Run
No.Dete Time Refcrcnce Method
CO Concentrrdon
nnmvd
CEMS
CO Concentredon
nnmvd
Averrge
Dllference
nnmvdStartEnd
I
)
3
4
5
6
7
8
9
2t25t25
425t25
2125125
2t25t25
2t25t25
2t25t25
2t25125
2t25125
2/25125
l:50
2:ll
2:32
3:30
3:51
4:12
5:05
5:26
5:47
l2:10
l2:11
l2:52
13:50
l4:11
l4:32
l5:25
l5:46
l6:07
19.61
20.32
20.80
22.29
20.3't
20.9'l
20.16
t9.57
t9.67
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
19.61
20.32
20.80
22.29
20.37
20.97
20.16
19.57
t9.67
Averagt 20.42 0.00 20.418
Standard Deviation (Sd'0.864
Applicable Source Standard (AS'44000
Confi dence Coeffi cient (CC'0.664
Reledve Accurecy (BAl 0.048'/.
Performance Reouired - Aoolicable Source Standarc RAS 5%
Performance Specification Methoc PS4
Conlidence Coefficient CC
cc = lto'3t, sallVn I
where,
\3r L306 = degrees of freedom value
n 9 : number ofruns selected for calculating the RA
Sd 0.864 = standard deviation ofdifference
CC-UZ4 = confidence coefEcient
Reladve Accurecy, RA
ld l+ lcclRA = 7s;;Tr' xloo
where,
d 20.42 = average difference of Reference Method and CEMSCC 0.664 = confidence coefficient
As 2666m= applicable source standard, ppmvd
RA 0.05 = relative accuracy, o/o
02 Summary
Locetion: MPC-Tesoro - Salt Lake City Refinerry, UT
Source: Regea - Primary Analyzer
ProJect No.: AST-2025-0377
Confidcnce Coefficlent, CC
cc = lto'It " sally'n I
where,
t6.e75 2.306 = degrees offreedom value
n 9 = number of runs selected for calculating the RA
Sd 0.035 = standard deviation ofdifference
CC 0.027 = confidence coefficient
Rcledve Accurecy, RA
ld l+ lcclM = 7r;;*7ix 1oo
where,d 0.06 _= average differe,nce of Reference Method and CEMSCcffi- = confi dence coefficient
RM -67;-= reference methc/',% dry
RA L2.77 = relative accuracy, o/o
Run
No.Dete Time Reference Method
O, Conccntrrdon
o/" ilrt
CEMS
O, Concentredon
o/o dry
Average
Dlfference
oh dryStert End
1
)
3
4
5
6
7
I
9
2t25t2s
2/25125
2t25t25
2t25t25
2125125
2t25t25
2t25125
2125t25
2125t25
. l:50
.2:Ll
2:32
3:30
3:51
4:12
5:05
.5:26
5:47
2:10
2:31
2:52
3:50
4:11
4:32
5:25
5:46
6:07
0.64
0.70
0.62
0.60
0.77
0.64
0.63
0.66
0.76
0.56
0.63
0.57
0.59
0.74
0.59
0.58
0.60
0.63
0.08
0.07
0.05
0.0r
0.03
0.05
0.05
0.06
0.13
Averace 0.67 0.61 0.059
Standard Deviation (Sd)0.035
Confidence Coefficient (CC)0.027
Rehtive Accuncy @A)12.77'/"
Performance Required - Mean Refereace Method RA< 20%
Performance Specifi cation Method PS3
pulIATEE)CO2 Summary
Locedon: MPC-Tesoro - Salt lake Ciw Refincrv. UT
Sourcc: Rec€n - Primary Analyzer
Project No.: AST-2025-0377
Confidence CoeflIcient, CC
aa = lto'gt r rollVn I
where,
h.er L306 = degrees of freedom value
n 9 = number of runs selected for calculating the RA
Sd-dliil= standard deviation of diffcre,Dce
CC 0.101 = confidence coefficient
Reledve Accurecy, RA
ld I + lcclRA = 73;;;p:x1oo
where,d -0.64 = average difference of Refaence Method and CEMSCC 0.101 - confidence coefficient
RM 16.477 =refcrencemethod,%dryRA 4.47 - relative accuracy, oZ
Run
No.Drte Tlme Refercnce Method
C0: Concentredon
e/. drt
CEMS
C0: Concentredon
t/" ilrv
Averegc
Difference
o/. ilrvStrrtEnd
I
2
3
4
5
6
7
8
9
2t25t25
2t25125
2125125
425t25
2t2St25
2125125
2/2st25
2t25t25
2t25t25
1 1:50
L2:ll
l2:32
13:30
13:51
l4:12
15:05
L5.26
l5:47
l2:1 0
l2:31
l2:52
l3:50
14:ll
l4:32
l5:25
l5:46
l6:0'1
16.45
16.34
16.46
16.68
16.28
16.49
16.56
t6.57
16.47
17.t7
t7.06
17.t9
t7.41
16.96
t7.22
17.1 I
r6.97
16.93
-0.72
-0.72
-0.73
-0.73
-0.68
-0.73
-0.55
-0.40
-0.46
Avcraqt 16.48 t7.l I -0.636
Standard Deviation (Sdl 0.131
Confi dence Coeffi cient (CCl 0.101
Reledve Accurecv (RAl 4.47 V"
Performance Required - Mcan Refcrencc Methoc RA s 20%
Performance Spccification Methoc PS3
ooldoc\E4Gte&F\eEa&tt
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Runl-RMData=larEE)AI
MPC-Tesoro - Salt Lake City Refinery, UTLocation:
Source:
Project No.:
Regen - Primary Analyzer
AST-202s-0377
D*e:2125125
Time
Unit
Status
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
I l:50
I l:51
ll:52
I l:53
I l:54
I l:55
I l:56
I l:57
I l:58
I l:59
l2:00
l2:01
l2:02
l2:03
l2:04
l2:05
l2:06
l2:07
l2:08
l2:09
12:10
16.85
16.93
16.83
16.83
16.83
16.71
16.79
16.8s
t6.8'1
16.8s
16.88
16.94
16.87
16.87
16.88
16.84
16.91
16.80
16.81
16.83
16.73
19.39
s0.00
0.00
-0.12
-0.06
s0.00
49.08
49.s4
19.61
20.12
l9.l
19.33
19.03
18.88
19.85
19.41
19.93
19.s9
19.70
19.63
18.91
18.66
18.82
19.16
19.82
19.96
t9.45
19.51
18.81
19.54
Or - Outlet
%o dry
Valid
0.70
11.00
0.06
0.06
0.06
11.01
10.98
11.00
o.64
0.70
0.64
0.70
0.71
0.72
0.77
0.72
0.69
0.69
0.69
0.68
0.63
0.67
0.6'7
0.66
0.70
0.66
0.72
0.72
0.70
0.76
COr - Outlet
Yo ilry
Valid
16.84
10.90
-0.07
-0.04
-0.06
I l.l5
I l.l3
tt.t4
16.45
CO - Outlet
ppmvd
Valid
Run2-RMData
Location:
Source:
Project No.:
MPC-Tesoro - Salt Lake CiW Refinery, UT
Regen - Primary Analper
AST-2025-0377
Dfiez 2125125
Time
Unit
Status
Or - Outlet
o/o dry
Valid
COr - Outlet
Yo ilry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Averege Cal Response (CM)
0.75
I1.00
0.06
0.06
0.06
I l.0l
10.98
I1.00
0.70
t6.73
10.90
-0.07
-0.04
-0.06
I l.ls
I l.l3
I l.14
16.34
20. l0
50.00
0.00
-0.12
-0.06
s0.00
49.08
49.s4
20.32Corrected Run A
l2:ll
12:12
12:13
12:14
l2:15
l2:16
12:17
l2:1 8
l2:19
l2:20
l2:21
l2:22
l2:23
l2.,24
l2:25
l2:26
l2:27
l2:28
l2:29
l2:30
l2:31
0.73
0.74
0.72
0.76
0.70
0.74
0.6'7
0.69
0.72
0.76
0;79
0.85
0.82
0.78
0.79
0.75
0.'16
0.76
0.77
0.75
0.76
16.77
16.77
16.78
16.74
t6.82
16.76
16.8s
16.83
16.78
t6.70
16.67
16.s6
16.60
16.67
16.66
t6.73
t6.72
t6.72
16.69
16.72
16.73
19.31
20.87
20.08
20.t6
19.61
19.59
19.68
18.81
19.65
19.97
20.66
20.55
20.80
20.00
20.13
20.67
19.88
20.59
20.52
20.49
20.04
FlaAI1EE>Run3-RMData
Location:
Source:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
Regen - Primary Analyzer
AST-202s-0377
Date:2/25/25
Time
Unit
Stetus
Or - Outlet
o/o dry
Valid
COr - Outlet
%" ilry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
0.68
I 1.00
0.06
0.06
0.06
l l.0l
10.98
I1.00
o.62
16.85
10.90
-0.07
-0.04
-0.06
I 1.15
I l.13
I l.14
t6.46
20.58
50.00
0.00
-0.12
-0.06
50.00
49.08
49.s4
20.80Corrected Run A
l2:32
l2:33
l2:34
l2:35
l2:36
l2:37
l2:38
l2:39
l2:40
l2:41
l2:42
l2:.43
l2:44
l2:45
l2:45
l2:47
l2:48
l2:49
l2:50
L2:51
L2:52
0.62
0.s0
0.57
0.70
0.78
0.83
0.88
0.81
0.71
0.69
0.57
0.57
0.58
0.62
0.62
0.66
0.68
0.68
0.75
0.68
0.72
16.94
t7.13
17.02
16.78
16.69
16.59
16.50
16.65
16.81
16.85
17.03
17.04
t7.01
16.9s
t6.94
16.88
16.85
16.83
16.73
16.84
16.76
21.01
28.1 0
20.69
22.32
20.64
20.23
20.9t
20.20
t9.2s
19.24
t9.41
1.t .r1
20.89
18.79
t9.47
18.70
20.38
19.22
20.90
19.96
19.s3
Run4-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Primary Analper
Project No.: AST-2025-0377
Dste:2/25/25
Time
Unit
Status
Or - Outlet
Yo ilry
Valid
COr - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (CMA)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
0.66
r 1.00
0.06
0.06
0.06
10.98
t0.97
10.98
0.60
17.05
10.90
-0.04
-0.03
-0.04
I 1.13
I l.14
I l.14
16.68
2r.92
s0.00
-0.12
0.27
0.08
49.08
49.06
49.07
'r1 10Corrected Run A Corr
l3:30
l3:31
13:32
l3:33
l3:34
13:35
l3:36
13:37
l3:38
l3:39
l3:40
13:41
13:42
13:43
13:44
13:45
13:46
13:47
l3:48
13:49
13:50
0.61
0.64
0.74
0.77
0.76
0.74
0.74
0.69
0.65
0.65
0.56
0.s4
0.55
0.60
0.56
0.70
0.64
0.68
0.68
0.s7
0;t3
17.07
17.08
16.94
16.90
16.94
16.94
t6.97
t7.02
17.08
17.07
17.19
17.22
17.21
17.12
17.18
17.00
17.09
16.99
17.02
t7.16
16.9s
28.04
19.01
19.73
19.59
23.6',1
21.66
r 8.80
21.27
22.89
21.0s
23.67
25.48
24.38
27.28
22.28
t8.62
22.20
21.23
19.s0
22.12
17.83
AI =la Run5-RMData
Locetion:
Source:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
Resen - Primarv Analrrzer
AST-202s-0377
D*ez 2/25125
Time
Unit
Status
Or - Outlet
Yo dry
Valid
COr - Outlet
%o ilry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
0.82
l1.00
0.06
0.06
0.06
10.98
10.97
10.98
0.77
16.65
10.90
-0.04
-0.03
-0.04
I l.l3
I l.l4
I 1.14
16.28
20.04
50.00
-0.12
0.27
0.08
49.08
49.06
49.07
20.37Corrected Run A
13:5 I
13:52
l3:53
13:54
l3:55
l3:56
13:57
l3:58
l3:59
l4:00
l4:01
l4:02
l4:03
l4:04
l4:05
l4:06
l4:07
l4:08
l4:09
l4: l0
l4:ll
0.84
0.88
1.00
1.00
0.78
0.74
0.73
0.74
0.76
0.88
0.89
0.88
0.87
0.90
0.87
0.81
0.81
0.78
0.74
0.69
0.67
t6.77
16.72
16.56
16.57
t6.66
16.72
16.73
16.73
16.'11
16.s0
t6.49
16.49
16.s4
16.46
16.53
t6.66
16.65
16.68
16.76
16.85
16.89
18.38
t9.02
19.4s
20.61
19.36
19.29
19.16
19.06
t9.75
20.55
20.94
2r.34
20.93
21.s9
21.s3
21.26
20.09
20.t9
19.76
19.61
18.94
AI =ratEE)Run6-RMData
Locatlon: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Primary Analyzer
Project No.: AST-2025 -037 7
D*e:2/25125
Time
Unit
Status
Uncorrected Run Averege (Cou)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Averege Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
l4:12
l4:13
l4:14
l4:15
l4:16
l4:17
l4: l8
l4:19
l4.,20
l4:21
l4:22
l4:23
l4:24
l4:25
l4:26
l4:27
l4:28
l4:29
l4:30
l4:31
l4:32
16.89
16.95
16.77
16.73
16.67
16.67
16.6s
16.70
16.80
17.03
17.07
I 7.10
t7.t4
l't.rs
17.08
17.00
16.82
16.69
16.62
16.t6
16.83
20.62
s0.00
-0.12
0.27
0.08
49.08
49.06
49.07
20.97
19.1 6
20.92
19.6s
19.70
20.51
20.48
20.41
20.1 8
20.68
21.39
21.92
19.92
28.38
22.75
20.12
18.57
19.03
19.90
20.3s
19.76
19.23
Or - Outlet
nh dry
Valid
0.69
I1.00
0.06
0.06
0.06
10.98
10.97
10.98
0.64
0.67
0.63
0.73
0.78
0.82
0.81
0.83
0.79
0.74
0.60
0.56
0.54
0.s2
0.s3
0.56
0.61
0.71
0.79
0.83
0.76
0.'11
COr - Outlet
%o dry
Valid
16.86
10.90
-0.04
-0.03
-0.04
I l.l3
I 1.14
I l.14
t6.49
CO - Outlet
ppmvd
Valid
AI =IATEE)RunT-RMData
Location:
Source:
Project No.:
MPC-Tesoro - Salt Lake Citv Refinery. UT
Regen - Primarv Analyzer
AST-202s-0377
D*e:2125/25
Time
Unit
Stetus
Or - Outlet
oh dry
Valid
COr - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zrro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Averege Cal Response (Crrl)
0.68
11.00
0.06
0.06
0.06
10.97
10.98
10.98
0.63
r6.92
10.90
-0.03
-0.04
-0.04
I l.14
l1.l I
I 1.13
16.56
19.89
s0.00
0.27
0.24
0.26
49.06
48.84
48.9s
20.16Corrected Run A
l5:05
l5:06
l5:07
l5:08
l5:09
l5: l0
l5:l I
l5:12
l5:13
15: l4
l5:15
l5: l6
l5:17
l5: l8
l5: l9
l5:20
l5:21
l5:22
l5:23
l5.,24
l5:25
0.58
0.49
0.s2
0.63
0.71
0.53
0.58
0.65
0.80
0.87
0.87
0.86
0.84
0.74
0.69
0.71
0.68
0.59
0.66
0.66
0.6s
17.09
17.23
17.t7
17.00
16.88
17.15
17.08
16.97
16.73
16.63
16.62
16.64
t6.67
16.84
16.91
16.88
16.93
17.10
15.91
16.92
16.96
21.47
2t.24
19.06
t7.77
18.36
22.14
19.58
l9.l I
18.88
19.96
20.07
20.72
20.39
19.50
18.76
19.02
19.84
20.27
20.4s
20.21
20.88
=TAAI RunS-RMData
MPC-Tesoro - Salt Lake Citv Refinerv. UTLocetion:
Source:
Project No.:
Regen - Primary Analtzer
AST-202s-0377
Dste:2/25125
Time
Unit
Status
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
l5:26
l5:27
l5:28
l5:29
l5:30
l5:31
l5:32
l5:33
15:34
l5:35
l5:36
l5:37
l5:38
l5:39
l5:40
l5:41
l5:42
l5:43
l5:44
15:45
l5:46
O: - Outlet
Yo dry
Valid
0.72
I1.00
0.06
0.06
0.06
t0.97
10.98
10.98
0.66
COr - Outlet
Yo dry
Valid
t6.93
10.90
-0.03
-0.04
-0.04
I l.14ll.ll
r6.57
16.9s
16.91
16.89
16.77
16.79
17.02
16.99
17.04
t6.96
16.98
16.96
t6.93
16.79
16,82
16.83
16.93
16.94
17.05
t7.07
16.95
17.01
CO - Outlet
ppmvd
Valid
19.31
50.00
0.27
0.24
0.26
49.06
48.84
48.95
t9.57
o.64
0.67
0.68
0.76
0.74
0.68
o.7t
0.67
0.72
0.71
0.72
0.74
0.84
0.81
0.81
0.74
0.74
0.66
0.6s
0.73
0.69
17.89
18.50
18.97
19.74
t9.96
18.26
18.68
20.76
19.s3
18.88
t9.07
t8.97
18.75
19.27
19.42
19.30
19.72
2t.64
18.36
t9.57
20.29
Run9-RMData=IATEE!AI
MPC-Tesoro - Salt Lake City Refinery, UTLocation:
Source:
Project No.:
Regen - Primarv Anallzer
AST-202s-0377
D*e:2125/25
Time
Unit
Status
Oz - Outlet COr - Outlet CO - Outlet
Yodry Yodry ppmvd
Valid Valid Valid
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cy,)
Pretest System Zcro Response
Posttest System Zero Response
Average Zrcro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
0.82
I1.00
0.06
0.06
0.06
10.97
10.98
10.98
0.76
10.90
-0.03
-0.04
-0.04
I l.14ll.ll
I 1.13
16.47
17.03
16.95
16.90
16.90
16.87
16.77
t6.75
16.73
16.77
16.76
16.85
16.82
16.80
16.9',1
17.01
16.84
16.70
16.62
16.60
16.71
16.96
t9.42
50.00
o.27
0.24
0.26
49.06
48.84
48.9s
t9.67
18.77
19.50
18.79
t8.44
18.54
t9.07
19.31
19.30
t9.2t
19.61
20.s2
t9.96
19.0s
19.07
19.1 3
18.73
19.48
19.84
21.29
20.70
19.41
l5:47
l5:48
l5:49
l5:50
l5:51
l5:52
l5:53
l5:54
l5:55
l5:56
l5:57
l5:58
l5:59
l6:00
l6:01
l6:02
l6:03
l6:04
l6:05
l6:06
l6:07
0.68
o.'73
0.75
0.75
0.77
0.86
0.87
0.88
0.84
0.86
0.79
0.82
0.83
0.74
0.71
0.81
0.91
0.96
0.98
0.90
0.74
CO Summary
Locedon: MPC-Tcsoro - Salt I,ke Ciw Refinerv. UT
Source: Recen - Redundant Analyzer
Project No.:AST-2025-0377
Conlidence Coeflicient CC
cc = lto'3t , sallVn I
where,
h3r L306 = degrees of freedom value
n 9 = number of runs selected for calculating the RASdT981 = standard dwiation of difference
CC 0.754 = confidence coefficient
Reledve Accurecy, RA
ld I + lcclfu{ = !==;1gg
where,d 35.13 : average difference of Reference Method and CEMSCC 0.754 : conlideirce coefficiert
AS 44000.000 : applicable source standard, ppmvd
RA 0.082 = relative aca,sacy,Yo
Run
No.Dete Time Referencc Method
CO Concenhedon
oomvd
CEMS
CO Concentredon
oomvd
Averege
Difference
onmvdStrrtEnd
I
,,
3
4
5
6
7
8
9
2t26t25
2t26t25
2126t25
2126125
2126125
426125
2t26t25
2126125
2126t25
l0:30
l0:51
ll:12
l2:00
l2:21
l2:42
l3:30
13:51
l4:12
10:50
11:11
l1:32
l2:20
l2:41
13:02
l3:50
14:ll
l4:32
36.32
36.07
35.92
34.31
34.35
35.1 I
34.12
33.89
36.09
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
36.32
36.07
35.92
34.31
34.3s
35.1 I
34.12
33.89
36.09
Average 35. l3 0.00 35. I 30
Standard Deviation (Sd 0.981
Aoolicable Source Standard (AS'44000
Confi dence Coeffi cient (CC'0.754
Reledve Accurrcv (RAl 0.0t2 yo
Performance Required - Applicable Sourcc Stasdaft RAS 5%
Performance Spccifi cation Methoc PS4
AI =lalEE)02 Summary
Locrtion: MPC-Tesoro - Salt lake CiW Refinerv, UT
Source: Rccen - Redutrdant AnalYzer
Project No.: AST-2025-0377
Confidence Coefficient, CC
cc = lto'zt , sallVn I
where,
to.srs;|][: degrees of freedom value
n 9 = number ofruns selected for calculating the RA
Sd 0.020 = standard deviation ofdifference
CC 0.016 = confidence coefficient
Reladve Accurecy, RA
ld l+ lcclRA = 73;;7p:x1oo
where,
d 0.02 = average difference of Reference Method and CEMS
CC 0.016 = confidence coefficieirt
RM 1.521 = reference method,% dry
RA 2.25 _= relative accuracy, 7o
Run
No.Dete Time Reference Method
Or Concenhrdon
o/o dw
CEMS
O. Concentretion
o/" ilw
Averrge
Difference
o/o ilryStertEnd
t
2
3
4
5
6
7
8
9
2t26t25
2126125
2126t25
2126t25
2126125
2t26t25
2126125
426t25
2/26125
l0:30
10:51
I 1:12
12:00
L2:21
l2:42
l3:30
13:51
l4:12
0:50
1:1 I
l:32
2:20
2:41
3:02
3:50
4:1 1
4:32
.48
.54
.53
.57
.52
.48
.49
.44
.63
.50
.50
.52
.57
.50
.44
.45
.41
.63
-0.02
0.04
0.01
0.00
0.02
0.04
0.04
0.03
0.00
Averaqe 52 50 0.018
Standard Deviation (Sd)0.020
Confi dence Coefficient (CC)0.016
Reledve Accuncy (RAl 2.25 0/"
Performance Required - Mean Refereirce Mcthod RA < 20%
Performance Speci{ication Methoc PS3
COz Summary
Locedon:
Source:
ProJect No.:
MPC-Tcsoro - Salt
AST
Run
No.Drte Tlme Reference Method
COr Concentrrdor
o/" drv
CEMS
COr Concentrrdon
t/o drt
Avcrege
Difference
Yo trySt.rt End
I
2
3
4
5
6
7
8
9
2t26125
2t26l2s
2t26t25
2t26t2s
2t26t25
2t26t25
2t26t25
2126125
2t26125
0:30
0:51
l:12
2:00
2:21
2:42
3:30
3:51
4:12
0:50
1:ll
1:32
2:20
2:41
3:02
3:50
4:11
4:32
16.47
t6.44
t6.43
16.39
l6.u
16.48
16.45
t6.47
16.33
7.01
7.07
7.t4
7.t9
'7.26
7.27
7.24
1.26
7.10
-0.54
-0.63
-0.'tl
-0.80
-0.82
-0.79
-0.79
-0.'19
-0.77
Avcragc t6.43 7.17 -0.736
Standard Deviation (Sd)0.094
Conf dence Coeffi cient (CC)0.073
Reladve Accurecy (RA)4.92 o/"
Performance Required - Mean Refcr€nce Methoo RA< 20%
Performance Specification Mcthod PS3
Confldence Coefllclent, CC
cc = lto'3t " sallVn I
where,
h.er
-!\=
degrees of freedom value
n 9 : numbs ofnrns selected for calculating the RA
Sd 0.094 : standard deviation ofdifferenceCC 0.073 : confidence coefficient
Relrtive Accurecy, RA
ld l+ lcclRA = 73;;7p:xloo
where,
d
cc
RM
RA
-0.74 = average diffcrcncc of Refercnce Method and CEMS
0.073 = confidence cocfficient
= reference method, % dry
= relative accuracy, oZ4-92
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AI =rarEE)Runl-RMData
Locetion:
Source:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
Regen - Redundant Analyzer
AST-202s-0377
Dile:2/26/25
Time
Unit
Stetus
Or - Outlet
Y" ilry
Valid
1.53
I l.0l
0.06
0.07
0.07
10.91
10.91
10.91
1.48
1.6'7
1.55
t.4s
l. l0
1.39
l.6l
1.6s
1.67
1.77
1.80
l.8l
1.87
l.8l
t.62
1.43
1.30
1.20
t.02
1.24
1.49
l.s9
COr - Outlet
Yo dry
Valid
t6.71
10.92
-0.06
-0.07
-0.07
I 1.07
ll.M
1 1.06
t6.47
CO - Outlet
ppmvd
Valid
36.31
50.00
0.23
0.00
0.12
49.94
49.9s
49.9s
36.32
Uncorrected Run Average (Cou.)
Cal Gas Concentration (Cy,j
Pretest System Zoro Response
Posttest System Zero Response
Averege Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
l0:30
l0:31
l0:32
l0:33
l0:34
10:35
10:36
l0:37
10:38
l0:39
l0:40
l0:41
l0:42
l0:43
l0:44
10:45
l0:46
l0:47
l0:48
l0:49
l0:50
16.61
16.69
16.7s
17.05
16.80
16.64
16.60
16.61
16.51
16.s0
16.48
t6.43
16.48
t6.64
16.79
16.90
16.98
17. l3
16.93
16.74
16.64
38.34
34.5
37.50
37.58
34.28
34.81
35.62
36.07
37.32
38. l0
38.30
39.23
39.54
37.02
3s.24
33.68
33.91
39.92
32.32
34.40
34.8s
=raAI Run2-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Redundant Analyzer
Project No.: AST-2025-0377
Dste:2126125
Time
Unit
Stetus
Uncorrected Run Average (Cou.)
Cal Gas Concentration (Cya)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
Corrected Run A
l0:51
l0:52
l0:53
l0:54
l0:55
l0:56
l0:57
l0:58
l0:59
I l:00
11:01
ll:02
I l:03
I l:04
I l:05
I l:06
I l:07
I l:08
I l:09
I l:10ll:ll
Or - Outlet
Yo ilry
Valid
1.58
11.01
0.06
0.07
0.07
10.91
10.91
10.91
t.s4
COr - Outlet
o/o dry
Valid
t6.67
10.92
-0.06
-0.07
-0.07
I 1.07
1l.M
I 1.06
t6.44
CO - Outlet
ppmvd
Valid
36.07
s0.00
0.23
0.00
0.12
49.94
49.9s
49.95
36.07
37.6s
40.31
38.14
37.15
34.s8
33.82
34.9s
36.14
35.73
35.76
3s.45
36.66
37.38
38.40
38.88
37.36
35.1 8
33.51
33.31
33.1 1
33.92
1.89
1.98
t.79
t.67
t.47
l.4l
1.ss
1.63
1.60
1.62
t.62
1.66
t.73
r.86
1.56
1.33
1.3 5
1.32
1.28
1.38
1.48
16.41
16.36
16.50
16.58
t6.75
16.82
16.70
16.64
16.65
16.65
16.63
16.61
16.55
t6.4s
t6.70
t6.87
16.88
16.89
16.91
16.83
16.77
=TAAIlEe7:
Run3-RMData
Location: MPC-Tesoro - Salt Lake CiW Refinery, UT
Source: Regen - Redundant Anallzer
Project No.: AST-2025-0377
Datez 2126125
Time
Unit
Status
O: - Outlet
Y" ilry
Valid
1.57
11.01
0.06
0.07
0.07
10.91
10.91
10.91
l.53
l.s6
t.62
1.63
l.s3
1.59
1.52
t.4s
l.l0
1.20
1.35
1.57
1.62
l.7s
1.77
1.69
1.52
t.s2
1.70
t.7L
t.74
1.82
COr - Outlet
o/n dry
Valid
16.67
10.92
-0.06
-0.07
-0.07
I 1.07
I1.04
I 1.06
15.43
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou,)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zrro Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
35.91
50.00
0.23
0.00
0.12
49.94
49.9s
49.9s
3s.92
I l:12
I l:13
I 1:14
I l:15
I l:16
I l:17
I 1:18
I l:19
I l:20
ll:21
ll:22
ll:23
ll:24
ll:25
ll:26
ll:27
I l:28
ll:29
I l:30
I l:31
ll:32
16.68
16.64
16.63
16.7t
16.67
16.72
16.78
17.04
16.97
16.85
16.67
16.63
16.52
15.49
16.57
16.70
16.69
16.55
16.s6
16.53
16.46
35.1 I
36.78
36.75
36.21
35.1 3
35.21
34.93
34.86
37.30
33.88
34.44
35.4s
36.48
37.26
36.6s
35.05
34.67
36.80
36.62
37.06
37.51
pylI6r1EE)
L i i fl i) i. .
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Run4-RMData
Source: Regen - Redundant Analyzer
Project No.: AST-2025-0377
D*ez 2126125
Time
Unit
Stetus
Or - Outlet
oh dry
Valid
1.62
I l.0l
0.07
0.06
0.07
10.91
10.91
10.91
1.57
1.68
1.70
1.79
1.66
t.?l
1.57
1.49
1.49
1.58
1.59
t.64
r.62
1.s9
1.68
1.69
1.37
1.52
1.65
1.73
1.88
l.3l
COr - Outlet
o/" dry
Valid
16.s9
10.92
-0.07
-0.0r
-0.04
11.04
I1.04
I1.04
16.39
CO - Outlet
ppmvd
Valid
34.28
s0.00
0.00
0.10
0.05
49.9s
49.91
49.93
34.31
34.04
34.83
35.97
34.56
3s.34
33.98
32.53
32.41
33.32
34.30
33.90
33.70
33.47
34.35
3s.33
32.98
33.34
34.70
35.0s
36.77
34.93
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Z,ero Response (Co)
Pretest System Cel Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run Averase (Corr
l2:00
l2:01
l2:02
l2:03
l2:04
l2:05
l2:06
l2:07
l2:08
l2:09
l2:10
l2:ll
12:12
l2:13
l2:14
l2:15
12:16
12:17
12:18
12:19
l2:20
16.54
16.54
16.45
16.55
t6.52
16.65
16.68
t6.6'1
16.63
16.61
16.57
16.s9
16.61
16.55
16.55
16,'79
16.68
16.55
16.51
16.38
t6.87
=TAAI Run5-RMData
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Redundnnt Analrrzer
Project No.: AST-2025-0377
D*e:2126/25
Time
Unit
Status
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cyj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
%o ilry
Valid
l.s6
I l.0l
0.07
0.06
0.07
10.91
10.91
10.91
t.s2
1.36
1.55
1.75
l.7l
t.44
1.48
1.57
l.6l
1.75
1.85
t.7s
1.40
l.l8
1.43
l.5s
l.s7
1.33
1.47
1.67
t.'t7
1.67
COr - Outlet
Yo dry
Valid
16.64
10.92
-0.07
-0.01
-0.04
ll.M
I1.04
I1.04
16.44
CO - Outlet
ppmvd
Valid
34.32
s0.00
0.00
0.10
0.0s
49.95
49.91
49.93
34.3s
33.38
32.78
34.11
36.45
3s.77
32.66
33.1 8
33.28
3s.03
36.48
36.88
34.1 s
34.38
34.76
33.22
33.55
32.48
32.0t
34.15
36.05
3s.88
12:21
l2:22
l2:23
l2:24
l2:25
l2:26
l2:27
l2:28
l2:29
l2:30
12:31
l2:32
l2:33
l2:34
l2:35
l2:36
l2:37
I2:38
L2:39
l2:40
l2:41
16.79
16.66
16.47
16.53
16.74
16.70
16.64
16.60
16.50
16.40
16.51
16.78
16.9s
16.75
16.64
16.64
16.8s
16.73
t6.54
16.47
16.55
=raAI Run6-RMData
MPC-Tesoro - Salt Lake City Refinery. UTLocetion:
Source:
Project No.:
Regen - Redundant Analyzer
AST-2025-0377
Dfie:2126125
Time
Unit
Status
Uncorrected Run Average (Cour)
Cal Gas Concentration (Cpj
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run Avera
Or - Outlet
oh dry
Valid
t.52
I l.0l
0.07
0.06
0.07
10.9t
10.91
10.91
1.48
COr - Outlet
Vo dry
Valid
16.68
t0.92
-0.07
-0.01
-0.04
ll.M
11.04
I1.04
16.48
CO - Outlet
ppmvd
Valid
35.07
50.00
0.00
0.10
0.05
49.9s
49.91
49.93
35.1 1
l2:42
L2:43
l2:44
l2:45
l2:46
l2:47
l2:48
l2:49
l2:50
l2:51
l2:52
l2:53
l2:54
l2:55
12:56
l2:57
l2:58
l2:59
l3:00
l3:01
13:02
1.70
l.7s
1.73
1.79
1.74
1.28
1.34
1.42
1.49
1.74
1.80
1.77
1.62
1.3 I
1.32
1.44
l.4l
1.3s
t.l6
t.34
1.48
16.54
16.49
16.s3
t6.47
16.53
16.89
16.82
16.77
16.70
16.51
16.46
t6.49
16.61
16.88
16.84
t6.74
16.77
16.83
16.96
16.82
16.72
35.25
35.76
3s.88
36.81
37.01
34.23
37.33
33.71
34.05
35.00
37.22
37.01
36.1 5
36.35
31.72
33.37
32.79
33.95
36.3s
32.9t
33.65
AI =TA IEE)Run7-RMData
Location:
Source:
Project No.:
MPC-Tesoro - Salt Lake City Refinery, UT
Regen - Redundant Analwer
AST-2025-03'17
Datez 2126/25
Time
Unit
Status
O: - Outlet
Vo dry
Valid
COr - Outlet
Yo dry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cy,j
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
l.s3
I l.0l
0.06
0.06
0.06
10.91
r0.92
t0.92
1.49
16.68
10.92
-0.01
-0.03
-0.02
ll.M
u.09
I 1.07
16.45
33.92
50.00
0.10
0.20
0.15
49.91
49.38
49.6s
34.12Corrected Run A
l3:30
13:31
13:32
l3:33
13:34
l3:35
l3:36
13:37
13:38
l3:39
l3:40
l3:41
13:42
13:43
13:44
13:45
13:46
13:47
13:48
l3:49
13:50
1.46
1.43
1.48
1.60
l.s9
1.53
1.56
1.56
l.5l
Ls9
1.72
1.62
1.7 |
1.63
1.67
1.54
t.44
1.44
1.34
1.35
r.37
16.72
16.75
16.69
16.63
16.64
16.67
16.64
16.64
16.71
16.65
16.53
16.61
t6.54
16.61
16.57
16.68
16.75
t6.76
16.8s
16.83
16.81
33.48
32.90
33. l4
34.44
34.60
33.42
34.72
34.26
33.6s
34.07
34.73
34.63
35.06
3s.41
35.55
34.71
33.77
33.08
32.83
31.60
32.35
=TAAI RunS-RMData
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Redundant Analyzer
Project No.: AST-2025-0377
Dstez 2/26/25
Time
Unit
Status
Uncorrected Run Average (Cou)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (CM)
Corrected Run A
Or - Outlet
Vo llry
Valid
COr - Outlet
oh dry
Valid
t6.70
10.92
-0.01
-0.03
-0.02
ll.M
I1.09
I 1.07
16.47
CO - Outlet
ppmvd
Valid
1.48
I t.0l
0.06
0.06
0.06
10.91
10.92
t0.92
1.44
l.3l
1.08
0.99
1.29
1.44
1.55
l.s6
1.61
1.67
1.69
1.68
1.67
1.28
l.l8
1.34
1.41
1.57
t.s2
1.62
132
1.84
33.70
50.00
0.10
0.20
0.15
49.91
49.38
49.65
33.89
13:5 I
13:52
l3:53
13:54
l3:55
l3:56
13:57
l3:58
l3:59
l4:00
l4:01
l4:02
l4:03
l4:04
14:05
14:06
l4:07
l4:08
l4:09
l4:10
l4:l I
16.86
17.03
17.08
16.87
16.72
16.64
16.65
16.58
16.54
16.53
16.s3
16.5s
16.86
16.93
16.80
16.74
16.61
16.67
16.59
16.52
16.41
31.67
34.46
38.31
30.79
32.82
33.37
33.7s
32.71
34.s9
35.87
35.28
3s.04
34.05
32.s3
3t.21
3t.75
33.1 3
33.45
33.31
34.24
35.2',7
Run9-RMData
Location: MPC-Tesoro - Salt Lake CiE Refinery, UT
Source: Regen - Redundant Analyzer
Project No.: AST-2025-0377
D*e:2/26/25
Time
Unit
Status
O: - Outlet
Yo ilry
Valid
COr - Outlet
o/o dry
Valid
CO - Outlet
ppmvd
Valid
Uncorrected Run Averege (Cour)
Cal Gas Concentration (Cy,1)
Pretest System Zero Response
Posttest System Zero Response
Average Zero Response (Co)
Pretest System Cal Response
Posttest System Cal Response
Average Cal Response (Cu)
1.67
I l.0l
0.06
0.06
0.06
10.91
r0.92
r0.92
L63
16.56
r0.92
-0.01
-0.03
-0.02
I1.04
I 1.09
I1.07
16.33
35.88
50.00
0.r0
0.20
0.15
49.91
49.38
49.65
36.09Corrected Run A
l4:12
l4: l3
l4:14
l4: l5
l4: l6
l4:17
l4: l8
l4:19
l4:20
l4:21
l4:22
l4:23
l4:24
l4:25
l4:26
l4:27
l4:28
l4:29
l4:30
l4:31
l4:32
1.96
1.94
1.59
l.s8
1.70
r.66
t.7t
1.80
1.88
1.70
1.84
1.88
t.73
1.46
l.s8
t.64
1.42
l.14
1.43
1.57
1.83
16.29
16.32
16.62
16.62
16.s2
16.54
16.52
16.44
16.37
16.s3
16.42
16.39
16.50
16.72
16.64
16.60
16.78
16.98
16.77
16.6s
16.44
37.32
38.22
37.t6
33.96
3s.21
35.1 8
35.97
36.12
37.56
36.93
36.'ts
37.22
38.67
34.63
34.82
3s.1 3
34.59
32.55
35.01
33.75
36.63
AI =lalEE)QA Data
Location MPC-Tesoro - Salt Lake City Refinery, UT
Sorr..
Project No. AST-2025-0377
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Make
Model
S/N
Ooeretins Ranse
Servomex
4900
r00269
25
Thermo
48i
JC1314100812
200
Thermo
42iQ
12327'.l30s2t
200
Ametek
9900
m-9900-sl202-l
2000
Cylinder ID
7*ro
Low
Mid
Hieh
NA
NA
RR02538
E80069884
NA
NA
cc721736
cc721736
NA
NA
EB00l 1606
EB001 1606
NA
NA
EB0039876
EB0039876
Cylinder Certified Values
7*ro
Low
Mid
Hish
NA
NA
ll
23.99
NA
NA
519
sl9
NA
NA
501
501
NA
NA
5000
5000
Cylinder Expiration Date
Z*ro
Low
Mid
Hish
NA
NA
9n9t31
4fi132
NA
NA
21912',1
2/9127
NA
NA
9lt613t
9/t6t3t
NA
NA
612',1129
6/27129
Tvpe of Samnle Line Heated Sample Line
pl/l6rrrcE)
TE(--ll l.i lLl r, L 1-lt]r [] rl
Location: MPC-Tesoro - Salt Iake City Refinery, UT
Source: COB Brrpass - Primary Analper
Project No.: AST-2025-0377
Response Times
seconds
Paremeter O: - Outlet CO - Outlet NOr - Outlet SO: - Outlet
Zero
Low
Mid
Averege
60
NA
60
60
NA
60
t20
NA
120
180
NA
180
60.0 60.0 120.0 180.0
A/l6rrEE)r; t,li. i .1 , f- :'
Calibration Data
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Bypass - Primary Analyzer
Project No.: AST-2025-0377
Dile:2125125
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Exnected Average Concentration 2.00 50.00 50.00 s00.00
Span Between
Low
High
Desired Soan
2.00
20.00
23.99
50.00
250.00
100.00
50.00
2s0.00
200.00
s00.00
2s00.00
1000.00
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
9.60
14.39
40.00
60.00
80.00
120.00
400.00
600.00
High Range Gas
Low
Hieh
NA
NA
NA
NA
NA
NA
NA
NA
Actual Concentration(Yo or ppm)
7*ro
Low
Mid
Hish
0.00
NA
I 1.00
23.99
0.00
NA
s0.00
100.00
0.00
NA
100.00
200.00
0.00
NA
s00.00
1000.00
ResDonse Time (seconds)60.00 60.00 120.00 180.00
Upscele Calibration Gas (Cur)Mid Mid Mid Mid
lnstrument Response (7o or ppm)
7*ro
Low
Mid
Hieh
0.00
NA
I l.0l
24.00
0.00
NA
s0.00
100.00
0.06
NA
100.24
200.12
0.04
NA
s02.22
999.17
Performance (7o of Span or Cal. Gas Conc.)
Z,ero
Low
Mid
Hish
0.00
NA
0.04
0.04
0.00
NA
0.00
0.00
0.03
NA
o.t2
0.06
0.00
NA
0.22
0.08
Status
Z.aro
Low
Mid
Hiph
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
=r€rAI Bias/Drift DeterminationslEE)
MPC-Tesoro - Salt Lake City Refinery, UTLocation:
Source:
Project No.:
COB Bypass - Primary Analrrzer
AST-2025-0377
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.06
I l.0l
10.98
0.00
-0.12
s0.00
49.08
0.55
0.31
97.75
98.02
0.50
0.36
490.41
490.42
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.06
0.06
I t.0l
10.98
0.00
-0.12
50.00
49.08
0.55
0.31
97.75
98.02
0.50
0.36
490.41
490.42
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
0.06
0.06
I l.0l
10.98
0.00
-0.12
50.00
49.08
0.55
0.31
97.75
98.02
0.50
0.36
490.4r
490.42
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.98
10.97
-0.r2
0.27
49.08
49.06
0.31
0.64
98.02
97.95
0.36
0.15
490.42
490.68
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.06
10.98
10.97
-0.12
0.27
49.08
49.06
0.31
0.64
98.02
97.95
0.36
0.15
490.42
490.68
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posffest Svstem Uoscale Resoonse
0.06
0.06
10.98
10.97
-0.12
0.2't
49.08
49.06
0.31
0.64
98.02
97.9s
0.36
0.15
490.42
490.68
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale ResDonse
0.06
0.06
10.97
10.98
0.27
0.24
49.06
48.84
0.64
0.34
97.95
97.99
0.15
0.29
490.68
490.49
Run 8
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.06
0.06
10.97
10.98
0.27
0.24
49.06
48.84
0.64
0.34
97.95
97.99
0. ls
0.29
490.68
490.49
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.06
10.97
10.98
0.27
0.24
49.06
48.84
0.64
0.34
97.9s
97.99
0.15
0.29
490.68
490.49
AI =lalEe
. []
Bias/Drift Determinations
Locadon: MPC-Tesoro - Salt Lake Ciw Rcfinery. UT
Source: COB Bypass - Primary Analrzer
Project No.: AST-2025-0377
Prremeter 0r - Outlet CO - Outlet NOr - Outlet SO: - Outlet
Run 1 Dete 2l2SnS
Span Value
lnitial Instrument Zero Cal Response
nitial Instrument Upscale Cal Response
iinal Instnunent Zero Cal Response
iinal lnstument Upscale Cal Respoilie
ketest System Zero Response
losttest System Zero Response
lretest System Upscale Response
)osttest Svsim I Jnscele R*mnse
23.99
0.00
I l.0l
0.00
ll.0l
0.06
0.06
I l.0l
10.98
100.00
0.00
50.00
0.00
50.00
0.00
-0.12
50.00
49.08
200.00
0.06
100.24
0.06
100.24
0.55
0.31
91.75
98.02
1,000.00
0.04
502.22
0.04
502.22
0.50
0.36
490.41
490.42
3ias (%)
Jretest Zero
Posttest Zero
lretest Span
?osttest Soan
0.25
0.25
0.00
-0.13
0.00
-0.12
0.00
-0.92
0.25
0.13
-t.25
-1.11
0.05
0.03
-1.18
-1.18
)rift (%)
Zero
\fi.t
0.00
-0.13
-0.t2
-0.92
-0.12
0.13
-0.01
0.00
Run 2 Date 2l25ns
Jpan Value
hstnrment Zero Cal Response
hstnrment Upscale Cal Response
linal lnstrument Zer o Cal Response
linal lnstrument Upscale Cal Response
lretest System Zero Response
losttest System Zero Response
lretest System Upscale Response
)osttest Svstem Unscale Resnonse
23.99
0.00
I 1.01
0.00
I 1.01
0.06
0.06
11.01
10.98
100.00
0.00
50.00
0.00
50.00
0.00
-0.12
50.00
49.08
200.00
0.06
100.24
0.06
r00.24
0.55
0.31
97.75
98.02
1,000.00
0.04
502.22
0.04
s02.22
0.50
0.36
490.41
490.42
lias (%)
lretest Zero
losttest Zero
lretest Span
)osttest Snan
0.25
0.25
0.00
-0. l3
0.00
-0.12
0.00
-0.92
0.25
0.13
-t.25
-1.11
0.05
0.03
- 1.18
- 1.18
)rift (%)
Zsro
V[i.{
0.00
-0. l3
-0.12
-0.92
-0.t2
0. l3
-0.01
0.00
Run 3 Datc 2125125
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final InstrumentZero Cal Response
Final lnstument Upscale Cal Response
Pretest Systern Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
I l.0t
0.00
I 1.01
0.06
0.06
11.01
10.98
100.00
0.00
50.00
0.00
50.00
0.00
-0. l2
50.00
49.08
200.00
0.06
100.24
0.06
t00.24
0.55
0.31
97.75
98.02
1,000.00
0.04
502.22
0.04
502.22
0.50
0.35
490.41
490.42
Bias (%)
Praest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.2s
0.00
-0.13
0.00
-0.12
0.00
-0.92
0.25
0.13
-t.25
-1.11
0.05
0.03
-1.1 8
-1.18
Drift (%)
Zero
Mid
0.00
-0.13
-0.t2
-0.92
-0.12
0.13
-0.01
0.00
Bias/Drift Determinations
Location:
Source:
Project No.:AST-2025-0317
MPC-Tcsoro - Salt Lake City Refrnery, UT
COB Bypass - Primary Analyzer
Peremeter O' - Outlet CO - Outlet NOr - Outlet SOr - Outlet
Run 4 Dete 2125125
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstrument Zero Cal Response
Final Instnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
11.01
0.00
I l.0l
0.06
0.06
10.98
10.97
100.00
0.00
50.00
0.00
50.00
-0.12
0.27
49.08
49.06
200.00
0.06
100.24
0.06
100.24
0.31
0.64
98.02
91.9s
1,000.00
0.04
502.22
0.04
502.22
0.35
0.15
490.42
490.68
Bias (%)
Pretest Zero
Posttest Zero
Praest Span
Posttest Soan
0.25
0.25
0.13
0.17
0.r2
0.27
0.92
0.94
0.13
0.29
l.l I
1.15
0.03
0.01
1.18
l. 15
Drift (%)
Zero
Mid
0.00
-0.04
0.39
-0.02
0.17
-0.03
-0.02
0.03
Run 5 Date 2l25ns
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstrumentZqo Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Sysrcm Upscale Response
23.99
0.00
11.01
0.00
I l.0l
0.05
0.06
10.98
10.97
100.00
0.00
50.00
0.00
50.00
-0.12
0.27
49.08
49.06
200.00
0.06
t00.24
0.06
100.24
0.31
0.64
98.02
97.95
1,000.00
0.M
502.22
0.M
s02.22
0.36
0.15
490.42
490.68
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.13
0.17
0. t2
0.2't
0.92
0.94
0.13
0.29
LlI
1.15
0.03
0.01
1 .18
1.15
Drift(%)
Zerc
Mid
0.00
-0.04
0.39
-0.02
0.t7
-0.03
-0.02
0.03
Run 6 Dete 2l25l2s
Span Value
lnstrument Zero Cal Response
lnstnrment Upscale Cal Response
Final lnstument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
11.01
0.00
11.01
0.06
0.06
10.98
10.97
100.00
0.00
50.00
0.00
50.00
-0.12
0.27
49.08
49.06
200.00
0.06
100.24
0.06
100.24
0.31
0.64
98.02
97.95
1,000.00
0.04
s02.22
0.M
502.22
0.36
0. l5
490.42
490.58
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.2s
0.13
0.17
0. l2
0.27
0.92
0.94
0. l3
0.29
l.l I
1.15
0.03
0.01
l.l8
l.l5
Drift(%)
Zerc
Mid
0.00
-0.M
0.39
-0.02
0.17
-0.03
-0.02
0.03
pua6rrce
'i..: Ii'{ri..\:. ;f- :
Bias/Drift Determinations
Locedon: MPC-Tesoro - Salt Lakc City Refinery, UT
Source: COB Bwass - Primarv Analwer
Project No.: AST-2025-0377
Prrrmeter O, - Outlet CO - Outlet NOr - Outlet SOr - Outlet
Run 7 Dete 2l25ns
Span Value
Instrum€nt Zero Cal Response
Instnrment Upscale Cal Response
Final Instrument Zero Cal Response
Final lnstnrment Upscale Cal Response
Pret€st System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
23.99
0.00
11.01
0.00
I l.0l
0.06
0.06
10.97
10.98
100.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48.84
200.00
0.06
100.24
0.06
100.24
0.64
0.34
97.95
97.99
1,000.00
0.04
502.22
0.04
502.22
0.15
0.29
490.58
490.49
Bias (%)
Pretest Zero
Posttest Zero
Praest Span
Posttest Span
0.25
0.25
0.t7
0.13
0.27
0.24
0.94
1.16
0.29
0. l4
l.l5
l.l3
0.01
0.03
1. t5
t.t7
Drift (%)
Zero
Mid
0.00
0.04
-0.03
-0.22
-0.15
0.02
0.01
-0.02
Run E Drte 2125125
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final lnstrument Zqo Cal Response
Final Instument Upscale Cal Response
Praest Systern Zero Response
Posttest Systcm Zcro Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
11.01
0.00
11.01
0.06
0.05
t0.97
10.98
100.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48.84
200.00
0.06
100.24
0.06
100.24
0.64
0.34
97.95
97.99
1,000.00
0.04
502.22
0.04
502.22
0.15
0.29
490.68
490.49
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.17
0.l3
0.27
0.24
0.94
1.16
0.29
0.14
l.l5
1.13
0.01
0.03
1.15
t.t7
Drift(%)
Zero
Mid
0.00
0.04
-0.03
-0.22
-0.15
0.02
0.01
-0.02
Run 9 Dgte A25ns
Span Value
Instnrment Zero Cal Response
Instument Upscale Cal Response
Final lnstrument Zero Cal Response
Final lnstnrment Upscale Cal Response
Pretest System Zero Response
Postt€st System Zero Response
Pretest System Upscale Response
Posttest Svstcm Uoscale Response
23.99
0.00
11.01
0.00
I 1.01
0.06
0.06
10.97
10.98
100.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48.84
200.00
0.06
t00.24
0.06
100.24
0.64
0.34
97.95
97.99
1,000.00
0.04
502.22
0.04
502.22
0.15
0.29
490.68
490.49
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.2s
0.25
0.17
0.13
0.27
0.24
0.94
1.16
0.29
0.14
1.15
l.l3
0.01
0.03
l.1s
t.t7
Drift (%)
Zerc
!tid
0.00
0.04
-0.03
-0.22
-0.15
0.02
0.01
-0.02
AI FIATEE)QA Data
Locetion MPC-Tesoro - Salt Lake CiW Refinery. UT
Source COB Brpass - Redundant Analper
Project No. AST-2025-0377
Parameter Or - Outlet CO - Outlet NOx - Outlet SO' - Outlet
Make
Model
s/t{
Ooeratins Ranse
Servomex
4900
100269
25
Thermo
48i
JC1314l008l2
200
Thermo
42iQ
t232773052t
200
Ametek
9900
zD-9900-s1202-1
2000
Cylinder II)
7*ro
Low
Mid
Hiph
NA
NA
RR02538
EB0069884
NA
NA
cc721736
cc721736
NA
NA
EB00l 1606
EB00l 1606
NA
NA
EB0039876
EB0039876
Cylinder Certified Values
Zero
Low
Mid
Hish
NA
NAll
23.99
NA
NA
5t9
519
NA
NA
501
501
NA
NA
5000
5000
Cylinder Expiration Date
Zaro
Low
Mid
Hish
NA
NA
9n9/31
4/,/32
NA
NA
2t9t27
2t9127
NA
NA
9tr6t31
9lt6/31
NA
NA
6t27/29
6t27/29
fype of Ssmple Line Heated Sample Line
puIATEE)
T f (.1 lll'l l(l ,.\ L (', R..r li l-'
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Response Times
Source: COB Bypass - Redundant Analper
Project No.: AST-2025-0377
7*ro
Low
Mid
60
NA
::
60
NA
::
Calibration Data
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: COB Brmass - Redundant Analwer
Project No.: AST-2025-0377
D*e:2126125
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Exoected Averase Concentration 5.00 50.00 50.00 200.00
Spen Between
Low
High
Desired Span
5.00
2s.00
23.99
s0.00
2s0.00
100.00
s0.00
2s0.00
200.00
200.00
1000.00
1000.00
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hioh
9.60
14.39
40.00
60.00
80.00
120.00
400.00
600.00
lligh Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
NA
NA
Actual Concentration (7o or ppm)
7*ro
Low
Mid
Hish
0.00
NA
I t.0l
23.99
0.00
NA
50.00
100.00
0.00
NA
r00.00
200.00
0.00
NA
500.00
1000.00
Resoonse Time (seconds)60.00 60.00 60.00 180.00
Upscale Calibratlon Gas (C^r^)Mid Mid Mid Mid
Instrument Response (% or ppm)
Z,ero
Low
Mid
Hieh
0.00
NA
10.99
24.00
0.01
NA
49.99
100.00
0.00
NA
99.90
200. l 0
0.00
NA
498.97
997.s8
Performance (7o of Span or Cal. Gas Conc.)
Zero
Low
Mid
Hish
0.00
NA
0.08
0.04
0.01
NA
0.01
0.00
0.00
NA
0.0s
0.0s
0.00
NA
0.10
0.24
Status
Z,efO
Low
Mid
Hish
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
A/l6rrEE)Bias/Drift Determinations
Location: MPC-Tesoro - Salt Lake Citv Refinery, UT
Source: COB Broass - Redundant Analyzer
Project No.: AST-2025-0377
Parameter Or - Outlet CO - Outlet NOx - Outlet SOr - Outlet
Run 1
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.07
10.91
10.91
0.23
0.00
49.94
49.95
0.15
0.31
98.08
97.98
0.73
0.82
489.1 8
492.s6
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Resoonse
0.06
0.07
10.91
10.91
0.23
0.00
49.94
49.9s
0. l5
0.31
98.08
97.98
0.73
0.82
489. l 8
492.s6
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.07
10.91
10.91
0.23
0.00
49.94
49.9s
0.15
0.31
98.08
97.98
0.73
0.82
489. l 8
492.s6
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.07
0.06
10.91
10.91
0.00
0.10
49.9s
49.91
0.31
0.60
97.98
97.4',t
0.82
-0.06
492.s6
491.98
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale ResDonse
0.07
0.06
10.91
10.91
0.00
0. l0
49.95
49.9r
0.31
0.60
97.98
97.47
0.82
-0.06
492.s6
491.98
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.07
0.06
10.91
10.91
0.00
0.10
49.95
49.9t
0.31
0.60
97.98
97.47
0.82
-0.06
492.s6
491.98
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.91
10.92
0.10
0.20
49.91
49.38
0.60
0.63
97.47
97.50
-0.06
0.00
491.98
490.9s
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale ResDonse
0.05
0.06
10.91
t0.92
0.10
0.20
49.9t
49.38
0.60
0.63
97.47
97.s0
-0.06
0.00
491.98
490.9s
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.91
10.92
0.10
0.20
49.91
49.38
0.60
0.63
97.47
97.84
-0.06
0.16
491.98
490.9s
AI =TATEE)'.t.:
Bias/Drift Determinations
Location: MPC-Tesoro - Salt Lake CiW Refinerv. UT
Source: COB Bypass - Redundant Analyzer
Project No. : AST -2025 -037 7
Prnmeter Oz - Outlet CO - Outlet NOr - Outlet SOr - Outlet
Run I Date 2125125
Span Value
lnitial Instrum€nt Zero Cal Response
lnitial Instrument Upscale Cal Response
Final Instument Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.91
100.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
200.00
0.00
99.90
0.00
99.90
0.15
0.3 r
98.08
97.98
1,000.00
0.00
498.97
0.00
498.97
0.71
0.82
489.18
492.s6
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.29
-0.33
-0.33
0.22
-0.01
-0.05
-0.04
0.08
0.16
-0.91
-0.96
0.07
0.08
-0.98
-0.64
Drift(%)
Zerc
Mid
0.04
0.00
-0.21
0.01
0.08
-0.05
0.01
0.34
Run 2 Date 2l26ns
Span Value
lnstrument Zero Cal Response
lnstnrment Upscale Cal Response
Final lnstnrmentZero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest Systern Upscale Response
Postt€st Svstem Uoscale Response
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.9r
100.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
200.00
0.00
99.90
0.00
99.90
0.15
0.31
98.08
97.98
r,000.00
0.00
498.97
0.00
498.97
0.73
0.82
489. l 8
492.56
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.29
-0.33
-0.33
0.22
-0.01
-0.0s
-0.04
0.08
0. l6
-0.91
-0.96
0.07
0.08
-0.98
-0.64
Drift(%)
Zero
Mid
0.04
0.00
-0.23
0.01
0.08
-0.05
0.01
0.34
Run 3 Dete 2l26n3
Span Value
lnstnrment Zero Cal Response
Instrument Upscale Cal Response
Final lnstrument Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.91
r00.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
200.00
0.00
99.90
0.00
99.90
0. ls
0.31
98.08
97.98
1,000.00
0.00
498.97
0.00
498.97
0.73
0.82
489. I 8
492.56
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.29
-0.33
-0.33
0.22
-0.01
-0.05
-0.04
0.08
0. l6
-0.91
-0.96
0.07
0.08
-0.98
-0.64
Drift (%)
Zero
Mid
0.04
0.00
-0.23
0.01
0.08
-0.05
0.01
o.34
=raAIii-
Bias/D rift Determin ationsIGE)
,a I -
Locedon:
Source:
Project No.:AST-202s-0377
MPC-Tesoro - Salt Lake City Refinery, UT
COB Brarass - Redundant Analyzer
Prnmcter Ou - Outlct CO - Outlet NOr - Outlet S0r - Outlet
Run 4 Date 2l26ns
Span Value
lnstrument Zero Cal Response
Instrument Upscale Cal Response
Final Instrument Zero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest Systern Zero Response
Pretest System Upscale Response
Posttest Svstem UDscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.07
0.05
10.91
10.91
100.00
0.01
49.99
0.01
49.99
0.00
0.10
49.95
49.91
200.00
0.00
99.90
0.00
99.90
0.31
0.50
97.98
97.47
1,000.00
0.00
498.97
0.00
498.97
0.82
-0.06
492.56
491.98
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posnest Soan
0.29
0.25
0.33
0.33
0.01
0.09
0.04
0.08
0.16
0.30
0.96
1.22
0.08
0.01
0.il
0.70
Drift(%)
Zqo
Mid
-0.M
0.00
0.10
-0.04
0.15
-0.26
-0.09
-0.06
Run 5 Dete 2l26n1
Span Value
lnstnrment Zero Cal Response
lnstnrment Upscale Cal Response
Final InstrumentZero Cal Response
Final Instumetrt Upscale Cal Response
Pretest System Zero Response
Posttest System Zeto Response
Pretest System Upscale Response
Posttest Svstem Upscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.07
0.06
10.91
10.91
100.00
0.0r
49.99
0.01
49.99
0.00
0.10
49.95
49.91
200.00
0.00
99.90
0.00
99.90
0.31
0.60
97.98
97.47
1,000.00
0.00
498.97
0.00
498.97
0.82
-0.06
492.56
491.98
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.29
0.25
0.33
0.33
0.01
0.09
0.04
0.08
0.16
0.30
0.96
t.22
0.08
0.01
0.64
0.70
Drift (%)
Zero
Mid
-0.04
0.00
0.10
-0.04
0. l5
-0.26
-0.09
-0.06
Run 5 Date 2l26ns
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final Iostrument Zero Cal Response
Final Insttment Upscale Cal Response
Pretest System Zero Response
Posttest Systcm Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
23.99
0.00
10.99
0.00
10.99
0.07
0.06
10.91
10.91
100.00
0.01
49.99
0.01
49.99
0.00
0.10
49.95
49.91
200.00
0.00
99.90
0.00
99.90
0.31
0.60
97.98
97.41
1,000.00
0.00
498.97
0.00
498.97
0.82
-0.06
492.56
491.98
Bias (%)
Pretest Zero
Posttest Z€ro
Praest Span
Dn(tteqi Snrn
0.29
0.25
0.33
0.33
0.01
0.09
0.04
0.08
0.16
0.30
0.96
1.22
0.08
0.01
0.64
0.70
)riff (%)
Zero
vfid
-0.M
0.00
0. l0
-0.04
0.15
-0.26
-0.09
-0.06
AI =taIEE)BiaslDrift Determinations
Locadon: MPC-Tesoro - Salt Late City Refurery, UT
Source: COB Broass - Redundant Analrrzer
Project No.: AST-2025-0377
Prnmeter 0r - Outlet CO - Outlet NOr - Outlet SO, - Outlel
Run 7 Dete 2l26ns
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final Instrument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Postrcst Sysrcm Zero Response
Pretest System Upscale Response
Pnstfect Svst..m I Inscele Re-emnse
23.99
0.00
10.99
0.00
10.99
0.06
0.06
10.91
10.92
100.00
0.01
49.99
0.01
49.99
0. l0
0.20
49.91
49.38
200.00
0.00
99.90
0.00
99.90
0.60
0.53
97.47
97.50
1,000.00
0.00
498.97
0.00
498.97
-0.06
0.00
491.98
490.95
Bias (%)
Pretest Zero
Posttest Zero
Pr€test Span
Posftest Snan
0.25
0.25
0.33
0.29
0.09
0. l9
0.08
0.61
0.30
0.32
1.22
1.20
0.01
0.00
0.70
0.80
Drift (%)
Zero
\,lid
0.00
0.04
0.10
-0.53
0.02
0.02
0.01
-0.10
Run 8 Dete 2l26ns
Span Value
hstrument Zero Cal Response
lnstrumetrt Upscale Cal Response
Final Instrument Zero Cal Response
Final lnstrument Upscale Cal Response
Pretest Systern Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.06
10.91
t0.92
100.00
0.01
49.99
0.01
49.99
0.10
0.20
49.91
49.38
200.00
0.00
99.90
0.00
99.90
0.60
0.63
97.47
97.50
1,000.00
0.00
498.97
0.00
498.97
-0.06
0.00
491.98
490.95
3ias (%)
ketest Zero
losttest Zero
lretast Span
)osttesf Snan
0.25
0.25
0.33
0.29
0.09
0.19
0.08
0.61
0.30
0.32
1.22
1.20
0.01
0.00
0.70
0.80
)rift (%)
Lero
\,Iid
0.00
0.04
0.10
-0.53
0.02
0.02
0.01
-0.10
Run 9 llete 2126125
Span Value
lnstument Zero Cal Response
lnstrument Upscale Cal Response
Final Instrument Zero Cal Response
Final Instument Upscale Cal Response
Prctest System Zero Response
Posttest System Zero Response
Prctest System Upscale Response
Posttest Svstm I Inscale Rxmnse
23.99
0.00
10.99
0.00
10.99
0.06
0.06
10.91
10.92
100.00
0.01
49.99
0.01
49.99
0.10
0.20
49.91
49.38
200.00
0.00
99.90
0.00
99.90
0.60
0.53
91.47
97.84
1,000.00
0.00
498.97
0.00
498.97
-0.06
0.15
491.98
490.95
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.25
0.33
0.29
0.09
0.19
0.08
0.61
0.30
0.32
t.22
1.03
0.01
0.02
0.70
0.80
Drift(%)
Zero
Mid
0.00
0.04
0.10
-0.53
0.02
0. l9
0.02
-0.10
puIATEe QA Data
Location MPC-Tesoro - Salt Lake City Refinery, UT
Sorr."
Project No. AST-2025-0377
Parameter Or - Outlet COr - Outlet CO - Outlet
Make
Model
s/N
Oneratins Ranse
Servomex
4900
100269
25
Servomex
4900
100269
100
Thenno
48i
JCl3l4l008t2
200
Cylinder ID
7*ro
Low
Mid
Hish
NA
NA
RR02538
EB0069884
NA
NA
RR02538
EB0069884
NA
NA
cc721736
cc721736
Cylinder Certified Values
Z*ro
Low
Mid
Hish
NA
NAll
23.99
NA
NA
10.9
23.9
NA
NA
519
sl9
Cylinder Expiration Date
7*ro
Low
Mid
Hish
NA
NA
9n9/3r
4/U32
NA
NA
9/19/3r
4/t/32
NA
NA
219127
2t9/27
Tvne of Samnle Line Heated Line
Alt6rlrceTEOtlNIOAL GR.)r1F)
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Response Times
Source: Recen - Primary Analuer
Project No. : AST-2025 -037 7
bro
Low
Mid
Aver
=taAI Calibration DataIEE)
MPC-Tesoro - Salt Lake CityRefinery, UTLocation:
Source:
Project No.:
Regen - Primary Analyzer
AST-202s-0377
Dste:2125/25
Paremeter Or - Outlet CO, - Outlet CO - Outlet
Exnected Averase Concentration 2.00 16.00 s0.00
Span Between
Low
High
Desired Soan
2.00
20.00
23.99
r6.00
80.00
23.90
50.00
250.00
100.00
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
9.60
14.39
9.s6
14.34
40.00
60.00
lligh Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Actual Concentratioo (Yo or ppm)
Znro
Low
Mid
Hish
0.00
NA
I1.00
23.99
0.00
NA
10.90
23.90
0.00
NA
s0.00
100.00
Resoonse Time (seconds)60.00 60.00 60.00
Upscale Calibration Gas (Cnr^)Mid Mid Mid
Instrument Response (%o or ppm)
7*ro
Low
Mid
Hish
0.00
NA
11.01
24.00
-0.05
NA
1 l.l8
23.88
0.00
NA
s0.00
100.00
Performance (7o of Span or Cal. Gas Conc.)
7*ro
Low
Mid
Hish
0.00
NA
0.04
0.04
0.21
NA
t.t7
0.08
0.00
NA
0.00
0.00
Status
7*ro
Low
Mid
Hish
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
tEe=laAI Bias/Drift Determinations
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Primary Analrrzer
Project No.: AST-2025-0377
Paremeter Or - Outlet COr - Outlet CO - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
I l.0l
10.98
-0.07
-0.04
I 1.15
I 1.13
0.00
-0.r2
50.00
49.08
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.06
I l.0l
10.98
-0.07
-0.04
I 1.15
I l.13
0.00
-0.t2
50.00
49.08
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
I l.0l
10.98
-0.07
-0.04
I l.l5
I l.l3
0.00
-0.t2
50.00
49.08
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale ResDonse
0.06
0.06
10.98
10.97
-0.04
-0.03
I l.13
I 1.14
-0.12
0.27
49.08
49.06
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
0.06
0.06
10.98
10.97
-0.04
-0.03
I t.13
I l.14
-0.12
0.27
49.08
49.06
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale ResDonse
0.06
0.06
10.98
10.97
-0.04
-0.03
I l.13
I l.l4
-0.12
0.27
49.08
49.06
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.97
10.98
-0.03
-0.04
I l.14ll.ll
0.27
0.24
49.06
48.84
Run 8
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale ResDonse
0.06
0.06
10.97
10.98
-0.03
-0.04
I l.14ll.ll
0.27
0.24
49.06
48.84
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.97
10.98
-0.03
-0.04
I l.l4ll.ll
0.27
0,24
49.06
48.84
Bias/Drift Determinations
Locrtion: MPC-Tesoro - Sdt Lake Citv Refinerv. UT
Source: Regen - Primary Analyzer
Project No.: AST-2025-0377
Prrrmeter Or - Outlet COz - Outlct CO - Outlet
Run 1 Dete 2l25ns
Span Value
Initial Insfrumerlt Zero Cal Response
Initial Instnrment Upscale Cal Response
Final Instnrment Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest Systern Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
23.99
0.00
I 1.01
0.00
11.01
0.06
0.06
11.01
10.98
23.90
-0.05
I l.l8
-0.05
l 1.18
-0.07
-0.M
l 1.15
I 1.13
100.00
0.00
50.00
0.00
50.00
0.00
-0.12
50.00
49.08
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.00
-0.13
-0.08
0.04
-0. l3
-0.2t
0.00
-0. l2
0.00
-0.92
Drift (%)
Zero
Mid
0.00
-0.1 3
0.13
-0.08
-0.t2
-0.92
Run 2 Date 2l2sns
Span Value
Instnrment Zero Cal Response
lnstument Upscale Cal Response
Final tnstnrmentZqo Cal Response
Final Instrument Upscale Cal Response
Pretest Systern Zero Response
Posttest System Zero Response
Prete.st System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
11.01
0.00
11.01
0.06
0.06
11.01
10.98
23.90
-0.05
I 1.18
-0.05
1 1.18
-0.07
-0.04
1 l.l5
I 1.13
100.00
0.00
50.00
0.00
s0.00
0.00
-0. l2
50.00
49.08
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.00
-0.13
-0.08
0.M
-0.13
-0.21
0.00
-0.12
0.00
-0.92
Drift(%)
Zero
Mid
0.00
-0.13
0.13
-0.08
-0. l2
-0.92
Run 3 Dete Azsns
Span Value
lnstnrment Zero Cal Response
lnstrument Upscale Cal Response
Final Instnrment Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem UDscale Response
23.99
0.00
11.01
0.00
11.01
0.06
0.06
I l.0l
10.98
23.90
-0.05
I 1.18
-0.05
I l.l8
-0.07
-0.04
I l.l5
I l.l3
100.00
0.00
50.00
0.00
50.00
0.00
-0.12
50.00
49.08
Bias (%)
Pretest Z€ro
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.00
-0.13
-0.08
0.04
-0.13
-0.21
0.00
-0.12
0.00
-0.92
Drift(%)
Zero
Mid
0.00
-0. l3
0.13
-0.08
-0.12
-0.92
=rcrAI Bias/Drift Determinations
Locedon: MPC-Tesoro - Salt Lake Citv Refinerv. UT
Source: Regen - Primary Analyzer
Project No.: AST-2025-0377
Peremeter 0r - Outlct COz - Outlet CO - Outlet
Run 4 Dete 2l2sns
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final Instnrment Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest Systern Zero Response
Pretest Systern Upscale Response
Postt€st Svstem Uoscale Resoonse
23.99
0.00
I l.0l
0.00
11.01
0.06
0.05
10.98
t0.97
23.90
-0.05
I l.l8
-0.05
I t.l8
-0.04
-0.03
11.13
I l.14
100.00
0.00
50.00
0.00
s0.00
-0.12
0.27
49.08
49.06
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.2s
0. l3
0.17
0.04
0.08
0.2t
0.17
0.12
0.27
0.92
0.94
Drift(%)
Zero
Mid
0.00
-0.04
0.04
0.M
0.39
-0.02
Run 5 Drte A25nS
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final InstrumentZero Cal Response
Final lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem llnscale Resnonse
23.99
0.00
r 1.01
0.00
11.01
0.06
0.06
10.98
t0.91
23.90
-0.05
1 1.18
-0.05
I 1.18
-0.04
-0.03
I l.l3
I 1.14
100.00
0.00
50.00
0.00
50.00
-0.12
0.27
49.08
49.06
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
losttest Soan
0.25
0.25
0.13
0. l7
0.M
0.08
0.21
o.t7
0.12
0.27
0.92
0.94
)rift (%)
Lero
vfid
0.00
-0.04
0.M
0.04
0.39
-0.02
Run 5 Date 2l25ns
ipan Value
hstnrment Zero Cal Response
nstument Upscale Cal Response
iinal lnstrument Zero Cal Response
iinal Instnrment Upscale Cal Response
lretest System Zero Response
losttest System Zero Response
lretest System Upscale Response
)osftesf Swfem IJnscale Resnonse
23.99
0.00
I 1.01
0.00
I 1.01
0.06
0.06
10.98
10.9?
23.90
-0.05
I l.l8
-0.05
I l.l8
-0.04
-0.03
1 l.l3
I 1.14
100.00
0.00
50.00
0.00
50.00
-0.t2
0.27
49.08
49.06
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Span
0.25
0.2s
0.13
0.17
0.04
0.08
0.21
0.17
0.r2
0.27
0.92
0.94
Drift(%)
Zero
Mid
0.00
-0.04
0.M
0.04
0.39
-0.02
=taAI Bias/Drift DeterminationsIEE).ri :
Locedon: MPC-Tesoro - Salt Lake Citv Refinerv, UT
Source: Regen - Primary Analyzer
Project No.:AST-2025-0377
Prremeter Or - Outlet COr - Outlet CO - Outlet
Run 7 Date 2l2Sl2S
Spao Value
lnstrument Zero Cal Response
Instnrment Upscale Cal Response
Final Instnrment Zero Cal Response
Final Instumcnt Upscale Cal Response
Pretest System Zero Respoose
Posttest System Zero Response
Pretest System Upscale Response
P^.ft*t Svstcm I Inscale Ramnse
23.99
0.00
11.01
0.00
11.01
0.06
0.06
t0.91
10.98
23.90
-0.05
I 1.18
-0.05
1 1.18
-0.03
-0.04
I l.14
ll.ll
I00.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48.84
Sias (%)
lretest Z€ro
Posttest Zero
ket€st Span
Posttest Snan
0.25
0.25
0.t7
0.13
0.08
0.04
0.t7
0.29
0.27
0.24
0.94
l.l6
Drift(%)
Zero
\ilid
0.00
0.04
-0.04
-0.13
-0.03
-0.22
Run t Date 2lzsns
Span Value
lnstnrment Zero Cal Response
lnstnrment Upscale Cal Response
Final lnstnrment Zero Ca[ Response
Final Instnrment Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem I Inscale Resoonse
23.99
0.00
I 1.01
0.00
I l.0l
0.06
0.06
10.97
10.98
23.90
-0.05
I 1.18
-0.05
I 1.18
-0.03
-0.04
I 1.14
11.11
100.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48_84
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Pnsttest Snen
0.25
0.25
0.17
0.13
0.08
0.04
0.17
0.29
0.21
0.24
0.94
l. l6
Drift(%)
Zerc
\,Iid
0.00
0.04
-0.04
-0.13
-0.03
-0.22
Run 9 Date 2l25ns
Span Value
lnstnrment Zero Cal Response
lnstrument Upscale Cal Response
Final Instument Zero Cal Response
Final Instument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Rqsoonse
23.99
0.00
I r.0l
0.00
I 1.01
0.05
0.05
10.97
10.98
23.90
-0.05
I r.l8
-0.05
I 1.18
-0.03
-0.M
ll.14
11.il
100.00
0.00
50.00
0.00
50.00
0.27
0.24
49.06
48.84
3ias (%)
Praest Zero
Posttest Zero
lretest Span
)osttest Snan
0.25
0.25
0.17
0.13
0.08
0.04
o.t7
0.29
0.27
0.24
0.94
1.16
)rift (%)
Zero
\iIid
0.00
0.04
-0.04
-0.1 3
-0.03
-0_22
AllErrEE)QA Data
Location MPC-Tesoro - Salt Lake Citv Refinerv. UT
Source Regen - Redundant Analyzer
Project No. AST-2025 -0377
Paremeter Or - Outlet COr - Outlet CO - Outlet
Make
Model
S/N
Oneretins Rense
Servomex
4900
100269
25
Servomex
4900
100269
100
Thermo
48i
JCl314l008l2
200
Cylinder ID
Znro
Low
Mid
Hieh
NA
NA
EB0069878
E80069884
NA
NA
E80069878
E80069884
NA
NA
cc72t736
cc721736
Cylinder Certilied Values
Z*ro
Low
Mid
Hish
NA
NA
11.01
23.99
NA
NA
10.92
23.9
NA
NA
sl9
519
Cylinder Expiration Date
7*ro
Low
Mid
Hish
NA
NA
8n8t32
4n/32
NA
NA
8n8t32
4^/32
NA
NA
219127
Tvne of Samole Line Heated Sample Line
Response Times
Locetion: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Redundant Analper
Project No.: AST-2025-0377
Tnro
Low
Mid
60
NA
::
60
NA
60
AI =IAIEE)Calibration Data
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Source: Regen - Redundant Analyzer
Project No.: AST-2025-0377
D*e:2/25125
Parameter Or - Outlet COr - Outlet CO - Outlet
Expected Average Concentration 5.00 17.00 s0.00
Span Between
Low
High
Desired Span
s.00
25.00
23.99
17.00
8s.00
23.90
50.00
2s0.00
100.00
Low Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Mid Range Gas
Low
Hish
9.60
t4.39
9.s6
14.34
40.00
60.00
High Range Gas
Low
Hish
NA
NA
NA
NA
NA
NA
Actual Concentration (o/o or ppm)
Znro
Low
Mid
Hish
0.00
NA
I t.0l
23.99
0.00
NA
10.92
23.90
0.00
NA
50.00
100.00
Response Time (seconds)60.00 60.00 60.00
Upscale Calibration Gas (C-^)Mid Mid Mid
Instrument Response (% or ppm)
Tnro
Low
Mid
Hish
0.00
NA
10.99
24.00
-0.08
NA
tt.t7
23.88
0.01
NA
49.99
r00.00
Performance (7o of Span or Cal. Gas Conc.)
Z*ro
Low
Mid
Hish
0.00
NA
0.08
0.04
0.33
NA
l.0s
0.08
0.01
NA
0.01
0.00
7*ro
Low
Mid
Hieh
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
PASS
NA
PASS
PASS
1EE)=I TAI Bias/Drift Determinations
Location:
Source:
Project No.: AST-2025-0377
MPC-Tesoro - Salt Lake City Refinery, UT
Regen - Redundant Analyzer
Parameter O: - Outlet COr - Outlet CO - Outlet
Run I
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Response
0.06
0.07
10.91
10.91
-0.06
-0.07
I1.07
I1.04
0.23
0.00
49.94
49.9s
Run 2
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale ResDonse
0.06
0.07
10.91
10.91
-0.06
-0.07
I1.07
I1.04
0.23
0.00
49.94
49.95
Run 3
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.06
0.07
10.91
10.91
-0.06
-0.07
11.07
11.04
0.23
0.00
49.94
49.9s
Run 4
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.07
0.06
10.91
10.91
-0.07
-0.01
I1.04
I 1.04
0.00
0.10
49.95
49.91
Run 5
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.07
0.06
10.91
10.91
-0.07
-0.01
I1.04
I1.04
0.00
0.10
49.9s
49.91
Run 6
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Upscale Response
0.07
0.06
10.91
10.91
-0.07
-0.01
I1.04
I 1.04
0.00
0. l0
49.9s
49.91
Run 7
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.91
10.92
-0.01
-0.03
1l.M
11.09
0.10
0.20
49.91
49.38
Run 8
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale ResDonse
0.06
0.06
10.91
t0.92
-0.01
-0.03
I1.04
I 1.09
0.10
0.20
49.91
49.38
Run 9
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
0.06
0.06
10.91
10.92
-0.01
-0.03
I1.04
I 1.09
0.10
0.20
49.91
49.38
AITa-
Bias/Drift Determinations
Locetion: MPC-Tesoro - Salt Iake CiW Refrnery. UT
Source: Regen - Redundant Analyzcr
ProJect No.: AST-2025-0377
Peremetcr 0r - Outlet CO: - Outlet CO - Outlet
Run I Date A26ns
Span Value
Initid Instrument Zero Cal Response
Initial lnstrument Upscale Cal Response
Final lnstrument Zqo Cil Response
Final lnstrument Upscale Cal Response
Praest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Systcm Upscale Response
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.91
23.90
-0.08
I 1.17
-0.08
I 1.17
-0.06
-0.07
I1.07
l 1.04
100.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
Bias (%)
Pretest Z€ro
Posttest Zero
Fretest Span
Posttest Span
0.25
0.29
-0.33
-0.33
0.08
0.04
-0.42
-0.54
0.22
-0.01
-0.05
-0.04
Drift (%)
Zero
Mid
0.04
0.00
-0.04
-0.13
-0.23
0.01
Run 2 Dete 2126125
Span Value
lnstnrment Zero Cal Response
lnstnrment Upscale Cal Response
Final Instrumeut Zero Cal Response
Final lnstument Upscale Cal Response
Pretest System Zero Response
Posttest System Zcro Response
Pretest System Upscale Response
Posttest Svstcm Uoscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.91
23.90
-0.08
I l.l7
-0.08
1 1.17
-0.06
-0.07
I1.07
I 1.04
100.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
Bias (%)
Praest Zero
Posttest Zero
Praest Span
Posttest Span
0.25
0.29
-0.33
-0.33
0.08
0.04
-0.42
-0.54
0.22
-0.01
-0.05
-0.04
Drift(%)
Zero
Mid
0.04
0.00
-0.04
-0.13
-0.23
0.01
Run 3 Dete 2126125
Span Value
lnstrument Zero Cal Response
Instnrment Upscale Cal Response
Final Instrument Zero Cal Response
Final Instilment Upscale Cal Response
Praest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.07
10.91
10.91
23.90
-0.08
I 1.17
-0.08
1 1.17
-0.06
-0.07
11.07
I 1.04
100.00
0.01
49.99
0.01
49.99
0.23
0.00
49.94
49.95
Bias (%)
Pretest Ze[o
Posttest Zero
Prctest Span
Posttest Soan
0.2s
0.29
-0.33
-0.33
0.08
0.M
-0.42
-0.54
0.22
-0.01
-0.05
-0.04
Drift(%)
Zqo
Mid
0.04
0.00
-0.04
-0.13
-0.23
0.01
AI =l T
lr '.
]EE)Bias/Drift Determinations
T r ir ,1 '
Locedon: MPC-Tesoro - Salt Lake CiW Refinery, UT
Source: Reqen - Redundant Analwer
Project No.: AST -2025-0377
Prremeter O' - Ouflet CfL - fhrilet CO - Outlet
Run 4 Dete 2l26ns
Span Valuc
Instnrment Zero Cal Response
Instrum€nt Upscale Cal Response
Final InstrumentZero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Reponse
hetest System Upscale Response
Posttest System Upscale ResDonse
23.99
0.00
r0.99
0.00
r0.99
0.07
0.06
10.91
10.91
23.90
-0.08
1 1.17
-0.08
1 1.17
-0.07
-0.0r
11.04
11.04
100.00
0.01
49.99
0.01
49.99
0.00
0.10
49.95
49.91
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Pd<tfeqt Sn^n
0.29
0.25
0.33
0.33
0.04
0.29
0.54
0.54
0.01
0.09
0.04
0.08
Drift(%)
Zerc
\,lid
-0.04
0.00
0.25
0.00
0.10
-0.M
Run 5 Dete 2l26ns
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstument Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstean f]oscale Resnonse
23.99
0.00
10.99
0.00
10.99
0.07
0.06
10.91
10.91
23.90
-0.08
I 1.17
-0.08
I 1.17
-0.07
-0.01
I 1.04
11.04
100.00
0.01
49.99
0.01
49.99
0.00
0. l0
49.9s
49.91
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Snan
0.29
0.25
0.33
0.33
0.(N
0.29
0.54
0.54
0.01
0.09
0.04
0.08
Drift(%)
Zero
Mid
-0.04
0.00
0.25
0.00
0.10
-0.M
Run 5 Date 2l26ns
Span Value
lnstnrment Zero Cal Response
Instrument Upscale Cal Response
Final Instument Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttcst Systcm Zero Response
Praest System Upscale Response
Posttest Svstem Upscale Response
23.99
0.00
10.99
0.00
10.99
0.07
0.06
10.91
10.91
23.90
-0.08
I 1.17
-0.08
11.17
-0.07
-0.01
I 1.04
I 1.04
100.00
0.01
49.99
0.01
49.99
0.00
0.10
49.95
49.91
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.29
0.25
0.33
0.33
0.M
0.29
0.54
0.54
0.01
0.09
0.04
0.08
Drift (%)
Zero
Mid
-0.04
0.00
0.25
0.00
0. l0
-0.04
Bias/Drift Determinations
Location: MPC-Tesoro - Salt Lake CiW Refinery. UT
Source: Regen - Redundant Analwer
ProJect No.: AST-2025-0377
Peremeter Or - Outlet CO: - Outlet CO - OuOet
Run 7 Dete 2126n5
Span Value
Instument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstrumentZero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zeto Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Rcsoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.06
10.91
10.92
23.90
-0.08
1 1.17
-0.08
1 1.17
-0.01
-0.03
l1.04
I 1.09
100.00
0.01
49.99
0.01
49.99
0.10
0.20
49.91
49.38
Bias (%)
Pretest Zero
Posttest Zero
Pretest Span
Posttest Soan
0.25
0.25
0.33
0.29
0.29
0.21
0.54
0.33
0.09
0.19
0.08
0.51
Drift(%)
Zerc
Mid
0.00
0.04
-0.08
0.2t
0.10
-0.53
Run 8 Dete 2l26ns
Span Value
lnstrument Zero Cal Response
lnstrument Upscale Cal Response
Final lnstnrment Zero Cal Response
Final Instrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest Svstem Uoscale Resoonse
23.99
0.00
10.99
0.00
10.99
0.06
0.06
10.91
10.92
23.90
-0.08
I 1.17
-0.08
1 1.17
-0.01
-0.03
ll.M
I 1.09
100.00
0.01
49.99
0.01
49.99
0. l0
0.20
49.91
49.38
Bias (%)
Praest Zero
Posttest Zero
Praest Span
Posttest Soan
0.25
0.25
0.33
0.29
0.29
o.2t
0.54
0.33
0.09
0.19
0.08
0.61
Drift (%)
Zero
Mid
0.00
0.04
-0.08
o.2l
0. l0
-0.53
Run 9 Dete 2l26ns
Span Value
Instrument Zero Cal Response
Instrument Upscale Cal Response
Final lnstrument Zero Cal Response
Fiaal lnstrument Upscale Cal Response
Pretest System Zero Response
Posttest System Zero Response
Pretest System Upscale Response
Posttest System Upscale Response
23.99
0.00
r0.99
0.00
10.99
0.06
0.06
10.91
10.92
23.90
-0.08
I l.l7
-0.08
I 1.17
-0.01
-0.03
I 1.04
I 1.09
100.00
0.01
49.99
0.01
49.99
0.10
0.20
49.91
49.38
Bias (%)
Pretest Zero
Posnest Zero
Pretast Span
Posttest Snan
0.2s
0.25
0.33
0.29
0.29
0.21
0.54
0.33
0.09
0.19
0.08
0.51
Drift (%)
Zero
Vi.l
0.00
0.04
-0.08
0.21
0.10
-0.53
&PJI.Affi-Ea
Accreditation #62754
Red Ball Technical Gas Seryice
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PGVP Vendor lD # G12O24
EPA PROTOGOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
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coA #
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Customer:
:80069884
127907
900 PS|G
:t UUbYUU4.ZUZ4UJZU-L
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)4t03t2024
)4to1t2032
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:6UUOYOO4.ZUZCUJZU
)s4212711
This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-1 2/531 ,
G2.
-t
Concentratlon Uncertalfi Analytlcal Prlnclplo A$ayod On
*0.'l o/o
$.06 %
20 01 0/o
24 76 vo
1 162980025 03118n024
017146467 Un2nO24
SMART.CERT
This is to certity the gases referenced have been calibrated/tested, and verified to meet lhe defined speciflcations. This
calibrataon/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measuremenl parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
Brittany Johnson
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J R€vised on 2018-09-17
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shrevepon, A 71'|07
800-551 -81 50
PGVP Vendor lD # G12023
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
1R02538
25371
9OO PSIG
1R0253E.20230E31 -0
Certificatlon Date:
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Previous Certification Dates :
)9t21t2023
)911912031
iR02538.20230831
103925725
calrbratron has per the
G1,
Certifi ed Concentration(s)
Concentration
to^9 %
{1.00 %
Uncortalnty
to11 "/,
t0.03 o/o
Analytlcal Prlnclple
FTIR
MPA
Assayod On
Dioxide 09t21n023
ogt18DO23Orygen
Balance
Analytical Measurement Data Available Online.
cc737012.20230228
EBOO22021.20180323
1162980025 @t14t2023
017146467 09n1no23
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the deflned specifications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the ttem described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included. the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
'f* A"{"
Jasmine Godfrey
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J, Revised on 20'!8-09-17
PJLrtffi-Ea
Accreditation #62754
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, A 71107
800-551 -81 s0
PGVP Vendor lD # G12019
EPA PROTOGOL GAS GERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
:c721736
124234
1900 PSIG
)Qt21736.2019020 t-O
Certification Date:
Expiration Date:
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Lot Number:
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Previous Certiflcatlon Dates :
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)2t09t2027
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jc721736.20190207
198493836
This calibration standard has been certitled per the May 2012 EPA Traceability Protocol, Oocument EPA-600/R-12/531 ,
G1.
-t
Concentratlon Uncertalnty Anatytlcal Prlnclplo A33ayed On
E800147s9 E80014759.20180102 11h9n026 G|!IS N2
MKS MKS 2031DJG2EKVS13T 017146467 02n7D019
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specilications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
Anthony Cyr
Assistant Operations Manager
Assay Laboratory: Red Ball TGS
Vsrsion 02-J. Revrsed on 2018-09-17
Red Ball Technical Gas Service
555 Craig Kennedy Way
Shreveport, LA 71107
800-551 -81 50
PGVP Vendor lD # G12023
EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS
Cylinder Number:
Product lD Number:
Cylinder Pressure:
coA #
Customer PO. NO.:
Customer:
=8001 1606
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I9OO PSIG
-8001 1606.20230906-0
Certification Date:
Expiration Date:
MFG Facillty:
Lot Number:
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Previous Certificatlon Dates:
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E8001 1606.20230906
025274839
This calibration standard has been certified per the -12t531,
G1
Concontratlon Uncert lnty Analytlcal Pdnclple As3ayed On
09n1no23,09n8no23
'otal Oxides of Nitrogen 503 PPM
41-l\r-50
E80059947 202301 1 7
sx32691 202301 1 7
996 7 PPM
280 PPM
279 8 PPtu
Analytica I lnstrumentation
Make Modsl
42tsH1NO Chemilumines@nce Themo 1152610017 Nn9nO23
SMART.CERT
This is to certity the gases referenced have been calibrated/tested, and verifled to meet the defined specifications. This
calibration/test was performed using Gases or Scales that are trac€able through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technacal Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
,/arrt* thrrhu
Aaron Varelas
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J, Revrsed on 201&09-17
&
--Ig!s-.Accreditation #62754
Red Ball Technical Gas Service
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Cylinder Number:
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coA #
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This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-12/531,
G2
-l
Certified Concentration(s)
Concentrauon Uncertainty Analytlcal Pdnclple Assayed On
o6n4n02136t29t2}21Sulfur Dioxide 5000 PPM fl6PPM FTIR
Balance
Analytical Measurement Data Available Online
cc719287 CC7192A7 20200123 09t10n029 GMIS N2 so2 4566 PPM O27 M937410
Ana lytical lnstrumentation
s02
s02
FTIR
FTIR
MKS
MKS
Model
MKS 2O3lDJG2EKVS13I
MKS 2O31DJG2EKVS13T
017146467
017146467
05t17D021
c6n8t2021
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calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confldence level of the measurement, unless otherwise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
Amisha Jewitt
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J Revised on 2018-09-17
=TAAI NOx Converter Check
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Project No.: AST-2025-037 7
NO2 Converter Check - Outlet#Analyzer Model HffiCylinder ID Number #Cvlinder Concentration. Dpm
Pre-Test Dete 2124125 Time 14:19
Pre-Test Concentration, ppm 48.09
Pre-Test Efficiencv. 7o 97
Post-Test Date 2/25125 Time 16:46
Post-Test Concentration, ppm 45.82
Post-Test Efliciencv. 7o 92
*,s>
pul6rrpE)
__.,,\. \L Lti .r.t-
NOx Converter Check
Location: MPC-Tesoro - Salt Lake City Refinery, UT
Project No.: AST-2025-0377
NO2 Converter Check - Outlet
Analyzer Make Thermo
Analyzer Model 42ta
Serial Number 12327730521
Cylinder ID Number CC770777
Cylinder Exp. Date 4116127
Cvlinder Concentration. DDm 49.7
Pre.Test Date 2126125 Time 8:29
Pre'Test Concentiifi6-, ppm 4r:A
Pre'Test Efficiencv. 7o 92
Post-Test Date 2126/25 Time 15:08
Post-Test coocuot""tio-o, pp- 4(-n
Post-Test Efficiencv. 7o 93
*Required Eficiency is > 90 %.
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This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-12/531 ,
ino orocedure G2.
-t
Certifi ed Concentration(s)
Concentration Uncortalnty Analytlcal Prlnclple Asrayed On
Dioxide 49.7 PPM *0.5 PPM FTIR 02t16t2024,0/,116t2024
Balance
Analytical Online.
Analytica! Instrumentation
NO2
NO2
FTIR
FTIR
IVKS
MKS
MKS 2O3lDJG2EKVS13T
MKS 2O31GPPPlAsZK1XX
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ut15no24
SMART.CERT
This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This
calibration/test was performed using Gases or Scales that are traceable through National lnstitute of Standards and
Technology (NIST) to the lnternational System of Units (Sl). The basis of compliance stated is a comparison of the
measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage
factor of k=2 to approximate the 95% confidence level of the measurement, unless otheMise noted. This calibration certificate
applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball
Technical Gas Services. lf not included, the uncertainty of calibrations are available upon request and were taken into account
when determining pass or fail.
z^il;
Timothy Davis
Analytical Chemist
Assay Laboratory: Red Ball TGS
Versron 02-J. Revrsed on 2018-09.17
E80055436 20201021
EB0080844.20201 020
E80097551 20201021
29 22 PPM
94,5 PPM
63 3 PPM
c2190301 02
c2190301 02
c2190301 02
I\,f,t0s QA Data
E/-ialrce r\{,rosQA
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d.r. wf-Tanm - Srlt I rlra Ciru Pafina IIT
ura: COBBws-PriwAnalw
No.: AST-2025-0377
AI
Loo{on:
Sourc:
Ptolcct No.:
Dttc 2124125
tlcthod Crltcrh EPA
rnmalar
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dlbredor Enor P.rfomucc (7. of Soan)
ZGIO
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0.0
0.0nn
lncarltv (7. of Rrnrc)
Analyza Ma&c:
Analyza Model:
Analyzcr SN:
Envircnics ID:
Envircnics MFC Confi gution:
ComponavBalancc Ga:
Cylindcr Gu ID @ilution):
Cylinda Gu Conmtration @ilution), ppm:
Cylinda Ga ID (Mid-t cvcl):
Cylindr Gu Concmtation (Mid-kvcl), ppm:
INI (I II
Arrly,rr
Conccntrrdon
ahhh)
Injcdon I
Error
I + 7.a\
Injedon 2
Error
I r r.a\
InJcdon 3
Error
a * 7.a\
19.31 o.t%-o.t% -0.t%
12.06 o.oo/"-o.tvo o-oyo
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2.41J 4.lo/"0.30/"4.1./"
A/tfurce
SOURCE TESTING
Mass Flow Controller Calibration
Note: The mass flow controller's calibration values are used by the dilution system's operating software to improve accuracy. These calibrations are not
necessarily indicative of the systems overall performance. Performance is verified by conducting a Method 205 prior to each field use.
Calibration Performed By JFT
Dllutlon System Make:
Dllutlon System Model:
Dllutlon System S/N:
Callbratlon Equlpment Make:
Callbratlon Equlpment Model:
Callbratlon Equlpment S/t{:
Flow Cell S/t{:
Flow Cell S/N:
Callbratlon Gas:
Barometrlc Pressure, mmHt:
Amblent Temperature,'F:
Environics
4040
Scientific
M-10SLPD/sM M-D/sM, M-15LPM-D/s
272L2O;272L21
212t20
272t2L
Nitrogen
2s.559
70.7
Mass Flow Controller lD
Slze, ccm:
Make:
Model:
S/N:
#1
10,000
Environics
4040
45S242003
#2
10,000
Environics
4040
455242004
#3
1,000
Environics
4040
455242002
Set Flow True Flow Dlfference
cclmln cclmin
Set Flow True Flow Dlfference
cclmln cclmln
Set Flow True Flow Dlfference
cc/mln cclmln
5%
to%
20%
30%
40%
s0%
60%
70%
80%
90%
700%
500 489 2.2%
1,000 987 L.3%
2,000 t,970 L.s%
3,000 2,985 0.5%
4,000 4,0t4 0.4%
5,000 5,034 0.7%
6,000 6,053 0.9%
7,000 7,084 t.2%
8,000 8,119 L.S%
9,000 9,156 t.7%
10,000 Lo,202 2.o%
500 454 9.2%
1,000 959 4.L%
2,000 1,989 0.5%
3,000 3,003 0.r%
4,000 4,oL4 0.4%
5,000 5,033 0.7%
6,000 6,055 0.9%
7,000 7,093 L.3%
8,000 I,L23 L.5%
9,000 9,160 1.8%
10,000 10,195 2.O%
50 47 6.0%
100 97 3.0%
200 195 2.O%
300 298 0.7%
400 400 0.0%
500 502 0.4%
600 602 0.3%
700 706 0.9%
800 810 7.3%
900 9t4 L.6%
1,000 1,020 2.o%
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Run t
One Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv
212512511:50 AM
212512511:51AM
212512511:52AM
212512511:53AM
212512511:54AM
212512511:55 AM
212512511:56AM
212512511:57AM
212512511:58AM
212512511:59AM
212512512:00 PM
212512512:01PM
2125125L2:02PM
212512512:03 PM
212512512:04 PM
212512512:05 PM
212512512:06 PM
212512512:07 PM
212512512:08 PM
212512512:09 PM
212512512:10 PM
45773.49
45773.49
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.50
45713.51
45713.51
45773.57
45713.51
Galcutated Avg:
ait00436.pv
0.50
0.51
0.57
0.58
0.69
0.72
0.55
0.60
0.51
0.55
0.42
0.42
0.s8
0.59
0.59
0.s2
0.s8
0.62
0.55
0.47
0.58
0.s6
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
17.L6
17.20
77.L6
77.7L
77.70
17.06
17.06
77.70
t7.!8
L7.22
t7.23
L7.24
L7.25
17.24
t7.22
17.20
17.21
17.15
17.t4
17.16
77.t0
t7.t7
Run 2
One Minute Averages 02 REGEN FLUE GAS
PCT
ai100491.pv
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
212512512:11PM
2125125!2:t2PM
212512512:13 PM
212512572:t4PM
212512512:15 PM
212512512:16 PM
212512512:L7 PM
212512512:18 PM
212512512:19 PM
2125125L2:2OPM
2125125t2.,27PM
2125125L2:22PM
212512512:23PM
212512512:24PM
2125125L2:25PM
2125125t2:26PM
2125125L2:27 PM
2125125L2:28PM
2125125L2:29PM
212512512:30 PM
212512512:31PM
457L3.5t
45713.51
45713.51
45713.51
45713.51
45713.51
45713.51
45713.51
45713.51
45713.51
45773.52
45773.52
45773.52
45773.52
45773.52
45773.52
45773.52
45773.52
4s773.52
457!3.52
45773.52
ai100436.pv
0.57
0.60
0.55
0.62
0.s5
0.54
0.M
o.47
0.s2
0.60
0.77
0.87
0.86
0.64
0.70
0.64
0.63
0.69
0.64
0.62
0.65
0.63
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
17.!0
t7.73
t7.77
t7.13
17.13
17.16
17.t3
77.t7
77.L4
77.00
16.94
16.90
16.90
16.95
16.99
17.04
17.05
17.05
17.05
17.05
17.03
17.06Calculated Avg:
Run 3
One Minute Averages 02REGEN FLUEGAS COREGEN FLUEGAS CO2REGEN FLUEGAS
PCT PCT PCT
ai100491.pv ai100436.pv
0.50
0.53
0.55
0.52
0.68
0.83
0.94
0.87
0.58
0.55
0.4s
0.51
0.54
0.s4
0.32
0.35
0.50
0.45
0.55
0.66
0.53
0.57
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
212512572:32PM
212512512:33 PM
212512572:!lPM
212s12512:35 PM
212512512:36 PM
212512572:37 PM
212512512:38 PM
212512512:39 PM
212512572:40PM
212512572:4LPM
2125125L2:42PM
2125125L2:43PM
2125125t2:4PM
2l25l2sL2:45PM
212512512:46 PM
2125125L2:47 PM
212512512:48 PM
2125125 t2:49 PM
212512512:50 PM
212512512:51PM
2125125L2:52PM
45773.52
45773.52
45773.52
45713.53
45713.5s
45713.53
45713.53
45713.53
45713.53
45713.53
45713.53
45713.53
45713.53
45713.s3
45713.53
45713.53
4s713.s3
45713.53
45773.54
45773.54
45773.s4
Calculated Avg:
77.28
77.48
77.37
17.23
17.06
16.95
16.88
16.96
77.72
77.27
77.34
17.38
77.34
77.28
77.26
17.24
17.20
t7.20
17.09
17.04
L7.77
17.t9
Run 4
One Minute Averages
21251251:30 PM
21251251:31PM
21251251:32 PM
21251251:33 PM
21251251:34 PM
21251251:35 PM
21251251:36 PM
21251251:37 PM
21251251:38 PM
21251251:39 PM
21251251:40 PM
21251251:41PM
21251257:42PM
21251251:43 PM
21251257:MPM
21251251:45 PM
21251251:46 PM
2125125t:47 PV
21251251:48 PM
21251251:49 PM
21251251:50 PM
4s713.56
45713.56
45713.56
45773.57
45773.57
45773.s7
45773.57
45773.57
45773.57
457L3.57
4s7L3.57
457L3.57
457L3.57
457L3.57
457t3.57
457L3.57
45713.57
45713.58
4s713.58
45713.58
45713.s8
Calcutated Avg:
ai100436.pv
0.53
0.59
0.61
0.60
0.55
0.56
0.56
0.61
0.55
0.60
0.62
0.60
0.61
0.62
0.57
0.59
0.55
0.53
0.58
0.63
0.65
0.59
02REGEN FLUEGAS COREGEN FLUEGAS
PCT PCT
ai100491.pv
CO2 REGEN FLUE GAS
PCT
ai100438.pv
77.M
77.47
17.38
17.26
L7.26
17.29
17.3t
17.34
17.42
17.43
t7.47
17.54
17.55
17.50
17.57
17.46
17.39
77.47
77.32
!7.42
17.42
L7.41
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Run 5
one Minute Averages 02 REGEN FLUE GAS
PCT
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
ai100491.pv ai100436.pv
0.37
0.63
0.64
0.89
0.74
0.66
0.56
0.66
0.59
0.76
0.96
1.04
0.95
0.96
1.05
0.86
0.82
0.77
0.68
0.57
0.45
o.74
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
21251251:51PM
21251251:52 PM
21251251:53 PM
21251251:54 PM
21251251:55 PM
21251251:56 PM
21251251:57 PM
21251251:58 PM
21251251:59 PM
21251252:00 PM
2125125 2:01PM
21251252:02PM
21251252:03 PM
2125125 2:04 PM
21251252:05 PM
21251252:06 PM
21251252:07 PN
21251252:08 PM
21251252:09 PM
21251252:10 PM
21251252:11PM
45713.58
45713.58
45713.58
45713.58
45713.s8
45713.58
45713.58
45713.58
45713.58
45713.58
45713.58
45713.59
45713.59
45713.59
45713.59
45713.59
4s713.s9
45713.59
45713.59
45713.59
45713.59
Calcutated Avg:
17.77
17.08
16.98
16.88
16.94
17.05
17.08
17.06
17.0s
16.89
16.75
76.77
16.81
16.77
16.77
16.88
16.94
16.96
17.03
L7.t3
L7.23
16.96
Run 6
One Minute Averages
21251252:72PM
21251252:13 PM
21251252:t4PM
21251252:15 PM
2125125 2:16 PM
2t2st252:L7 PM
2125125 2:18 PM
2125125 2:19 PM
21251252:20PM
21251252:2lPM
21251252:22PM
21251252:23PM
21251252:24PM
21251252:25PM
21251252:26PM
21251252:27 PM
21251252:28PM
21251252:29PM
21251252:30 PM
21251252:31PM
2125125232PM
45713.59
45713.59
45713.59
4s713.59
45713.60
45713.60
45713.60
45713.60
45713.60
45713.60
4571s.60
45713.60
4s713.60
45713.60
45713.60
4s713.60
45713.60
45713.60
45713.60
45713.61
45713.61
Calculated Avg:
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv ai100436.pv
0.59
0.60
0.s2
0.59
0.80
0.78
0.84
0.73
0.66
o.M
0.56
0.49
0.49
0.49
0.42
0.20
0.40
0.62
0.79
0.85
0.58
0.59
17.22
L7.23
L7.77
L7.05
L7.07
17.00
16.99
L7.00
17.09
t7.32
L7.48
t7.49
1-7.54
17.55
17.50
17.40
77.25
77.09
16.97
17.06
77.t9
77.22
Run 7
One Minute Averages 02 REGEN FLUE GAS
PCT
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
ai100491.pv ai100436.pv
0.48
0.55
0.53
0.50
0.55
0.48
0.46
0.51
0.M
0.80
0.88
0.95
0.92
0.82
0.s3
0.4s
0.50
0.38
0.28
0.56
0.54
0.58
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2125125 3:05 PM
2125125 3:06 PM
2125125 3:07 PM
2125125 3:08 PM
2125125 3:09 PM
2125125 3:10 PM
2125125 3:11PM
2125125 3:12 PM
2125125 3:13 PM
2125125 3:14 PM
2125125 3:15 PM
2125125 3:16 PM
2125125 3:17 PM
2125125 3:18 PM
2125125 3:19 PM
2125125 3:20 PM
2125125 3:21PM
21251253:22PM
2125125 3:23 PM
21251253:24PM
2125125 3:25 PM
45713.63
45713.63
45713.63
45713.63
45713.63
45713.63
45713.63
45713.63
45713.63
45713.64
457t3.U
457L3.64
457t3.M
457t3.64
457t3.64
457t3.64
457L3.64
457t3.64
45713.U
45713.U
45773.il
Calcutated Avg:
17.39
77.49
77.5t
17.36
17.77
17.28
77.47
77.29
17.09
16.87
16.77
16.75
16.76
16.88
17.03
t7.04
L7.07
L7.12
L7.72
16.99
L7.02
t7.Lt
Run 8
One Minute Averages 02 REGEN FLUE GAS
PCT
COREGEN FLUEGAS CO2REGEN FLUEGAS
PCT PCT
ai100491.pv ai100436.pv
0.47
0.46
0.s9
0.52
o.52
0.63
0.63
0.73
0.72
0.67
0.51
0.55
0.61
0.63
0.55
0.s8
0.58
0.s8
0.61
0.74
0.63
0.60
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2125125 3:26 PM
21251253:27 PM
2125125 3:28 PM
2125125 3:29 PM
2125125 3:30 PM
2125125 3:31PM
2125125 3:32 PM
2125125 3:33 PM
2125125 3:34 PM
2125125 3:35 PM
2125125 3:36 PM
2l2sl25 3:37 PM
2125125 3:38 PM
2125125 3:39 PM
2125125 3:40 PM
2125125 3:41PM
21251253:42PM
2125125 3:43 PM
21251253:MPM
2125125 3:45 PM
2125125 3:46 PM
45713.64
45773.64
45713.65
45713.6s
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.65
45713.6s
45713.66
45713.66
45713.66
45713.66
Catculated Avg:
17.04
17.04
17.06
16.97
16.94
15.92
16.82
16.80
16.86
16.90
17.05
77.L4
77.08
17.06
77.04
17.0t
17.O3
16.99
16.88
16.86
16.89
16.97
Run 9
One Minute Averages 02 REGEN FLUE GAS
PCT
ai100491.pv
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
21251253:47 PM
2125125 3:48 PM
21251253:49 PM
2125125 3:50 PM
2125125 3:51PM
2125125 3:52 PM
2125125 3:53 PM
2125125 3:54 PM
2125125 3:55 PM
2125125 3:56 PM
2125125 3:57 PM
2125125 3:58 PM
2125125 3:59 PM
21251254:00 PM
21251254:01PM
21251254:02 PM
21251254:03 PM
21251254:04 PM
21251254:05 PM
21251254:06 PM
21251254:07 PM
45713.66
45713.66
4s713.66
45713.66
45713.66
4s713.66
45713.66
45713.66
45713.66
45713.66
45713.67
45773.67
45773.67
45773.67
45773.67
45713.67
45773.67
45773.67
45773.67
45773.67
45773.67
Gatculated Avg:
ai100436.pv
0.59
0.s9
0.55
0.59
0.62
0.58
0.70
0.59
0.s4
0.53
0.61
0.s3
0.55
0.76
0.80
0.82
0.73
0.78
0.63
0.62
0.62
0.63
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
16.93
16.98
17.06
77.74
17.t2
77.01
16.95
77.01
77.04
17.01
16.94
16.95
16.89
16.78
16.75
16.76
L6.77
16.83
16.89
16.89
16.87
16.93
Run 1
One Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
o/o Vo qb
ai10049t.pv
212612510:30 AM
212612510:31AM
212612510:32AM
212612510:33AM
212612510:34AM
212612510:35AM
212612510:36AM
212612510:37AM
212612510:38AM
2126125 t0:39AM
2126125 t0:40 AM
212612510:41AM
212612510:42AM
212612510:43AM
212612510:44AM
212612510:45AM
212612510:46AM
212612510:47AM
212612510:48AM
212612510:49AM
212612510:50 AM
45714.4
45714.M
45714.M
45774.M
45774.M
45774.M
45774.M
457L4.M
457t4.44
457L4.M
457L4.45
45714.4s
45774.45
45774.45
45774.45
45774.45
457t4.45
457L4.45
457t4.45
457t4.45
4s714.45
Catculated Avg:
ai100436.pv
1.72
1.55
1.51
1.03
1.19
1.55
1.66
1.61
t.76
1.81
t.84
1.84
1.91
7.62
1.4iI
7.22
1.19
1.00
1.04
1.33
1.55
1.50
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
16.79
16.87
17.05
17.20
77.74
16.96
16.89
16.88
16.83
16.75
76.7L
16.70
76.77
16.90
17.05
t7.22
L7.37
L7.49
L7.40
17.79
17.06
t7.ot
Run 2
one Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv
212612510:51AM
212612510:52 AM
212612510:53AM
212612510:54AM
212612510:55AM
212612510:56AM
212612510:57AM
212612510:58AM
212612510:59AM
212612511:00 AM
212612511:01AM
212612511:02 AM
212612511:03AM
212612511:04AM
212612511:05 AM
212612511:06AM
212612511:07AM
212612511:08 AM
212612511:09 AM
212612511:10 AM
2126125 t1:11AM
457L4.45
457t4.45
457L4.45
457L4.45
457t4.46
45774.46
45774.46
45774.46
4s7L4.46
45774.46
45774.46
4s774.46
45774.46
4s774.46
45774.46
45774.46
45774.46
45774.46
45774.47
45714.47
45714.47
Catculated Avg:
ai100436.pv
1.81
L.O4
1.91
1.80
1.49
1.35
L.47
1.58
1.56
1.65
1.59
1.61
L.7t
L.75
L.77
t.2t
7.25
7.20
7.23
1.16
1.36
1.50
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
16.85
16.71
16.79
16.96
L7.70
L7.75
L7.70
17.03
17.02
17.03
17.04
L7.01
16.95
16.82
17.O!
17.3t
17.32
77.30
17.36
17.35
17.23
17.o7
Run 3
One Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv
212612511:12 AM
212612511:13AM
212612511:14AM
212612511:15AM
212612511:16AM
212612511:17AM
212612511:18 AM
212612511:19AM
212612511:20AM
212612511:21AM
2126125t7:224M
212612511:23AM
212612577.,244M
212612511:25AM
212612511:26AM
212612577:27 AM
212612511:28AM
212612511:29AM
212612511:30 AM
212612511:31AM
212612511:32AM
45774.47
45774.47
45774.47
45774.47
45774.47
45774.47
4s7L4.47
4s7L4.47
457L4.47
457t4.47
457L4.47
457t4.48
45774.48
45774.48
45774.48
45774.48
457L4.8
457L4.48
457t4.48
457t4.48
45714.8
Calcutated Avg:
ai100436.pv
t.M
1.56
1.60
1.53
1.50
1.46
1.43
t.74
1.05
7.27
7.42
1.60
7.72
L.73
L.75
1.55
L.45
1.60
1,.67
1.74
1.80
t.52
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
17.16
L7.tO
L7.08
L7.!3
t7.73
L7.72
L7.27
L7.43
17.46
17.33
77.22
77.70
77.04
16.97
17.03
77.77
L7.27
L7.tt
17.00
16.98
16.93
17.L4
Run 4
One Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv ai100436.pv
1.62
7.70
1.80
1.60
1.68
1.57
1.M
1.37
1.49
1.50
1.61
1.56
7.48
7.67
7.70
7.2t
1.38
1.59
1.68
7.87
1.38
L.s7
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
212612512:00 PM
212612512:01PM
2126125!2:O2PM
212612512:03 PM
212612512:04 PM
212612512:05 PM
212612512:06 PM
2126125!2:07 PM
212612512:08 PM
212612512:09 PM
212612512:10 PM
212612512:11PM
212612512:t2PM
212612512:13 PM
212612572:t4PM
212612512:15 PM
212612512:16 PM
212612572:t7 PM
212612512:18 PM
212612512:19 PM
212612572:20PM
45774.50
45774.50
45774.50
45774.50
45774.50
45774.50
45774.50
45774.5L
45774.5L
45774.5L
45774.51
45774.5t
45714.5t
45774.5L
45774.5t
45774.5L
45774.5L
45774.5t
45774.5L
45774.5t
45774.5t
Calcutated Avg:
77.18
77.13
77.75
77.t2
77.11
17.22
17.29
17.28
17.24
17.20
77.20
77.22
17.20
77.t6
17.20
77.30
17.25
77.74
77.07
17.00
17.37
17.19
Run 5
One Minute Averages 02REGENFLUEGAS COREGEN FLUEGAS CO2REGENFLUEGAS
PCT PCT PCT
ait00491.pv
2126125L2:2!PM
2126125L2:22PM
2126125t2:23PM
212612512:24PM
2126125!2:25PM
212612572:26PM
212612572:27 PM
212612572:28PM
212612512:29 PM
212612512:30 PM
212612512:31PM
212612572:32PM
212612512:33 PM
212612512:!tPM
212612512:35 PM
212612512:36 PM
2126125t2:37 PM
212612512:38 PM
212612512:39 PM
212612512:40 PM
212612572:4tPM
45774.52
4571^4.52
45774.52
45774.52
45714.52
45714.52
45774.52
45714.52
45774.52
45774.52
45774.52
45714.52
45714.52
45714.52
45774.53
457L4.53
457L4.53
45774.53
45714.53
45774.53
45774.53
Catculated Avg:
ai100436.pv
L.77
L.M
1.68
7.74
1.39
7.42
7.47
1.51
7.73
1.90
7.74
1.45
7.72
7.26
7.47
1.50
7.27
1.30
1.58
7.76
1.65
1.50
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
77.5L
17.33
L7.73
17.74
17.35
17.38
L7.29
t7.20
L7.70
17.02
L7.07
t7.37
17.53
t7.45
L7.29
L7.24
L7.34
L7.34
17.t6
77.t0
17.t5
17.26
Run 6
One Minute Averages 02 REGEN FLUE GAS CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT PCT
ai100491.pv
212612572:42PM
212612572:43PM
212612572:4PM
212612512:45 PM
2126125L2:46PM
2126125L2:47 PM
2126125t2;48P14
212612512:49 PM
212612512:50 PM
212612512:51PM
2126125L2:52PM
212612512:53 PM
2126125L2:54PM
212612512:55 PM
212612512:56 PM
2126125t2:57 Pl4
212612512:58 PM
212612512:59 PM
21261251:00 PM
21261251:01PM
21261251:02 PM
457L4.53
457L4.53
45774.53
45774.53
45774.53
45774.53
45774.s3
4s774.53
45714.54
45774.54
45774.54
45714.54
45714.54
45714.54
45714.54
457L4.54
457t4.54
457t4.54
457L4.54
457L4.54
45774.s4
Calculated Avg:
ai100436.pv
1.59
7.72
1.68
7.73
1.68
1.26
1.15
1.28
L.37
1.65
1.81
L.78
1.60
t.29
t.72
1.39
L.26
t.34
1.01
1.16
7.42
t.4
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
17.75
17.09
17.09
17.05
17.06
77.34
77.49
77.41
77.3t
77.74
77.03
17.06
17.77
17.33
17.45
L7.38
17.3s
17.49
17.62
77.46
17.35
,,7.27
Run 7
One Minute Averages 02 REGEN FLUE GAS
PCT
ai100491.pv
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
21261251:30 PM
21261251:31PM
21261251:32 PM
21261251:33 PM
21261251:34 PM
21261251:35 PM
21261251:36 PM
21261251:37 PM
21261251:38 PM
21261251:39 PM
21261251:40 PM
21261251:41PM
2126125L:42PM
21261251:43 PM
21261251:44 PM
21261251:45 PM
2126125 t:46 PM
21261257:47 PM
21261251:48 PM
21261251:49 PM
21261251:50 PM
457L4.56
457L4.56
457L4.56
457L4.57
457L4.57
45774.57
45774.57
45774.57
45774.57
45774.57
45774.57
457L4.57
45714.57
45774.57
45774.57
45774.57
45774.57
45774.58
45774.58
45774.58
45774,58
Catculated Avg:
ai100436.pv
1.38
1.38
1.33
t.M
1.52
1.46
1.45
1.51
t.48
1.46
1.56
L.70
1.55
L.62
1.63
1.56
1.43
1.32
1.30
t.t7
1.27
1.45
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
L7.25
t7.29
L7.3t
17.26
17.L9
77.23
77.24
77.22
77.29
77.26
17.72
77.77
77.73
77.74
17.75
77.77
17.29
17.33
17.37
t7.47
L7.37
17.24
Run 8
one Minute Averages
21261251:51PM
21261251:52 PM
21261251:53 PM
21261251:54 PM
21261251:55 PM
21261251:56 PM
21261251:57 PM
21261251:58 PM
21261251:59 PM
2126125 2:00 PM
21261252:01PM
21261252:02PM
2126125 2:03 PM
21261252:04PM
21261252:05 PM
2126125 2:06 PM
21261252:07 PM
2126125 2:08 PM
2126125 2:09 PM
2126125 2:10 PM
2126125 2:11PM
45714.58
457L4.58
457t4.58
457t4.58
45774.58
457L4.58
45774.58
45774.58
45774.58
45714.58
45714.58
45714.59
457t4.59
45714.59
457L4.59
457L4.59
457L4.59
457L4.59
457L4.59
45774.59
45714.59
Calcutated Avg:
02 REGEN FLUE GAS
PCT
ai100491.pv
L.24
t.t4
1.00
1.03
7.24
7.37
1.55
1.45
1.63
1.68
1.66
1.70
1.61
1.06
1.10
t.32
L.34
1.58
7.42
7.70
7.75
1.4!
CO REGEN FLUE GAS
PCT
ai100436.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
CO2 REGEN FLUE GAS
PCT
ai100438.pv
17.36
77.47
77.62
77.56
t7.35
L7.23
t7.t5
17.13
77.70
17.05
77.04
17.06
77.23
77.46
77.48
17.35
17.24
t7.17
t7.18
L7.L2
17.02
!7.260.00
Run 9
one Minute Averages 02 REGEN FLUE GAS
PCT
ai100491.pv
CO REGEN FLUE GAS CO2 REGEN FLUE GAS
PCT PCT
21261252:72PV
2126125 2:13 PM
21261252:74PM
2126125 2:15 PM
2126125 2:16 PM
21261252:77 PM
2126125 2:L8 PM
21261252:19 PM
21261252,,20PM
21261252.,27PM
21261252:22PM
21261252,,23PM
21261252:24PM
2t26t2s2;25PM
21261252:26PM
21261252:27 PM
21261252:28PM
21261252:29PM
2126125 2:30 PM
21261252:31PM
21261252:32PM
457L4.59
457L4.59
457L4.59
457t4.59
457L4.60
457L4.60
457L4.60
457L4.60
457t4.60
45774.60
45774.60
45774.60
45774.60
45774.60
45774.60
45774.60
45774.60
457L4.60
45774.60
457L4.67
45774.67
Calculated Avg:
ai100436.pv
1.91
2.0t
1.93
1.38
1.55
1.59
7.70
1.66
7.84
7.79
1.70
1.86
1.96
1.51
7.48
1.57
1.59
1.18
1.10
1.38
1.65
1.63
ai100438.pv
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
16.90
16.87
17.05
L7.18
L7.77
L7.07
17.09
17.00
16.92
17.00
17.03
16.95
16.94
L7.13
77.24
17.t6
17.20
t7.M
77.48
77.27
17.77
17.10
ffiorpnRTMENT oF
APR -2?0?_5 i
DIVISION OF AIR QUALITY
H-101 Nox 20252
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name Tesoro
Company Contact:Rheannon Schaefer
Contact Phone No.[phone]
Stack Designation:Crude Furnace H-101
Test & Review Dates
Test Date:2/18/2025 &
Review Date: 4/8/2025
Observer:
Reviewer:Paul Morris
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.0540 0.044
lbs./hr.
ppm
Percent
%O2 Correction as a whole #
Test Information Heat Input
Equivalent
Diameter (in.)As ft^2 Y Dl H @ Cp Pbar Pq (static)
fuel flow rate
(Btu/hr.)
Heat Input
(Btu/hr.)
FALSE
Contractor Information
Contact: Charles Horton
Contracting Company: Alliance Technical Group, LLC
Address: 3683 W 2270 S, Suite E West Valley City, UT 84120
Phone No.: [phone]
Project No.:
8531

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
Diluent
F factor used
O2
CO2
Anthrocite 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
H-101 Nox 20252
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Tesoro
Crude Furnace H-101
Average Emission
Dry SO2 NOX CO
lbs./MMbtu 0.044 Average % concentration
lbs./hr.CO2 O2
ppm or % 31.80 9.14 5.40
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)4.42E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.820E-06
lbs./hr.9.09 5.49
ppm or %31.98 9.17 5.52
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)4.34E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.790E-06
lbs./hr.9.18 5.33
ppm or %31.73 9.17 5.38 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)4.35E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 3.786E-06
lbs./hr.9.16 5.39
ppm or %31.70 9.23 5.44 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
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)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
C For Cal Drift
Raw Value
C For Cal Drift
C For Cal Drift
C For Cal Drift
C For Cal Drift
O2
CO2
Clear
lbs./MMBTU
H-101 Nox 20252
Calibration Error Test
Test Date February 18, 2025 O2
CS - Cal. Span 23.99
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.
RR02538 09/19/31 Mid-level 11.00 11.00 0.00 0.00% Passed Cal.
EB0069884 04/01/32 High-level 23.99 24.00 0.01 0.04% 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 45.85%
100% of Cal. Span High-level 100.00%
Test Date February 18, 2025 CO2
CS - Cal. Span 23.90
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 -0.05 0.05 0.209% Passed Cal.
RR02538 09/19/31 Mid-level 10.90 11.16 0.26 1.088% Passed Cal.
EB0069884 04/01/32 High-level 23.90 23.83 0.07 0.293% 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 45.61%
100% of Cal. Span High-level 100.00%
Test Date SO2
CS - Cal. Span
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level
Mid-level
High-level
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level
40 to 60% of Cal. Span Mid-level
100% of Cal. Span High-level
Test Date February 18, 2025 NOx
CS - Cal. Span 100.00
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
EB0011606 09/16/31 Mid-level 50.00 50.34 0.34 0.340% Passed Cal.
High-level 100.00 99.91 0.09 0.090% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 50.00%
100% of Cal. Span High-level 100.00%
Test Date CO
CS - Cal. Span
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level
Mid-level
High-level
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level
40 to 60% of Cal. Span Mid-level
100% of Cal. Span High-level
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
H-101 Nox 20252
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Crude Furnace H-101
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % % Unprotected
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 50.00 10.90 11.00
Calibration Error Test
Cs - Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.00 -0.05 0.00
Mid-Level 50.34 11.16 11.00
High-Level 99.91 23.83 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 50.34 11.16 11.00
Low-Level 0.00% 0.21% 0.00%
ppmdv Difference 0 0.05 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.34% 1.09% 0.00%
ppmdv Difference 0.34 0.26 0
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.09% 0.29% 0.04%
ppmdv Difference 0.09 0.07 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.02 -0.06 0.09 System Bias.
SBi - Zero Bias TRUE 0.02% TRUE 0.04% 0.38%± 5% of Span
Difference TRUE 0.02 TRUE 0.01 0.09
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 49.62 11.00 10.94
SBi - Up-Scale Bias TRUE 0.72% TRUE 0.67% 0.25%
Difference TRUE 0.72 TRUE 0.16 0.06
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/18/2025 SO2
SO2 NOX CO CO2 O2 NOX
31.9 9.2 5.5 CO
0.0% 31.9% 0.0% 38.4% 23.0%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.00 -0.05 0.13 System Bias.
SBi - Zero Bias TRUE 0.00% TRUE 0.00% 0.54%± 5% of Span
Difference TRUE 0.0 TRUE 0.0 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.06 11.02 10.96
SBi - Up-Scale Bias TRUE 0.28% TRUE 0.59% 0.17%
Difference TRUE 0.3 TRUE 0.1 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.02% TRUE 0.04% 0.17% Drift
Difference TRUE 0.0 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.44% TRUE 0.08% 0.08%
Difference TRUE 0.4 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Crude Furnace H-101 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 9.09 5.49 85.42 29.67 29.67
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws #NUM!
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs
(ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Drift Dialog
Failed Cal Error Dialog
CO Calibration Gas
Failed Bias Dialog
H-101 Nox 20252
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Crude Furnace H-101
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 50.00 10.90 11.00
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.00 -0.05 0.00
Mid-Level 50.34 11.16 11.00
High-Level 99.91 23.83 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 50.34 11.16 11.00
Low-Level 0.00% 0.21% 0.00%
ppmdv Difference 0 0.05 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.34% 1.09% 0.00%
ppmdv Difference 0.34 0.26 0
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.09% 0.29% 0.04%
ppmdv Difference 0.09 0.07 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.00 -0.05 0.13 System Bias.
SBi - Zero Bias TRUE 0.00% TRUE 0.00% 0.54%± 5% of Span
Difference TRUE 0 TRUE 0 0.13
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.06 11.02 10.96
SBi - Up-Scale Bias TRUE 0.28% TRUE 0.59% 0.17%
Difference TRUE 0.28 TRUE 0.14 0.04
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/18/2025 SO2
SO2 NOX CO CO2 O2 NOX
31.7 9.3 5.4 CO
0.0% 31.7% 0.0% 38.7% 22.4%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.01 -0.05 0.14 System Bias.
SBi - Zero Bias TRUE 0.01% TRUE 0.00% 0.58%± 5% of Span
Difference TRUE 0.0 TRUE 0.0 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 49.74 11.00 10.96
SBi - Up-Scale Bias TRUE 0.60% TRUE 0.67% 0.17%
Difference TRUE 0.6 TRUE 0.2 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.01% TRUE 0.00% 0.04% Response Spec.
Difference TRUE 0.0 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.32% TRUE 0.08% 0.00%
Difference TRUE 0.3 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Crude Furnace H-101 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 9.18 5.33 85.50 29.68 29.68
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Drift Dialog
Failed Cal Error Dialog
Failed Bias Dialog
H-101 Nox 20252
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Crude Furnace H-101
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 50.00 10.90 11.00
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.00 -0.05 0.00
Mid-Level 50.34 11.16 11.00
High-Level 99.91 23.83 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 50.34 11.16 11.00
Low-Level 0.00% 0.21% 0.00%
ppmv Difference 0 0.05 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.34% 1.09% 0.00%
ppmv Difference 0.34 0.26 0
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.09% 0.29% 0.04%
ppmv Difference 0.09 0.07 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.01 -0.05 0.14 System Bias.
SBi - Zero Bias TRUE 0.01% TRUE 0.00% 0.58%± 5% of Span
Difference TRUE 0.01 TRUE 0 0.14
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 49.74 11.00 10.96
SBi - Up-Scale Bias TRUE 0.60% TRUE 0.67% 0.17%
Difference TRUE 0.6 TRUE 0.16 0.04
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/18/2025 SO2
SO2 NOX CO CO2 O2 NOX
31.6 9.2 5.4 CO
0.0% 31.6% 0.0% 38.6% 22.7%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.01 -0.08 0.15 System Bias.
SBi - Zero Bias TRUE 0.01% TRUE 0.13% 0.63%± 5% of Span
Difference TRUE 0.0 TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 49.94 10.99 10.96
SBi - Up-Scale Bias TRUE 0.40% TRUE 0.71% 0.17%
Difference TRUE 0.4 TRUE 0.2 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.00% TRUE 0.13% 0.04% Response Spec.
Difference TRUE 0.0 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.20% TRUE 0.04% 0.00%
Difference TRUE 0.2 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Crude Furnace H-101 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 9.16 5.39 85.45 29.68 29.68
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Cal Error Dialog
Failed Drift Dialog
Failed Bias Dialog
UFU Nox 2025
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name Tesoro
Company Contact:Rheannon Schaefer
Contact Phone No.[phone]
Stack Designation:Ultraformer Furnace F-1
Test & Review Dates
Test Date:2/17/2025 &
Review Date: 4/8/2025
Observer:
Reviewer:Paul Morris
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.0650 0.036
lbs./hr.
ppm
Percent
%O2 Correction as a whole #
Test Information Heat Input
Equivalent
Diameter (in.)As ft^2 Y Dl H @ Cp Pbar Pq (static)
fuel flow rate
(Btu/hr.)
Heat Input
(Btu/hr.)
FALSE
Contractor Information
Contact: Charles Horton
Contracting Company: Alliance Technical Group, LLC
Address: 3683 W 2270 S, Suite E West Valley City, UT 84120
Phone No.: [phone]
Project No.:
8489

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
Diluent
F factor used
O2
CO2
Anthrocite 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
UFU Nox 2025
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Tesoro
Ultraformer Furnace F-1
Average Emission
Dry SO2 NOX CO
lbs./MMbtu 0.036 Average % concentration
lbs./hr.CO2 O2
ppm or % 23.05 8.03 7.43
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)3.67E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.775E-06
lbs./hr.8.01 7.47
ppm or %23.23 8.10 7.49
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)3.61E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.744E-06
lbs./hr.8.05 7.41
ppm or %22.97 8.10 7.44 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)3.61E-02 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 2.741E-06
lbs./hr.8.02 7.41
ppm or %22.95 8.15 7.45 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
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)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft
lbs./hr.
ppm or %Raw Value
C For Cal Drift
Raw Value
C For Cal Drift
C For Cal Drift
C For Cal Drift
C For Cal Drift
O2
CO2
Clear
lbs./MMBTU
UFU Nox 2025
Calibration Error Test
Test Date February 17, 2025 O2
CS - Cal. Span 23.99
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.
RR02538 09/19/31 Mid-level 11.00 11.02 0.02 0.08% Passed Cal.
EB0069884 04/01/32 High-level 23.99 24.00 0.01 0.04% 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 45.85%
100% of Cal. Span High-level 100.00%
Test Date February 17, 2025 CO2
CS - Cal. Span 23.90
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 -0.03 0.03 0.126% Passed Cal.
RR02538 09/19/31 Mid-level 10.90 11.19 0.29 1.213% Passed Cal.
EB0069884 04/01/32 High-level 23.90 23.87 0.03 0.126% 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 45.61%
100% of Cal. Span High-level 100.00%
Test Date SO2
CS - Cal. Span
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level
Mid-level
High-level
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level
40 to 60% of Cal. Span Mid-level
100% of Cal. Span High-level
Test Date February 17, 2025 NOx
CS - Cal. Span 100.00
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.01 0.01 0.010% Passed Cal.
EB0011606 09/16/31 Mid-level 50.00 49.28 0.72 0.720% Passed Cal.
High-level 100.00 100.00 0.00 0.000% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 50.00%
100% of Cal. Span High-level 100.00%
Test Date CO
CS - Cal. Span
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level
Mid-level
High-level
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level
40 to 60% of Cal. Span Mid-level
100% of Cal. Span High-level
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
Valid Cal Gas
UFU Nox 2025
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Ultraformer Furnace F-1
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % % Unprotected
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 50.00 10.90 11.00
Calibration Error Test
Cs - Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.01 -0.03 0.00
Mid-Level 49.28 11.19 11.02
High-Level 100.00 23.87 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 49.28 11.19 11.02
Low-Level 0.01% 0.13% 0.00%
ppmdv Difference 0.01 0.03 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.72% 1.21% 0.08%
ppmdv Difference 0.72 0.29 0.02
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.00% 0.13% 0.04%
ppmdv Difference 0 0.03 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.29 -0.01 0.15 System Bias.
SBi - Zero Bias TRUE 0.28% TRUE 0.08% 0.63%± 5% of Span
Difference TRUE 0.28 TRUE 0.02 0.15
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.64 11.03 10.94
SBi - Up-Scale Bias TRUE 1.36% TRUE 0.67% 0.33%
Difference TRUE 1.36 TRUE 0.16 0.08
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/17/2025 SO2
SO2 NOX CO CO2 O2 NOX
23.6 8.1 7.5 CO
0.0% 23.6% 0.0% 33.9% 31.2%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.43 -0.04 0.17 System Bias.
SBi - Zero Bias TRUE 0.42% TRUE 0.04% 0.71%± 5% of Span
Difference TRUE 0.4 TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.25 11.04 10.97
SBi - Up-Scale Bias TRUE 0.97% TRUE 0.63% 0.21%
Difference TRUE 1.0 TRUE 0.2 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.14% TRUE 0.04% 0.08% Drift
Difference TRUE 0.1 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.39% TRUE 0.04% 0.13%
Difference TRUE 0.4 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Ultraformer Furnace F-1 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 8.01 7.47 84.52 29.58 29.58
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws #NUM!
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs
(ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Drift Dialog
Failed Cal Error Dialog
CO Calibration Gas
Failed Bias Dialog
UFU Nox 2025
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Ultraformer Furnace F-1
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 50.00 10.90 11.00
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.01 -0.03 0.00
Mid-Level 49.28 11.19 11.02
High-Level 100.00 23.87 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 49.28 11.19 11.02
Low-Level 0.01% 0.13% 0.00%
ppmdv Difference 0.01 0.03 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.72% 1.21% 0.08%
ppmdv Difference 0.72 0.29 0.02
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.00% 0.13% 0.04%
ppmdv Difference 0 0.03 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.43 -0.04 0.17 System Bias.
SBi - Zero Bias TRUE 0.42% TRUE 0.04% 0.71%± 5% of Span
Difference TRUE 0.42 TRUE 0.01 0.17
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.25 11.04 10.97
SBi - Up-Scale Bias TRUE 0.97% TRUE 0.63% 0.21%
Difference TRUE 0.97 TRUE 0.15 0.05
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/17/2025 SO2
SO2 NOX CO CO2 O2 NOX
23.3 8.2 7.4 CO
0.0% 23.3% 0.0% 34.1% 31.0%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.46 -0.02 0.18 System Bias.
SBi - Zero Bias TRUE 0.45% TRUE 0.04% 0.75%± 5% of Span
Difference TRUE 0.5 TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.19 11.06 10.96
SBi - Up-Scale Bias TRUE 0.91% TRUE 0.54% 0.25%
Difference TRUE 0.9 TRUE 0.1 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.03% TRUE 0.00% 0.04% Response Spec.
Difference TRUE 0.0 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.06% TRUE 0.08% 0.04%
Difference TRUE 0.1 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Ultraformer Furnace F-1 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 8.05 7.41 84.55 29.58 29.58
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Drift Dialog
Failed Cal Error Dialog
Failed Bias Dialog
UFU Nox 2025
Division of Air Quality Stack Test Review of
Tesoro
SO2 NOX CO CO2 O2 Ultraformer Furnace F-1
CS Calibration Span 100.00 23.90 23.99
Units ppm ppm ppm % %
CV - Cylinder Value:SO2 NOX CO CO2 O2
Low-Level 0.00 0.00 0.00
Mid-Level 50.00 10.90 11.00
High-Level 100.00 23.90 23.99
0 to 20% of Cal. Span 0.00% 0.00% 0.00%
40 to 60% of Cal. Span 50.0% 45.6% 45.9%
100% of Cal. Span 100.0% 100.0% 100.0%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CMA 50.00 10.90 11.00
Calibration Error Test
Measured Concentration SO2 NOX CO CO2 O2
Low-Level 0.01 -0.03 0.00
Mid-Level 49.28 11.19 11.02
High-Level 100.00 23.87 24.00
Enter Up-scale Analyzer Response to be used during testing.
ACE Eq. 7E-1 49.28 11.19 11.02
Low-Level 0.01% 0.13% 0.00%
ppmv Difference 0.01 0.03 0
Status Passed Cal. Passed Cal.Passed Cal.
Mid-Level 0.72% 1.21% 0.08%
ppmv Difference 0.72 0.29 0.02
Status Passed Cal. Passed Cal.Passed Cal.
High-Level 0.00% 0.13% 0.04%
ppmv Difference 0 0.03 0.01
Status Passed Cal. Passed Cal.Passed Cal.
Pre-Test Sampling System Bias
Initial Values SO2 NOX CO CO2 O2
CO - Low-Level 0.46 -0.02 0.18 System Bias.
SBi - Zero Bias TRUE 0.45% TRUE 0.04% 0.75%± 5% of Span
Difference TRUE 0.45 TRUE 0.01 0.18
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.19 11.06 10.96
SBi - Up-Scale Bias TRUE 0.91% TRUE 0.54% 0.25%
Difference TRUE 0.91 TRUE 0.13 0.06
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:2/17/2025 SO2
SO2 NOX CO CO2 O2 NOX
23.3 8.2 7.5 CO
0.0% 23.3% 0.0% 34.1% 31.1%CO2/O2
Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100
Final Values SO2 NOX CO CO2 O2
CO - Low-Level 0.42 -0.03 0.17 System Bias.
SBi - Zero Bias TRUE 0.41% TRUE 0.00% 0.71%± 5% of Span
Difference TRUE 0.4 TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 50.22 11.10 10.98
SBi - Up-Scale Bias TRUE 0.94% TRUE 0.38% 0.17%
Difference TRUE 0.9 TRUE 0.1 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Drift % of Span - D=ABS(SBf - SBi)
Low-Level Drift TRUE 0.04% TRUE 0.04% 0.04% Response Spec.
Difference TRUE 0.0 TRUE 0.0 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Gas Drift TRUE 0.03% TRUE 0.17% 0.08%
Difference TRUE 0.0 TRUE 0.0 0.0
Pass or Re-Calibrate Pass Pass Pass
Ultraformer Furnace F-1 Flow & Moisture
As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms
FALSE 0.00 0.00 0.00 8.02 7.41 84.56 29.58 29.58
Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws
0.0000 #DIV/0! 0.999
Load - Megawatts
Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh
Heat Input
Btu/hr Low Mid High
Enert >
#1 - Times
Date
Failed Bias Dialog
Failed Cal Error Dialog
Failed Drift Dialog
Failed Bias Dialog