DAQ-2025-003350

1
DAQC-671-25
Site ID 10917 (B4)

MEMORANDUM

TO: STACK TEST FILE – COMPASS MINERALS

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Rob Leishman, Environmental Scientist

DATE: July 10, 2025

SUBJECT: Source: Boiler #1 and #2
Contact: Ian Wright – 801-732-3011
Location: 765 North 10500 West, Ogden, Weber County, UT
Test Contractor: Mostardi Platt
FRS ID#: UT00000049005700001
Permit/AO#: Operating Permit #5700001004 dated June 10, 2021
Last Revised December 15, 2023
Action Code: TR
Subject: Review of RATA and Stack Test Report dated
December 23, 2024

On January 7, 2025, Utah Division of Air Quality (DAQ) received a test report for the Compass Minerals
Boiler #1 and Boiler #2 stacks. Testing was performed on October 17, 2024, and October 23, 2024, to
demonstrate compliance with the emission limits found in Condition II.B.20.a. The DAQ calculated test
results are:

Source Test Date Test Method Pollutant Result Limit

Boiler #1 10/23/2024 Method 7E NOX 0.8 lb/hr 1.3 lb/hr
6.4 ppm 9.0 ppm

Boiler #2 10/17/2024 Method 7E NOX 0.7 lb/hr 1.3 lb/hr
5.8 ppm 9.0 ppm

DEVIATIONS: No deviations were noted in the report.

CONCLUSION: Compass Minerals was in compliance with the NOX emissions limits at
the time of the test.

RECOMMENDATION: Compass Minerals has demonstrated compliance with the NOX emissions
limits of the Title V operating permit for Boiler #1 and Boiler #2.

HPV: No.

ATTACHMENTS: Stack Test and RATA report, Stack Test review sheets.

1 8 2
Compass Minerals
765 N 10500 W
Ogden, UT 84404
www.com passminerals.com
r [phone]
December 23'd,2024
Mr. Bryce Bird
Utah Department of Environmental Quality
Division of Air Quality
195 North 1950 West
Salt Lake City, Utah 84115
RE: Source Test Report and Relative Accuracy Test Audit Results
Compass Minerals Ogden lnc. (Operating Permit No. 5700001004)
DIVISION OF AIR QUALITY
Mr. Bird,
Enclosed please find the final report for testing completed for Boiler No. 1 and Boiler No. 2 located at
Compass Minerals Ogden, lnc. This testing demonstrated compliance with the NOx emission limits found
in Operating Permit condition ll.B.21.and the Relative Accuracy Test Audit (RATA) required in 40 CFR Part
60, Subpart Db and performance specifications (PS) 2 and 3 as outlined in 40 CFR Part 50, Appendix B.
Testing was completed on October 17th and October 23d,2024 pursuant to the Site-SpecificTest Plan
approved by UDAQ on August 28th,2024. Test results demonstrated compliance with both the emission
limits found in the Operating Permit and the RATA performance specifications.
As the Responsible Official for this facility, I certify that:
o Testing was conducted while the source was operating within 90% of the maximum production
rate achieved in the previous 12 months,
o 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 Director, and
o Based on information and belief formed after reasonable inquiry, the statements and
information in this document are true, accurate, and complete.
Please contact lan Wright ([e-mail], [phone]) if you have any questions
regarding the information provided.
Respectfu lly,
EaMp r€.rzrt4-
Brandon Risner
Vice President, Operations
Compass Minerals Ogden lnc.
u-r i\I I r,ri- I'AFr llli:ti-r?)F
El!!]R0J.ilEr.J rl.l_ eiJAr tTyf--- -= I
Gontinuous Emissions
Monitoring System
Relative Accuracy Test
Audit and Gompliance Test
Report
Compass Minerals Ogden, lnc.
Boiler #1 Stack and Boiler #2 Stack
765 North 10500 West
Ogden, Utah 84404
Utah Division of Air Quality (UDAO)
Title V Operating Permit #5700001004
Report No. M2442068
October 17 and 23,2024
UJ-(d
frl
9.,$
r{tl-{(d
{r,ao
E
mostardi?platt
Relative Accuracy Test Audit and Gompliance Test Report
Compass Minerals Ogden, lnc.
Boiler #1 Stack and Boiler #2 Stack
765 North 10500 West
Ogden, Utah 84404
Utah Division of Air Quality (UDAO)
Title V Operating Permit # 5700001004
Report Submittal Date
December 17,2024
Submitted By
(Z-'."L- S{t-
Richard J. Sollars ll
[phone], Phone
[e-mail], Email
@ Copyright2024
All rights reserved in
Mostardi Platt
?'.5i?* oFArR nri,,r"
No. M2442OGB
TABLE OF CONTENTS
1.0 EXECUTTVE SUMM4RY........... ...........................1
2.0 PROCESS DESCRrprON.............. ......................2
Table 2-1: CEMS Descriptions ...........2
3.0 SUMMARY OF TEST RESULTS .........3
4.0 TEST METHODOLOGY............ ...........4
4.1 Method 1 Sample and Velocity Traverse Determination.................. ........4
4.2 Method 2 Gas Velocity Determination............. ....................4
4.3 Method 3A Oxygen (Oz)/Carbon Dioxide (COz) Determination......... ...........................4
4.4 Method 4 Moisture (HzO) Determination ..........5
4.5 Method 7E Nitrogen Oxides (NOx) Determination ...............5
5.0 TEST RESULT SUMMARIES ..............6
5.1 RATA Summary Tab1es......... ...........................6
5.2 Compliance Summary Tables .................. .....10
APPENDICES
Appendix A - Test Section Diagrams..... .............. 13
Appendix B - Sample Train Diagrams ............... ......................17
Appendix C - Calculation Nomenclature and Formulas..... ......21
Appendix D - Reference Method Test Data.... ........................30
Appendix E - Continuous Emissions Monitoring System Data and Plant Operating Data..................69
Appendix F - Field Data Sheets .......94
Appendix G - Calibration and Response Time Data... ...........127
Appendix H - Calibration Gas Cylinder Data............ ....... ... 148
Appendix I - NOz to No Converter Test....... ....... 153
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
OMostardi Platl
1.0 EXECUTIVE SUMMARY
Mostardi Platt conducted a Continuous Emissions Monitoring System (CEMS) Relative Accuracy
Test Audit (RATA) program for Compass Minerals Ogden, lnc. at the facility located in Ogden,
Utah on the Boiler #1 Stack on October 23,2024, and Boiler #2 Stack on October 17,2024.
Additionally, a compliance emission test on the NO, concentration and emission rates from the
exhaust of the test locations were performed. Three RATA runs were combined to form one
compliance run. This report summarizes the results of the test program and test methods utilized.
This test program was completed to satisfy the requirements found in United States
Environmental Protection Agency (USEPA) Title 40, Code of Federal Requlations, (40CFR); the
applicable federal, state, and local agency; and, the applicable facility specific operating and Title
V Operating Permit # 5700001004.
The test locations, test dates, and test parameters are summarized below.
The identifications of the individuals associated with the test program are summarized below.
The test crew consisted of R. Bocanegra, J. Colston, G. Mills, A. Robles, and Rich Sollars of
Mostardi Platt.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
RATA TEST INFORMATION
Test Locations Test Dates Test Parameters
Boiler #1 Stack October 23,2024
Carbon Dioxide (COz), Oxygen (Oz), Nitrogen
Oxides (NO,), Moisture (HzO), and Volumetric
Flow Rate
Boiler #2 Stack October 17,2024 COz, Oz, NO,, HzO, and Volumetric Flow Rate
TEST PERSONNEL INFORMATION
Location Address Contact
Test Facility Compass Minerals Ogden, lnc.
765 North 10500 West
Ogden, UT 84404
Holly Hurst
Director, Environmental Compliance
[phone]
HurstH@com oassminerals. com
Testing Company
Representative
Mostardi Platt
702 West 48h Avenue
Denver, CO 80216
Richard J. Sollars
Vice President - AET West Region
(630) 993-21 00
[e-mail]
Page 1 of 157 OMostardi Platt
2.0 PROCESS DESCRIPTION
Compass operates a mineral recovery facility on the eastern shore of the south arm of the Great
Salt Lake near Ogden, Utah in Weber County. This facility produces sodium chloride (NaCl),
sulfate of potash (SOP) (KzSO+), and magnesium chloride (MgClz). The process uses crystallized
salts, including halite (sodium chloride) and a mixed salt containing potassium sulfate and
magnesium sulfate from solar evaporation ponds. The raw halite is washed, wet-screened, dried,
cooled, dry-screened, packages, and shipped. The mixed salt is washed, slurried, thickened,
crystallized, and converted to schoenite which is then filtered, dried, screened, half
granulated/compacted and shipped as sulfate of potash.
Boiler #1 and Boiler #2 are in the sulfate of potash (SOP) plant; each boiler is rated at 108.1 1
MMBtu/hr and is equipped with ultra-low NO, burners, internal flue gas recirculation and
continuous oxygen trim systems that maintain an optimum air to fuel ratio.
Table 2-1: CEMS Descriptions
Project No. M2442068
Boiler #l Stack and Boiler #2 Stack
Test Location Pollutant Make Model Serial No.Soan
Boiler #1 NO,ABB URAS 26 o24'.1708662t1000 0-75 ppm (low)
0-500 oom (hioh)
Oz ABB Maonos 206 0242165372t1000 0-100%
Boiler #2
NO"ABB URAS 26 0241708662t1000 0-75 ppm (low)
0-500 ppm (hiqh)
Oz ABB Maonos 206 0242165372t1000 0-100%
Page 2 of 157 @Mostardi Platt
3.0 SUMMARY OF TEST RESULTS
The test results from this program indicate that each CEMS meets the USEPA performance
specification (PS) for relative accuracy as published in 40CFR60. A summary of the test results
can be found below.
The following tables present the parameters tested, performance specifications and
requirements, and relative accuracy of each CEMS component:
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
RATA RESULTS SUMMARY
Test
Location Parameter Test Method Units
Required Performance
Criteria
Relative
Accuracy
Boiler #1
Stack
NOx USEPA Method 3A,
7E and 19 lb/MMbtu 310o/o RA of the applicable
standard of 0.20 lb/MMBtu 0.56%
o2 USEPA Method 3A % dry 3 20o/o RA of the mean
reference value 2.33%
Boiler #2
Stack
NOx USEPA Method 3A,
7E and 19 lb/MMbtu 3 10o/o RA of the applicable
standard of 0.20 b/MMBtu 0.00%
o2 USEPA Method 3A %dry s 20o/o RA of the mean
reference value 0.670/0
COMPLIANCE RESULTS SUMMARY
Test Location Parameter Test Methods Pollutant Limit Test Results
Boiler #1 Stack
NOx USEPA Methods 1, 2,
3A, 4, and 7E
9.0 ppmvd
1.30 lb/hr
6.4 ppmvd
0.84 lb/hr
Boiler #2 Stack 9.0 ppmvd
1.30 lb/hr
5.9 ppmvd
O.77lblhr
Page 3 of 157 @Mostardi Platt
4.0 TEST METHODOLOGY
Emission testing was conducted following the USEPA methods specified in 40CFR60 in addition
to the Mostardi Platt Quality Manual. Schematics of the test section diagrams and sampling trains
used are included in Appendix A and B respectively. Calculation nomenclature is included in
Appendix C. Copies of analyzer print-outs for each test run are included in Appendix D. CEM data
and process data as provided by Compass Minerals Ogden, lnc. are included in Appendix E.
The following methodologies were used during the test program:
4.1 Method 1 Sample and Velocity Traverse Determination
Test measurement points were selected in accordance with USEPA Method 1, 40CFR60,
Appendix A. The characteristics of the measurement location is summarized below.
4.2 Method 2 Gas Velocity Determination
Gas velocity was measured following USEPA Method 2, 40CFR60, Appendix A, for purposes of
calculating stack gas volumetric flow rate and emission rates on a lb/ton basis. An S-type pitot
tube, 0-1O-inch differential pressure gauge, and Ktype thermocouple and temperature readout
were used to determine gas velocity at each sample point. Prior to beginning testing an absence
of cyclonic flow traverse was conducted.
All of the equipment used was calibrated in accordance with the specifications of the Method.
Copies of field data sheets are included in Appendix F. Calibration data are presented in Appendix
G. This testing met the performance specifications as outlined in the Method.
4.3 Method 3A Oxygen (Oz)/Carbon Dioxide (COz) Determination
Stack gas Oz and COz concentrations and emission rates were determined in accordance with
USEPA Method 3A, 40CFR60, Appendix A. A California Analytical analyzer was used to determine
the Oz and COz concentrations in the manner specified in the Method. The instrument has a
paramagnetic detector and the 02 operates in the nominal range of O% lo 25% with the specific
range determined by the high-level calibration gas and the COz operates in the nominal range of
0 to 25o/o with the specific range determined by the high-level calibration gas. High-range
calibrations were performed using USEPA Protocol gas. Zero nitrogen (a low ppm pollutant in
balance nitrogen calibration gases) was introduced during other instrument calibrations to check
instrument zero. High- and a mid-range o/o Oz and COz levels in balance nitrogen were also
introduced. Zero and mid-range calibrations were performed using USEPA Protocol gas after
each test run. This testing met the performance specifications as outlined in the Method.
Calibration data are presented in Appendix G and copies of the gas cylinder certifications are
found in Appendix H.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
SAMPLE POINT SELECTION
Test Location
Stack
Diameter
Upstream
Distance
Downstream
Distance Test Parameters
Number of
Sampling
Points
Boiler Stack #1
and Boiler Stack
#2
3.33 feet 9.0
diameters 4.5 diameters
Oz, COz, NOx Stratification: '12
Test Runs: 3
Volumetric Flowrate 16
Page 4 of 157 @Mostardi Platt
4.4 Method 4 Moisture (HzO) Determination
Stack gas moisture content was determined using a Method 4 sampling train. ln this technique,
stack gas was drawn through a series of four impingers. The entire impinger train was
measured/weighed before and after each test run to determine the mass of moisture condensed.
All of the equipment used was calibrated in accordance with the specifications of the Method.
Calibration data will be appended to the final report.
4.5 Method 7E Nitrogen Oxides (NOx) Determination
Stack gas NOx concentrations and emissron rates were determined in accordance with USEPA
Method 7E, 40CFR60, Appendix A. A California Analytical Chemiluminescence Nitrogen Oxides
Analyzer was used to determine nitrogen oxides concentrations, in the manner specified in the
Method. The instrument operated in the nominal range of 0 ppm to 20 ppm with the specific range
determined by the high-level span calibration gas.
The CAI 700 LX operates on the principle that nitric oxide (NO) and ozone (Os) react to produce
a characteristic luminescence with an, intensity linearly proportional to the NO concentration.
lnfrared light emission results when electronically excited NOz molecules decay to lower energy
states. Specifically,
NO+O. -+NO, +O, +h,,
where h,, = light
Nitrogen dioxide (NOz) must first be transformed into NO before it can be measured using the
chemiluminescent reaction. NOz is converted to NO by a molybdenum NOzto-NO converter
heated to about 326"C at the Boiler #1 Stack and to about 315"C at the Boiler #2 Stack. The flue
gas sample is drawn into the CAI 700 LX through the sample bulkhead. The sample flows through
a capillary, and then to the mode solenoid valve. The solenoid valve routes the sample either
straight to the reaction chamber (NO mode) or through the NOzto-NO converter and then to the
reaction chamber (NOx mode). A flow sensor prior to the reaction chamber measures the sample
flow. Dry air enters the CAI 700LX through the dry air bulkhead, passes through a flow switch,
and then through a silent discharge ozonator. The ozonator generates the ozone needed for the
chemiluminescent reaction. At the reaction chamber, the ozone reacts with the NO in the sample
to produce excited NOz molecules. A photomultiplier tube (PMT) housed in a thermoelectric cooler
detects the luminescence generated during this reaction. From the reaction chamber, the exhaust
travels through the ozone (Os) converter to the pump, and is released through the vent.
The NO and NOx concentrations calculated in the NO and NOx modes are stored in memory. The
difference between the concentrations is used to calculate the NOz concentration. The CAI 700
LX outputs NO, NOz, and NOx concentrations to the front panel display, the analog outputs, and
also makes the data available over the serial or ethernet connection.
Stack gas was delivered to the analyzer via a Teflon@ sampling line, heated to a minimum
temperature of 250"F. Excess moisture in the stack gas was removed using a refrigerated
condenser. The entire system was calibrated in accordance with the Method, using USEPA
Protocol gases introduced at the probe, before and after each test run. This testing met the
performance specifications as outlined in the Method.
A list of calibration gases used and the results of all calibration and other required quality
assurance checks are found in Appendix G. Copies of the gas cylinder certifications are found in
Appendix H. The NOz to NO converter test can be found in Appendix l. This testing met the
performance specifications as outlined in the Method.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 5 of 157 @Mostardi Platl
5.0 TEST RESULT SUMMARIES
5.1 RATA Summary Tables
A average enissions are < 50% of the applicable std (0.20 lb/lvtt/btu tlOx), the enission standard value nust be used in the denoninator
to clculate the RA, rather than the nEan of the RM.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Client: Compass Minerals Ogden, lnc
Facility: Ogden Plant
Project #: M244206
Fuel Type: Natural Gas
Location: Boiler #1 Stack
Date: 10123124
Test Method: 7E, 34
Fuel Factor: 8710
Applicable Standard 0.20
02 based NOx lb/mmBtu RATA
CEM Analvzer lnformation
NO" Monitor/Model:ABB URAS 26 NO. Serial #:0241708662t1000
02 Monitor/Model:ABB Maqnos 206 02 Serial #:o242165372t1000
1 =accept
0=reject
Test
Run test Date Start Time End Time RM NO,
lb/MMBtu
cEM NOx
lb/MMBtu
(RM-CEM)
Difference
(di)
(RM€EM)
Differencea
(di21
1 1 10t23t24 09:25 09:45 0.009 0.008 0.001 0.000001
1 2 10t23t24 09:46 10:06 0.009 0.008 0.001 0.000001
1 3 10t23t24 10:07 1O:27 0.009 0.008 0.001 0.000@1
1 4 10t23t24 10.40 11:00 0.009 0.008 0.001 0.000001
1 5 10t23t24 11:01 1121 0.009 0.008 0.001 0.000001
1 6 10t23t24 11:22 11.42 0.009 0.008 0.001 0.000001
1 7 10123t24 11:55 12.15 0.008 0.008 0.000 0.000000
1 I 10t23124 12.16 12.36 0.009 0 008 0.001 0.000001
0 9 10t23t24 12:37 12:57 0 009 0.008 0.001 0.000001
0 10 10t23t24 13: 15 1 3:35 0.009 0 008 0.001 0.000001
0 11 10t23t24 13:36 1 3:56 0.009 0.008 0.001 0.000001
1 12 10t23t24 13 57 14 17 0.008 0.008 0.000 0.000000
n 9
(0.975)2.306
Mean Reference Method Value 0.009 RM avq
Mean CEM Value 0.008 CEM avq
Sum of Differences 0.007 di
Mean Difference 0.001 d
Sum of Differences Squared 0.000 li2
Standard Deviation 0.000 rd
Confi de nce Coeflicie nt 2.5o/o Error fi taill 0.0(x):c
Relative Accuracv . APS 0.55 IAA
Page 6 of 157 OMostardi Platt
Client: Compass Minerals Ogden,
Facility: Ogden Plant
Project #: M244206
lnc. Location: Boiler #1
Date: 10123124
Test Method: 3A
Oz% ldryl RATA
CEM Analvzer lnformation
Stack
O, Monitor/Model:ABB Magnos 206 O, Seria! # :0242165372t',tOOO
1 =acce pt
0=reject
Test
Run
Test
Date Start Time End Time RM02%
(dry)
cEM 02 %
(drv)
(RM4EM)
Difference
(di)
(RM-cEM)
Difference2
(di2)
1 1 10t23124 09:25 09:45 4.9 5.0 -0.1 0.01
1 2 10t23t24 09:46 10:06 5.0 5.0 0.0 0.00
1 3 10t23t24 '10:07 10.27 4.9 5.0 {.1 0.01
1 4 10t23t24 10:40 11:00 4.9 5.0 -0.1 0.01
1 5 10t23t24 11:01 11:21 4.9 5.0 4.1 0.01
1 6 10t23t24 11:22 11 42 4.9 5.0 4.'l 0.01
1 7 10t23124 1 1:55 12:15 4.9 5.0 -0.1 0.01
1 8 10123124 12:16 12:36 4.9 5.0 {.1 0.01
1 9 10t23t24 12:37 12:57 4.9 5.0 -0.1 0,01
0 10 10t23t24 13:15 13:35 4.9 5.0 {.1 0.01
0 11 10t23t24 13:36 13:56 4.9 5.0 {.1 0.01
0 12 10t23t24 13:57 14:17 4.9 5.0 {.'l 0.01
n 9
t(0.9751 2.306
Mean Reference Method Value 4.911 RM avo
Mean CEM Value 5.000 CEM avo
Sum of Differences {.800 di
Mean Difference {.089 d
Sum of Differences Squared 0.080 di2
Standard Deviation 0.033 sd
Confi dence Coefficient 2.5o/o Error (1 -ta i !)0.026 cc
Relative Accuracv 2.33 RA
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 7 of 157 @Mostardi Platt
Client: Compass Minerals Ogden,
Facility: Ogden Plant
Project #: M244206
Fuel Type: Natural Gas
lnc. Location; Boiler#2 Stack
Date: 10117124
Test Method: 7E, 3A
Fuel Factor: 8710
Applicable Standard: 0.20
02 based NOx lb/mmBtu RATA
CEM Analvzer lnformation
NO, Monitor/Model:ABB Uras 26 NO, Serial #:0241708662/1000
02 Monitor/Model:ABB Maqnos 206 02 Serial #:0242165372t1000
1=accept
0=reject
Tes(
Run Test Date Start Time End Time RM NOI
lb/MMBtu
cEM NOx
lb/MMBtu
(RM.cEM)
Difference
(di)
(RM-cEM)
Difference2
(di2)
1 1 10t17t24 07.40 08:00 0.008 0.008 0 000 0 000000
1 2 10t17t24 08:01 08:21 0.008 0 008 0.000 0 000000
1 3 10t17t24 0822 08:42 0.008 0.008 0 000 0 000000
1 4 10t17t24 08:53 09:13 0.008 0 008 0.000 0.000000
0 5 10t17t24 09:14 09:34 0.009 0.008 0.001 0.000001
1 6 10t17t24 09:35 09:55 0.008 0.008 0.000 0.000000
1 7 10t17t24 10:08 10.28 0 008 0.008 0.000 0.000000
1 8 10t17t24 10:29 10:49 0.008 0.008 0.000 0.000000
1 I 10t17t24 10:50 11:10 0.008 0 008 0.000 0.000000
1 '10 10t'17t24 11 20 11 40 0.008 0.008 0 000 0 000000
0 11 10t17t24 11 41 12.O1 0.008 0.008 0 000 0.000000
0 12 10t17t24 12:02 12'22 0.008 0.008 0.000 0.000000
n 9
t(0.975)2.306
Mean Reference Method Value 0.008 RM avo
Mean CEM Value 0.008 CEM avo
Sum of Differences 0.000 di
Mean Difference 0.000 d
Sum of Differences Squared 0.000 di2
Standard Deviation 0.000 sd
Confi de nce Coefficie nt 2.5Yo Error (1 -ta il I 0.000 cc
Relative Accuracy - APS 0.00 RAA
A average emisionsare < 50% of the applicable Cd (0.20 lb/MMbtu NOx), the emission $andard value mu9 be ued in the denominator
to clculate the RA, rather than the mean of the RM.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 8 of 157 @Mostardi Platt
Client: Compass Minerals Ogden,
Facility: Ogden Plant
Project #: M24426
lnc. Location:
Date:
Test Method:
Oz % (dry) RATA
CEM Analvzer !nformation
Boiler #2 Stack
10t17t24
3A
O, Monitor/Model:ABB Magnos 206 Or Serial #:024216537211000
1 =acce pt
0=reject
Test
Run
Tes(
Date Start Time End Time RM02%
(drv)
CEM O2o/o
(drv)
(RM4EM)
Difference
(di)
(RM4EM)
Difference2
(di2)
0 1 10117124 07:40 08:00 5.4 5.5 -0.1 0.01
1 2 10117124 08:01 08:21 5.5 5.5 0.0 0.00
0 3 10t17t24 08:22 08:42 5.4 5.5 -0.1 0.01
1 4 10t17t24 08:53 09:1 3 5.5 5.5 0.0 0.00
0 5 10117t24 09:'14 09:34 5.5 5.6 {.1 0.01
1 6 10117124 09:35 09:55 5.5 5.6 {.1 0.01
1 7 10117t24 '10:08 10:28 5.5 5.5 0.0 0.00
I 8 10t17124 10:29 10:49 5.5 5.5 0.0 0.00
1 o 10117t24 '10:50 11:10 5.5 5.5 0.0 0.00
10 10t17124 11:20 11:40 5.5 5.5 0.0 0.00
I 11 10t17t24 't't:41 12:01 5.5 5.5 0.0 0.00
1 12 10t17124 12:02 12:22 5.5 5.5 0.0 0.00
n 9
t(0.975)2.306
Mean Reference Method Value 5.500 RM avo
Mean CEM Value 5.511 CEM avo
Sum of Difrerences 4.100 di
Mean Difference 4.011 d
Sum of Differences Squared 0.010 di2
Standard Eleviation 0.033 sd
Confi de nce Coefficie nt 2.5o/o Error (1 -ta i l)0.026 cc
Relative Accuracy 0.67 RA
Project No. M2442068
Boiler #'1 Stack and Boiler #2 Stack
Page 9 of 157 @Mostardi Platt
5.2 Compliance Summary Tables
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
Reference Method Test Data
Test No.Date
Start
Time
End
Time
NOr,
oomvd
Volumetric
Flow dscfrn NOx !b/hr
1 10t23t2024 9:25 9:45 6.7 18152 0.87
2 10t23t2024 9:46 '10:06 6.5 18202 0.85
3 10t23t2024 10:07 10:27 6.7 18242 0.88
Comoliance Run 1 6.7 18199 0.87
4 10t23t2024 10:40 11:00 6.3 1 8283 0.83
5 10t23t2024 11:01 11:21 6.4 18272 0.84
o 10t23t2024 11.22 11:42 6.4 1 8356 0.84
Comoliance Run 2 6.4 18304 0.84
7 10t23t2024 11:55 12:15 6.2 1 8353 0.82
8 10t23t2024 12'.16 12:36 6.3 1 8363 0.83
I 10t23t2024 12:37 12:57 6.4 1 8268 0.83
Comoliance Run 3 6.3 18328 0.83
Three Run Averaoe:6.4 18277 0.84
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #2 Stack
Refurence Method Test Data
Test No.Date
Sta rt
Time
End
Time
NO,,
oomvd
Volumetric
Flow dscfrn NOx lb/hr
1 10t17t2024 7.40 8:00 5.8 18237 0.76
2 10t17t2024 8:01 8:21 5.8 18227 0.76
3 10117t2024 8:22 8:42 5.8 1 8200 0.76
Gompliance Run I 5.8 1822'.|.0.76
4 10t17t2024 8:53 9:13 5.9 1 8293 0.77
5 10t17t2024 9:14 9:34 6.0 18213 0.78
6 10t17t2024 9:35 9:55 6.0 1 8269 0.79
Comoliance Run 2 6.0 18258 0.78
7 10117t2024 10:08 10.28 5.9 18279 0.77
I 10t17t2024 10:29 10:49 5.8 18213 0.76
I 10t17t2024 10:50 11:10 5.8 18193 0.76
Comoliance Run 3 5.8 18229 0.76
Three Run Averaoe:5.9 18236 0.77
Page 10 of 157 @Mostardi Platl
6.0 CERTIFICATION
Mostardi Platt is pleased to have been of service to Compass Minerals Ogden, lnc. lf you have
any questions regarding this test report, please do not hesitate to contact us at 630-993-2100.
As the program manager, I hereby certify that this test report represents a true and accurate
summary of emissions test results and the methodologies employed to obtain those results. The
test program was performed in accordance with the test methods and the Mostardi Platt Quality
Manual, as applicable.
MOSTARDI PLATT
C-'."L S{t-Project Manager
Richard J. Sollars ll
yW,tu/*.
Quality Assurance
Jeffrey M. Crivlare
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 11 of 157 @Mostardi Platt
APPENDICES
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 12 ot 157 @Mostardi Platt
Appendix A - Test Section Diagrams
Proiect No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 13 of 157 @Mostardi Platt
EQUAL AREA TRAVERSE FOR ROUND DUCTS
(Volumetric Flow)
Job:Compass Minerals Ogden, lnc.
Ogden Production Plant
Ogden, UT
Boiler #1 Stack and Boiler #2 Stack (ldentical)
October 17 and23,2024
3.33 Feet
8.71 Sq. Feet
I
2
6.0 lnches
Length
9.0 Dia.
T
I
Length
4.5 Dia.I
Test Location:
Test Date:
Stack Diameter (Feet):
Stack Area (Square Feet):
No. Sample Points Across
Diameter:
No. of Ports:
Port Length (lnches):
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
8
7
6
5 5678
4
3
2
I
Page 14 of 157 @Mostardi Platt
EQUAL AREA TRAVERSE FOR ROUND DUCTS
(Stratifi cation Traverse)
"*9.0 Dia.-f--
I
Length
4.5 Dia.I
Job:Compass Minerals Ogden, lnc.
Ogden Production Plant
Ogden, UT
Boiler #1 Stack and Boiler #2 Stack (ldentical)
October 17 and23,2024
3.33 Feet
8.71 Sq. Feet
6
2
6.0 lnches
Test Location:
Test Date:
Duct Diameter:
Duct Area:
No. Points Across Diameter:
No. of Ports:
Port Length:
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
1
2
3
4
5
6
Page 15 of 157 OMostardi Platt
GASEOUS TRAVERSE FOR ROUND DUCTS
Length
9.0 Dia.T
I
Length
4.5 Dia.I
Job:
Test Location:
Test Date:
Stack Diameter (Feet):
Stack Area (Square
Feet):
No. Sample Points:
Compass Minerals Ogden,
Ogden Production Plant
Ogden, UT
Boiler #1 Stack and Boiler
Stack (ldentical)
October 17 and 23,2024
3.33 Feet
8.71 Sq. Feet
3
Distance from lnside
To Traverse Point:
1. 83.3 % of diameter
2. 50.0 % of diameter
3. 16.7 o/o of diameter
lnc.
#2
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 16 of 157 OMostardi Platt
Appendix B - Sample Train Diagrams
ProJect No M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 17 of 157 OMostardi Platt
7.62 cm (3 in.).
USEPA Method 2 - Type S Pitot Tube Manometer Assembly
1.90-2.54 cm
(0.75 -1 .0 in.)t
*Suggested (lnterference Free)
Pitot tube/ Thermocouple
Spacing
ATD-001 USEPA Method 2 Rev. 1.2
+
T-
1t1t2021
Project No. M2442068
Boiler #'l Stack and Boiler #2 Stack
Page t8 of t57 @Mostardi Platt
USEPA Method 4- Moisture Content Sample Train Diagram
ATD-032 USEPA Method 4 Rev. 1.2 1t|t202'l
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Temperature Sensor
-\/
Glass
Wool
Plug I
tfhr \Ltllce Bath
alY.
O r)
,,1-r'I
rL,,
'l lx,lii,r.'in','
1l B#"q i' L--l : tjirst -^r_,i_.. \l
Heated Probe Sheath
Temperature Sensors I
100 mL
each Dl
HzO
,I
Dry Gas
Meter 4 Ft'--
Empty Silica /[\,\r\Orifice lncline Gauge
,,, Lful"I
Air Tight
Pump ilt\!TL
/\
Et *_l_l"aargle1
-/
Page 19 of 157 @Mostardi Platt
USEPA Methods 3A and 7E Extractive Gaseous Sampling Diagram
ATD-010 Extractive 3A and 7E Rev. 1.3 'u1t2021
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
I_l
Sample Gas Manifold
Page 20 of 1 57 @Mostardi Platt
Appendix C - Calculation Nomenclature and Formulas
Project No. M2442064
Boiler #1 Stack and Boiler #2 Stack
Page21 ol 157 OMoslardi Platt
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Project #: M244206
Test Location: Boiler#1 Stack
Date: 10123124
( 6.6 ppm - 0.0 ppm) x
(4.87 o/o - -0.01 o/o) x
Samole Calculations
NOx ppmvd
8.9 ppm
8.8 ppm - 0.0 ppm
()2 o/o (dry)
11.06 o/o
Ll.l2o/o - -0.01 o/o
02 based NOx lb/mmBtu
0.00000080 lbs/dscf
= 6.7 ppm
= 4.89 o/o
6.7 ppm x (1.194 x
0.00000080 lbs/dscf
10^-7) =
x 8,710 dscf/mmBtu x 20.9o/o
(20.9o/o - 4.89 o/o)
= 0.009 NOx lbs/mmBtu
Cs.r=(C-Q) x c.,cr-Q
where:
Co", = Effluent gas concentration, dry basis, ppm or o/o
C = Average gas concentration indicated by gas analyzer, dry basis, ppm or %o
Co = Average of initial and final system calibration bias check responses for the zero gas, ppm or 7o
C. = Average of initital and final system calibration bias check responses for the upscale calibration gas, ppm or o/o
Cra = Actual concentration of the upscale calibration gas, ppm or 7o
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 22 of 157 OMostardi Platl
Volumetric Flow Rate Calculations
Client: Compass Minerals Ogden, Inc.
PIant: Ogden Plant
Location: Boiler #1 Stack
Run: Normal Load, Run 1
Date: 10123124
Moisture Content
BWS = Vwc(std) * Vwss(std)
Vwc(sto) *Vwss(stdl * Vm(su)
where: V*.1n6y = Volume of condensed water vapor corrected to standard conditions
Vwss(std) = Volume of water vapor collected in silica gel,
corrected to standard conditions
vm(std) = Dry gas volume measured by dry gas meter,
corrected to standard conditions
Bws = 0.175
Dry Molecular Weight
Md=0.44x(o/oCO2) + 0.32x(0/oO2) + 0.28x0loN2
o/oCO2 = 8.9 o/oO2= 4.9 o/oN2 = 86.2
Md = 29.62
Wet Molecular Weight
Ms = Md x (l-Bws) + (18.0 x Bws)
Md = 29.62 Bws = 0.175
Ms = 27.59
Average Duct Velocity
Vs = 85.49 x Cp x Sqrt AP (avg) x Os (avs) + 460/ (Ps x Ms))'/2
Cp = 0.840 Ts (avg) = 303.6 Sqrt AP avg: 0.948
Ps = 25.87 Ms = 27.59
Vs = 70.41
Volumetric Flow Rate
Q (Actual Basis)= Vs x A x 60
Vs= 70.41 [= 8.710
Q= * "Ot
Qs (Standard Basis)= 17.647 x a x Ps
460 + Ts (avg)
Q = 36798 Ps = 25.87 Ts (avg) = 303.6
Qs = 22003 scfm
Qs (Standard Basis;= scfm x 60 min/hr
Qs = 1320164 scftr
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 23 ol 157 @Mostardi Platt
MOSTARDI PLATT
Volumetric Air Flow Calculations
Vm (std) =17 .647 x Vm x
Pno,
(46
t*41)xY,ar t
460 -+Tm)
Vw (std) = 0.0477 xVlc
Bws=[Vw (std)
Vw (std) + Vm (std)
y4 = (0.44x0/oCO2) + (0.32 xo/ooz) + [0.28 x (100 -o/oCoz-o/oo))
Ms = Mdx (1 - Bws) * (18 x Bws)
(Ts + 460)
ffixtlDPxCpxBS.49
Acfm = 7s x Area (of stack or duct) x 60
scfm- Acfmxtz.647. [*ffi]
minScfh= Scfmx 60 ,nr
Dscfm=Scfmx(1-Bws)
CN&F-031 Volumetric Flow Calcs Rev. 1.2 1t1t2021
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 24 ol 157 @Mostardi Platt
MOSTARDI PLATT
Moisture Calculations
(vr - v,)pvv,* = o.o+zot (vr _ vi)vwc(std): pr*M*
l,v wsg(std) -
(wr -wi)p*RT,ra = 0.0471s(Wr - W,)PrraM,
Pbo, + #Vm66) = 77.64V^Y iP
B*, =
Vwc(std) * VwssGta)
Vwcgta) + Vwss1ml I Vm1ta)
Water vapor in gas stream, proportion by volume
Molecular weight of water, 18.015 lb/lb-mole
Barometric pressure at the testing site, in. Hg
Standard absolute pressure, 29.92 in. Hg
ldealgas constant, 0.048137 (in. Hg)(ft3)/(g-mole)('R; =
[2 1 . 8348(in. Hg)(ft3y(lb-mole)(' R)]/453.592 g-mole/lb-mole
Absolute average dry gas meter temperature, "R
Standard absolute temperature, 528 "R
Final volume of condenser water, ml
lnitial volume of condenser water, ml
Dry gas volume measured by dry gas meter, dcf
Dry gas volume measured by dry gas meter, corrected to standard conditions, scf
Volume of condensed water vapor, corrected to standard conditions, scf
Volume of water vapor collected in silica gel, corrected to standard conditions, scf
Final weight of silica gel, g
lnitial weight of silica gel, g
Dry gas meter calibration factor
Average pressure exerted on dry gas meter outlet by gas sample bag, in. H2O
Density of water, 0.9982 g/ml
Specific gravity of mercury (Hg)
T"6/P"16
ft3/ml
CN&F-02'1 Moisture Calculations Rev. 1.2 111t2021
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Where:
B*. =
M*=
P*,. =
or dd-
ft=
l6 -
lsro-
Vr=
Vi =
V.=
Vm(std) =\,vu/ctsld) -\,Vwsg(std) -
Wt=
Wi =
f=
AH=
P*=
13.6 =
17.64 =
0.04707 =0.04715 = ft3ig
Page 25 of 1 57 @Mostardi Platt
MOSTARDI PLATT
Volumetric Flow Nomenclature
fi=
Bws =
cp=
Md=
Ms=
Mw=
Pbar =
Pg=
DH=
Ps=
Pstd =
Acfm =
Scfm=
Dscfm =
ft=
Ts=
Tm=
Tstd =
VS=
Vm(std)=
Vw(std) =
Vlc=
!=
Ap=
K1 =
o/oEA =
o/oCO2 =
o/oO2 =
%N2 =
0.264 =
0.28 =
0.32 =
0.44 =
13.6 =
Cross-sectional area of stack or duct, ft2
Water vapor in gas stream, proportion by volume
Pitot tube coefficient, dimensionless
Dry molecular weight of gas, lb/lb-mole
Molecular weight of gas, wet basis, lb/lb-mole
Molecular weight of water, 18.0 lb/lb-mole
Barometric pressure at testing site, in. Hg
Static pressure of gas, in. Hg (in. H2O/13.6)
Static pressure of gas, in.H2O
Absolute pressure of gas, in. Hg = Pbar + Pg
Standard absolute pressure,29.92 in. Hg
Actualvolumetric gas flow rate
Volumetric gas flow rate, corrected to standard conditions
Standard volumetric flow rate, corrected to dry conditions
ldeal gas constant, 21.85 in. Hg-ft3/'R-lb-mole
Average stack gas temperature, 'F
Average dry gas meter temperature, oF
Standard absolute temperature, 528'R
Gas velocity, fUsec
Volume of gas sampled, corrected to standard conditions, scf
Volume of water vapor in gas sample, corrected to standard conditions, scf
Volume of liquid collected
Dry gas meter calibration factor
Velocity head of gas, in. H2O
17.647 "R/in. Hg
Percent excess air
Percent carbon dioxide by volume, dry basis
Percent oxygen by volume, dry basis
Percent nitrogen by volume, dry basis
Ratio of 02 to N2 in air, v/v
Molecular weight of N2 or CO, divided by 100
Molecular weight of 02 divided by 100
Molecular weight of CO2 divided by 100
Specific gravity of mercury (Hg)
CN&F-024 Nomenclature Pitol
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rev. 1.2
Page 26 of 1 57 OMostardi Platt
MOSTARDI PLATT
Derivation of Factors Used in Nitrogen Oxides Calculations
Factors for calculating concentration as pounds per dry standard cubic feet:
Factorforc^,^ asNo, - 28316 846T1 scf =6.242801,,10-5 !!i!1Use6.2428x10-5- r\v2 ' q.53592x10814 lb /€ ml-
Factors for calculating from parts per million to lb/dscf:
Using 22.414 liters of gas per gram-mole at 0"C and 1 atmosphere pressure,
One pound-mole of gas is contained in 359.04765 ft3 at 32"F and 29.92 in. Hg, or 385.31943 ft3
at 68'F and 29.92 in. Hg
Where Mw
Factor for ppm NO, =
ppmx Mwlb/lb-+nole =lb/dscf
385. 31 943 dscf /lb-molexl 06
= pollutant molecular weight; NO2 = 46.0055 lb/lb-mole
= 8.3755 x 106 dscf/lb
46.0055 x 2.5952494 x 10-e
CN&F-008A Derivation of Factors NOx
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rev. 1.2
Use 8.3755 x 106
1t1t2021
Page 27 oI '157 @Mostardi Platt
MOSTARDI PLATT
ppm Conversion Calculations and Factors
ppm to lbs/scf
(ppm X) x (conversion factor X) = X lbs/scf
lbs/scf to lbs/hr
Dry ppm's with dry flow, and wet ppm's with wet flow.
(X lbs/scf) x (airflow scf/min) x (60 min/hr) = X lbs/hr
lbs/scf to lbs/mmBtu
Dry ppm's with dry diluent, and wet ppm's with wet diluent.
COz - (X lbs/scf) x (F") x (100/COz) = X lbs/mmBtu
Oz - (X lbs/scQ x (Fa) x (20.91(20.9-0z)) = X lbs/mmBtu
Conversion Factors
NO, - 1.19396 x 10-7
SOz - 1.6625 x 10-7
CO -7.2664 x 10-8
CHo-4.1637x10-8
CgHe-1.1419x10-7
CN&F-026 PPM Converstion Calcs & Factors Rev. 1.2
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 28 of 157 @Mostardi Platt
MOSTARDI PLATT
Itt2
Relative Accuracy Test Audit (RATA) Galculations
Mean Difference
n1std=-) din/-ti=l
Standard Deviation
-=[#]
Confidence Coefficient
.sd
CC = ts975-l'ln
Relative Accuracv
l7l + tcctRA:ffi x 100
Rev. 1.2CN&F-029 Part 60 RA Calcs
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
1t112021
Page 29 of 1 57 OMostardi Platt
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Appendix D - Reference Method Test Data
Page 30 of 1 57 @Mostardi Platt
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Project #: M244206
Test Location: Boiler #1 Stack
Date: 10123124
Time
9:25
9:26
9:27
9:28
9:29
9:30
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
Run 1
NOx pomvd O2o/o (dwl
6.40 4.93
6.50 4.92
6.60 4.89
6.60 4.926.70 4.866.60 4.83
6.60 4.86
6.70 4.856.50 4.83
6.60 4.85
6.70 4.84
6.60 4.84
6.60 4.846.60 4.88
6.70 4.86
6.70 4.85
6.60 4.86
6.60 4.88
6.50 4.86
6.60 4.88
6.60 4.88
Run 2Time NOx oomvd9:46 6.609:47 6.509:48 6.509:49 6.509:50 6.409:5'1 6.309:52 6.409:53 6.409:54 6.509:55 6.409:56 6.509:57 6.209:58 6.409:59 6.5010;00 6.40'10:01 6.4010:02 6.5010:03 6.6010:04 6.7010:05 6.7010:06 6.60
CO2o/o Gwl
8.82
8.88
8.90
8.83
8.86
8.93
8.94
8.95
8.97
8.95
8.93
8.96
8.97
8.95
8.96
8.97
8.97
8.96
8.97
8.96
8.97
O2o/o ldrvl
4.88
4.88
4.87
4.90
4.94
4.98
4.99
5.02
4.99
5.02
4.98
5.02
5.03
4.99
4.97
4.95
4.94
4.91
4.87
4.85
4.86
CO2 % (drv)
8.97
8.97
8.98
8.88
8.95
8.92
8.92
8.90
8.92
8.91
8.93
8.91
8.90
8.92
8.94
8.93
8.96
8.98
9.00
9.01
9.01
Average
Time
10:07
10:08
10:09
10:10
10:11
10:12
10:13
10:14
10:15
10:16
'1017
10:18
'10:19
10:20
10:21
10.22
1023
10:24
1O:25
10:26
1O:27
6.60
Run 3
NOx pomvd
6.70
6.70
6.70
6.70
6.60
6.60
6.50
6.50
6.70
6.60
6.60
6.60
6.80
6.70
6.70
6.60
6.60
6.70
6.60
6.80
6.70
4.87
02 o/o ldrvl
4.85
4.87
4.88
4.87
4.87
4.87
4.85
4.88
4.91
4.86
4.86
4.86
4.85
4.85
4.86
4.85
4.86
4.85
4.85
4.83
4.82
8.93
CO2%(drvl
9.01
9.01
9.00
9.00
9.01
9.01
9.02
9.01
8.99
9.02
9.01
9.02
9.03
9.02
9.01
9.03
9.01
9.02
9.03
9.04
9.04
Average
Time
10:40
1O:41
10:42
10:43
10:44
10:45
10:46
10:47
10:48
10:49
10:50
10:51
10:52
10:53
10:54
10:55
10:56
10:57
10:58
10:59
1 1:00
6.48
Run 4
NOx opmvd
6.40
6.30
6.20
6.20
6.20
6.20
6.30
6.10
6.20
6.40
6.20
6.20
6.40
6.20
6.30
6.40
6.30
6.30
6.40
6.30
6.40
4.94
02% (drvl
4.93
4.93
4.92
4.89
4.90
4.89
4.88
4.91
4.91
4.90
4.91
4.91
4.88
4.90
4.91
4.93
4.90
4.91
4.89
4.89
4.91
8.94
CO2% @ryl
9.12
9.13
9.14
9.16
9.16
9.16
9.17
9.16
9.16
9.17
9.17
9.17
9.18
9.18
9.16
9.15
9.16
9.15
9.16
9.15
9.14
6.289.024.86 9.16
OMostardi PlattProject No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 31 of 157
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Project #: M244206
Test Location: Boiler #1 Stack
Date: 10123124
Time
11:01
11'.02
11:03
11 04
11:05
11:06
11:07
11:08
11:09
11:10
11:11
11 .12
1 1:13
11:14
11:15
11:16
11:17
11:18
11:19
11.2O
11:21
Run 5
NOx ppmvd
6.50
6.40
6.40
6.30
6.40
6.40
6.50
6.30
6.40
6.40
6.30
6.20
6.50
6.20
6.40
6.30
6.40
6.50
6.40
6.40
6.20
02%Gwl
4.87
4.88
4.91
4.91
4.88
4.88
4.88
4.85
4.88
4.91
4.90
4.92
4.88
4.88
4.90
4.91
4.89
4.91
4.89
4.91
4.90
COZ% {dtvl
9.15
9.16
9.12
9.12
9.12
9.12
9.1 1
9.12
9.10
9.07
9.07
9.05
9.06
9.06
9.04
9.04
9.03
9.03
9.03
9.01
9.01
Run 6Time NOx ppmvd
11"22 6.40
11:23 6.3011.24 6.2011.25 6.30
11:26 6.20
11:27 6.3011:28 6.3011:29 6.3011:30 6.4011:31 6.40't1:32 6.30
11:33 6.4011:34 6.2011:35 6.301'l:36 6.2011:37 6.3011:38 6.20
1 1:39 6.40
11:40 6.1011:41 6.3011:42 6.20
02% Grvl
4.90
4.93
4.93
4.92
4.94
4.94
4.91
4.92
4.89
4.91
4.89
4.91
4.91
4.90
4.89
4.92
4.90
4.91
4.98
4.97
5.00
CO2 o/o ldwl
9.00
8.98
8.97
8.97
8.95
8.95
8.96
8.94
8.94
8.93
8.92
8.90
8.90
8.89
8.88
8.86
8.87
8.86
8.82
8.81
8.79
Average
Time
11:55
11:56
11:57
11:58
11:59
12:00
12O1
12:02
'12:03
12:04
12:O5
12:06
12:07
12:08
12'.O9
12'.10
12'.11
12.12
12:13
1214
12:15
5.37
Run 7
NOx oomvd
6.10
6.00
6.00
6.00
6.10
6.30
6.10
6.20
6.20
6.10
6.10
6.00
6.20
6.20
6.20
6.20
6.20
6.20
6.30
6.30
6.20
4.89
02% (dwl
4.98
4.99
4.97
4.95
4.94
4.95
4.94
4.94
4.95
4.94
4.96
4.94
4.96
4.94
4.91
4.93
4.95
4.93
493
4.92
490
9.08
CO2 % (drv)
9.12
9.12
9.13
9.14
9.15
9.14
9.14
9.13
9.12
9.12
9.10
9.10
9.09
9.10
9.10
9.10
9.08
9.09
9.09
9.10
9.1 1
4.92
O2o/o Gryl
4.94
4.93
4.93
4.96
4.92
4.95
4.97
4.97
4.93
4.93
4.95
4.97
4.97
4.98
4.96
4.95
4.97
4.96
4.97
4.97
4.96
8.91
CO2 % (drv)
9.09
9.10
9.10
9.08
9.10
9.09
9.08
9.09
9.1 1
9.12
9.1 1
9.10
9.10
9.10
9.12
9.13
9.13
9.13
9.13
9.13
9.14
Average 6.29
Run 8Time NOx pomvd
12.16 6.3012:17 6.3012:18 6.2012'.19 6.2012:20 6.2012:21 6.2012:22 6.1012.23 6.2012:24 6.4012:25 6.3012:26 6.3012:27 6.2012.28 6.2012:29 6.3012:30 6.3012:31 6.2012:32 6.2012:33 6.3012:34 6.1012:35 6.2012:36 6.20
Average 6.15
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
9.11 Average 6.23 9.114.94
Page 32 of 1 57
4.95
OMostardi Platt
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Project #: M2442O6
Test Location: Boiler#1 Stack
Oate: 10123124
Time
12:37
12:38
12:39
12:40
12:41
12:42
12:43
12:44
12:45
12:46
12:47
12.48
12:49
12:50
12:51
1252
12:53
12:54
12:55
12:56
12:57
Run 9
NOx ppmvd 02% Gwl
6.20 4.94
6.30 4.94
6.40 4.92
6.30 4.946.30 4.966.30 4.92
6.20 4.95
6.20 4.95
6.40 4.91
6.40 4.93
6.20 4.916.30 4.90
6.30 4.92
6.30 4.92
6.30 4.91
6.30 4.92
6.30 4.92
6.40 4.90
6.30 4.91
6.30 4.92
6.30 4.9'l
Run 10
Time NOx opmvd
1 3:1 5 6.4013:16 6.50
13:17 6.3013:18 6.30
1 3:1 9 6.2013:20 6.3013:21 6.4013:22 6.40
13:23 6.3013:24 6.3013:25 6.4013:26 6.3013:27 6.5013:28 6.30
13:29 6.4013:30 6.4013:31 6.60
13:32 6.50
13:33 6.6013:34 6.4013:35 6.60
CO2 % (drv)
9.15
9.17
9.18
9.17
9.16
9.18
9.16
9.17
9.19
9.18
9.19
9.20
9.19
9.19
9.20
9.20
9.20
9.21
9.21
9.21
9.22
O?oh (dwl
4.83
4.82
4.83
4.85
4.85
4.89
4.84
4.88
4.89
4.88
4.91
4.91
4.90
4.89
4.91
4.89
4.89
4.89
4.90
4.87
4.89
CO2o/o (dotl
9.20
9.21
9.21
9.20
9.18
9.17
9.20
9.17
9.18
9.18
9.17
9.18
9.18
9.19
9.17
9.19
9.19
9.19
9.19
9.20
9.19
Average
Time
13:36
13:37
13:38
13:39
13:40
13:41
13:42
13:43
13:44
13:45
13:46
13:47
13:48
13:49
13:50
13:51
13:52
13:53
13:54
13:55
13:56
6.30
Run 11
NOx opmvd
6.50
6.50
6.50
6.40
6.60
6.60
6.50
6.70
6.80
6.70
6.70
6.50
6.50
6.60
6.70
6.70
6.70
6.60
6.70
6.70
6.60
4.92
02% ldryl
4.89
4.94
4.92
4.90
4.90
4.89
4.89
4.89
4.89
4.89
4.89
4.90
4.92
4.89
4.92
4.88
4.89
4.87
4.89
4.88
4.90
9.19
CO2 % (drv)
9.20
9.17
9.18
9.18
9.18
9.20
9.20
9.20
9.19
9.20
9.19
9.19
9.18
9.20
9.18
9.20
9.19
9.20
9.19
9.19
9.19
4.88
O2oh Gwl
4.90
4.89
4.89
4.90
4.93
4.93
4.92
4.89
4.93
4.94
4.93
4.94
4.96
4.93
4.90
4.94
4.93
4.87
4.89
4.91
4.93
9.19
COZo/o Gryl
9.18
9.19
9.19
9.18
9.16
9.18
9.17
9.18
9.17
9.16
9.16
9.16
9.15
9.16
9.18
9.16
9.17
9.'19
9.19
9.17
9.18
Average 6.40
Run 12Time NOx oomvd'13:57 6.6013:58 6.7013:59 6.7014:00 6.5014:01 6.50'14:02 6.6014:03 6.40
14:04 6.0014:05 5.40
14:06 5.8014:07 6.0014:08 6.1014:09 6.0014:10 6.1014:11 5.9014:12 6.10
14:13 6.10
14:14 6.10'14:15 6.2014:'16 6.4014:17 6.40
Average
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
9.174.926.226.61 9.19 Average4.90
Page 33 of 1 57 @Mostardi Platt
Number of Ports Sampled:
Number of Points per Port:
Total Number of Traverse Points:
Part 75 Stratification Test Results Summary
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
October 23,2024
vs0
Page 34 of '157
2
6
12
Mostardi Platt
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
RATA Extractive 41 16120
OMostardi Platt
Port No.Point No.
Point
Marking,
lnches Time O2o/o
Mean
Difference
O"o/o NO, ppm
Mean
Difference
NO- oom
1 7 75824 9:1 U 864 022 62 u.2a
2 '1'1 83416 9:12 870 016 63 0.18
3 17.82816 9:14 8.69 0.17 6.5 002
4 34.13144 9:1b 8.71 015 6.2 o.zts
5 40 12584 9:1 8 872 014 6.3 0.18
6 44 20176 9:20 8.68 0.1 8 6.2 028
2 1 7 75824 9:25 8.82 0.04 6.4 006
2 1 1 .83416 9.2t E.90 U.U4 6.6 012
3 17 82816 9:29 886 0.00 67 o.22
4 34 13184 9:31 8.94 008 6.6 012
5 40.12584 9:33 8.97 0.11 6.5 U.UZ
6 44.20176 9:35 8.93 0.07 6.7 022
Averaqe 8.86 6.5
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Temp lD:
Meter lD:
Pitot lD:
Pitot Type:
Pitot Tube Coefficient:
Probe Length:
Sample PIane:
Port Length:
Port Size (diameter):
Port Type:
Duct Shape:
Diameter:
Duct Area:
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Total Number of Traverse Points:
Operating Level:
Servomex Serial Number:
Moisture Balance lD:
Stack Liner Material:
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
M244206
2 (RATA)
AIR
GM
cM53
cM53
6001
S-Type
0.84
6.0
Horizontal
6.00
4.00
Flange
Circular
3.33
8.71I
4.5
2
8
16
Normal
cAt 700
LV4
S
tn.
in.
ft
Sq. Ft.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 35 of '157 OMostardi Platl
(!EEooo=o
E
@@
-
@
o
F
r
@
9
Ce
2

r
ol

r
\

9

(l

-
:a
N
o
o
o
N
N
o
o
ON
t
s
N
t
s
E
N
F
N
go
g5
lE
o
o
o
o
6
0
0
0
;S
q
q
q
q
q
9
q
q
go
.
o
o
o
o
o
o
o
o
c=ai
E
g0Sa
o
o
o
o
o
o
o
o
:g
-
-
t
l
!
o
o
N
IG
rtN
@o
o
o
o
o
o
o
E
s
6

.E
B
t
B
E
B
$
t
s
H
s
F
N
o
t
=
o

-'

oO
-
O
O
O
O
O
5
=o
N
E
o
z-
=
r
b
d
c
i
<
d
q^
q
o
o
o
o
o
o
o
Et
-
8
8
8
8
8
8
8
8
F-N
6
6
6
6
0
6
6
o
-(@
6
0
@
N
@
6
6
xt
o
o
o
o
o
o
o
o
-i
o
o
-
o
o
o
o
o
=
FN
O
t
6
@
t
s
@
qN
.E(ooJCaJ
o
o'
E
-!!E
;,

sE
$
E
.9

!

-
ot
-
F
v
E
6
5
t
S
E
.
E
JJ

.D
d
.
o
a
,
,
,
J
J
G
.
o
-
a,o6tt,clEEo.Eo-
oo)EcnoaEPT
>
Ei
i
FE
I
T
st

!+
o
:
-
o
st
E
E
:
^
+
s3
8
8
8
:
-
FO
F
O
O
O
O
O
J^
N
O
i
t
6
0
0
0
L9
0
6
t
s
6
0
@
N
6
qo

6
6

6

6

6

0

6

6
o
ci
c
;

oo
o
d
o
o
-
E*
-
6
N
o
@
@
<
*I
Q
o
o
?
o
!
o
o
o
o
-i
o
o
o
o
o
o
o
o
=!?
N
O
t
6
@
F
O
ocoo.
.8

.E
;
E
.
€B
E-
b
.
9
o
6
1
3E
E

EE
E
i
o-
o
r
!
J
G
o
-
o
-
|!,-lJ
)o@('
)OJo)G(L
'6o.to
a
o
6
6
@
6
o
o
oc
go€t
.i

o@
o
o
!
@
F
6

i
!E
E
:
i
i
3
;
i
:

F
s
.-
t
s
t
s
N
F
N
N

E
-9oE:
!E
o
6
0
0
0
0
0
0
j'
6
q
q
q
q
q
q
q
q
Ea

o
o

o

o

o

o

o

o
f=ai
I
goSa
q
q
q
c
q
a
g
q
;.
:
o
-
?
6
o
r
s
o
€
vogU)N{to,
m6
6oOrNFVG{-
:
=Ho@z-
-
:l
t
oggEYo
(L
d
]
q^
c
c
c
q
q
q
9
q
E.
:
E
E
8
8
8
8
8
8
F-
N
N
O
O
O
O
O
O
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Ptant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
1
10t23t2024
9'.25
9:45
AIR
6
sqrt
DP
0.9327
0.9434
0 9592
0.9644
0 9539
0.9434
0 9381
0.9487
Test Tech: GM
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
DP
(in. HzO)
0.88
0.90
0.92
0.90
0.89
0.88
090
0.92
Sqrt.
DP
0.9381
0.9487
0 9592
0 9487
0 9434
0 9381
0.9487
0.9592
Temp
(oF)
304.0
304 0
304.0
304 0
303.0
303.0
303.0
303.0
Velocity
(v)
69.70
70.49
71.27
70.49
70.05
69.65
70.44
71.22
Porl Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. H2O)
0.87
0.89
0.92
0.93
091
089
088
0.90
Temp Velocity
(oF) (V)
304.0 69.30
304 0 70 09
304.0 71 .27
304 0 71.65
304.0 70 88
303 0 70 05
303.0 69.65
303.0 70.44
T€st ParameteG
P6", - Barometnc pressure, inches Hg
Po - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Oiameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
25.82
0.70
25.87
303 6
Circular
3.33
8.71
0 8988
0 9480
70.414
o/o CO2 8.90
o/o 02 4.90
% Nz 86.20
Md - dry basis lbflb mole 29.62
Ms - wet basis lb/lb mole 27.587
Bws - Moistur€ content fraction
Moisture determined by wb/db?
0.175
N
Q - ACFM
Osd - DSCFM
Os - SCFM
Os. SCFH
36,798
18,152
22.003
1,320,164
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 37 of I 57 OMostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Goefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: GM
DP
(in. HrO)
0.87
0.89
0.92
0.94
093
0.90
089
0.92
Sqrt.
DP
0.9327
0.9434
0 9592
0.9695
0.9644
0.9487
0.9434
0.9592
Temp
fF)
304 0
304.0
304.0
304 0
304.0
304.0
304.0
304 0
Volocity
(v)
69.30
70.09
71.26
72.O3
71.65
70.48
70.09
71 26
DP
(in. HrO)
0.88
0,89
092
093
0.91
089
089
090
Normal
2
10t23t2024
9:46
10:06
AIR
b
Sqrt.
DP
0.9381
0.9434
0 9592
0 9644
0.9539
0.9434
0 9434
0 9487
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
O . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp Velocity
fF) U)
304.0 69.69
304 0 70.09
304.0 71.26
304.0 71.65
304.0 70.87
304.0 70 09
304.0 70.09
304.0 70.48
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
P6u, - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.82
0.70
25.87
304.0
Circular
333
8.71
0.9044
0.9509
70 649
% coz 8.90
o/o 02 5.00
%Nz 8610
Md - dry basis lb/lb mole 29.62
Ms - wet basis lb/lb mole 27.590
Bws - Moisture content fraction 0.175
Moisture determined by wb/db (Y or N) N
36,921
18,202
22,464
1 ,323.810
Page 38 of 1 57 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0 840
b
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
3
10t23t2024
10:07
10:27
AIR
6
Sqrt.
OP
0 938'1
0.9381
0.9539
0.9544
0.9695
0.9592
0.9539
0.9487
TestTech: GM
Port Point
At
A2
A3
A4
A5
A6
A7
A8
DP
(in. H2O)
0.87
0.89
0.90
0.93
094
093
090
089
Sqrt.
DP
0.9327
0.9434
0 9487
0 9644
0.9695
0.9644
0.9487
0 9434
Temp
(oF)
303.0
303 0
303.0
303.0
303.0
303.0
303.0
303.0
Velocity
(v)
69.24
70 03
70.42
71 59
71.97
71.59
70.42
70.03
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
DP
(in. HrO)
0.88
088
0.91
0.93
094
0.92
0.91
0.90
Temp Velocity
(oF) (V)
303 0 69 64
303.0 69.64
303.0 70.81
303.0 71 59
303.0 71.97
303 0 71 .20
303 0 70.81
303.0 70.42
Tesl Parameters
P5u, - Barometric pressure, inches Hg
Po - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt OP
Average Velocity Vs (fusec)
25.82
0.70
25.87
303 0
Circular
3.33
8.71
0.9075
0.9526
70.711
o/o CO2 9.00
o/o 02 4.90
o/o N2 86.10
Md - dry basis lb/lb mole 29.64
Ms - wet basis lb/lb mole 27.600
Bws - Moisture content fraction 0.175
Moisture determined by wb/db (Y or N) N
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
36.954
18,242
22,112
1,326,710
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 39 of 157 OMostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
T€st Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: GM
DP
(in. HrO)
0.86
0.88
0.90
091
0.93
092
087
0.86
Sqrt.
DP
o.9274
0.9381
0.9487
0.9539
0.9644
0.9s92
0 9327
o.9274
Temp
(oF)
303.0
303.0
303.0
303.0
303.0
302.0
302.0
302.0
Velocity
(v)
68.68
69.48
70.26
70.65
71.42
70.99
69.04
68.64
DP
(in. HrO)
0.87
0.88
0.92
093
0.95
0.94
0.89
0.88
Normal
4
10t23t2024
10:40
11:00
AIR
6
Sqrt.
DP
0.9327
0.9381
0.9592
0 9644
o.9747
0 9695
0.9434
0.9381
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Os - SCFH
Temp Velocity
fF) (v)
302 0 69 04
302.0 69.43
302.0 70 99
303 0 71.42
303.0 72.19
303 0 71 .81
303.0 69 87
303.0 69.48
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
P6", - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of HrO
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fysec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.86
070
25 91
302.6
Circular
3.33
8.71
0.8994
0 9482
70.213
o/o CO2 9.10
o/o 02 4.90
% Nz 86.00
Md - dry basis lb/lb mole 29.65
Ms - wet basis lb/lb mole 27 683
Bws - Moisture content fraction 0.169
Moisture determined by wb/db (Y or N) N
36,693
18,283
22,001
1,320,045
Page 40 of '157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #1 Stack
6001
0 840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
5
10t23t2024
11.0'l
11.21
AIR
b
Sqrt.
DP
0.9274
0 9381
0.9592
0 9592
0.9644
0.9539
0.9327
0.9220
TestTech: GM
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
DP
(in. H2O)
088
089
091
093
093
0.91
090
0.89
Sqrt.
DP
0 9381
0.9434
0.9539
0.9644
0.9644
0.9539
0.9487
0.9434
Temp
fF)
303 0
303.0
303.0
303.0
303.0
303 0
303.0
303 0
Velocity
(v)
69 48
69.87
70.65
71.42
71.42
70.65
70.26
69 87
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. H2O)
0.86
088
092
092
093
091
0.87
085
Temp Velocity
fF) U)
303.0 68.68
303 0 69 48
303.0 71 .04
303.0 71 .O4
303.0 71 .42
303 0 70 65
303 0 69 08
303.0 68.28
Test Parameters
Pb., - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
25.86
070
25.91
303 0
Crrcular
3.33
8.71
0.8988
0.9479
70.208
o/o CO2 9.10
o/o 02 4.90
% Nz 86.00
Md - dry basis lb/lb mole 29.65
Ms - wet basis lb/lb mole 27.683
Bws - Moisturc contont fraction 0.169
Moisture determined by wb/db (Y or N) N
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
36,690
18,272
21.988
1 .319,303
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 41 of 't57 @vlostardi Platt
METHOD 2 VOLUMETRIC FLOW OATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
T€st Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: GM
DP
(in. H2O)
0.88
090
0.92
090
093
095
0.89
0.86
Sqrt.
DP
0 9381
0 9487
0.9592
0.9487
0.9644
o.9747
0.9434
o.9274
Temp
fF)
302.0
302.0
302.0
302.0
302.0
303.0
303.0
303.0
Velocity
(v)
69.47
70.25
71.03
70.25
71.41
72.22
69 91
68.72
DP
(in. H2O)
089
0.90
0.94
094
o.92
091
0.89
087
Normal
6
10t23t2024
11.22
11.42
AIR
6
Sqrt.
DP
0.9434
0.9487
0.9695
0.9695
0.9592
0.9539
0 9434
0.9327
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
O - ACFM
Osd - DSCFM
QS - SCFM
Qs. SCFH
Temp Velocity
frl N)
302.0 69.86
302.0 70.25
303.0 71.84
303.0 71.U
303.0 71 07
303.0 70.69
303.0 69 91
303.0 69 12
Port Point
A'l
A2
A3
A4
A5
A6
A7
A8
Tost ParameteE
P6", - Barometnc pressure, inches Hg
Ps - Stack Pressure, inches of HrO
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.86
070
25.91
302 6
Circular
3.33
8.71
0.9056
0.9s16
70.489
o/o CO2 8.90
o/o 02 4.90
% Nz 86.20
Md - dry basis lb/lb mole 29.62
Ms - wet basis lb/lb mole 27.656
Bws - Moisture content fraction 0.169
Moisture determined by wb/db (Y or N) N
36,838
18,356
22,089
1,325,353
Page 42 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
7
10t23t2024
11:55
12.15
AIR
6
Sqrt.
DP
0.9381
0 9434
0 9592
0.9695
0.9747
0.9644
0.9592
0.9539
TestTech: GM
Port Point
AI
A2
A3
A4
A5
A6
A7
A8
DP
(in. H2O)
085
087
090
092
0.94
0.95
0.93
0.92
Sqrt.
DP
0 9220
0.9327
0 9487
0.9592
0 9695
0.9747
0.9644
0 9s92
Temp
("F)
302.0
302.0
302 0
303.0
303.0
303 0
303 0
303.0
Velocity
(v)
68.30
69.09
70.28
71 .10
71.87
72.25
71 .48
71 .10
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. H2O)
088
089
092
0.94
0.95
0.93
092
091
Temp Velocity
("F) (v)
303.0 69.54
303.0 69 93
303.0 71.10
303.0 71 .87
303 0 72.25
303 0 71.48
303.0 71 .10
303.0 70.71
Test Parameters
P6., - Barometric pressure, inches Hg
Po - Stack Pressure, inches of H2O
P3 - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
25.86
0.70
25.91
302.8
Circular
333
8.71
0.9138
0.9558
70 840
o/o CO2 9.10
o/o 02 4.90
o/o N2 86.00
Md - dry basis lb/lb mole 29.65
Ms - wet basis lbnb mole 27.636
Bws - Moisture content fraction 0.173
Moisture determined by wb/db (Y or N) N
Q . ACFM
QSd - DSCFM
QS - SCFM
Qs. SCFH
37.021
18,353
22.192
1,331 ,519
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 43 of I 57 OMostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: GM
DP
(in. H2O)
0.88
089
092
092
0.93
0.92
0.90
091
Sqn.
DP
0 9381
0.9434
0 9592
0.9592
0.9644
0 9592
0.9487
0.9539
Temp
fF)
302.0
302.0
302.0
302 0
302 0
302 0
303 0
303 0
Velocity
(v)
69.49
69.88
71 05
71 05
71 44
71 05
70.32
70.71
DP
(in. H2O)
090
091
0.91
0.93
0.95
0.94
092
0.90
Normal
8
10n3t2024
12:16
12.36
AIR
6
Sqrt.
DP
0 9487
0 9539
0.9539
0.9644
0.9747
0.9695
0.9592
0.9487
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
P6", - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape.
Diameter, Feet
Cross Sec'tional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.86
0.70
25.91
302 6
Circular
3.33
8.71
0.9144
0.9562
70.861
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
Q . ACFM
Osd - DSCFM
Qs. SCFM
Qs. SCFH
Temp Velocity
fF) (v)
303 0 70.32
303.0 70.71
303 0 70.71
303 0 71 .48
303.0 72.25
303.0 71.87
303 0 71 .10
303.0 70.32
o/o CO2 9.10
o/o 02 4.90
% Nz 86.00
Md - dry basis lb/lb mole 29.65
Ms - wet basis lb/lb mole 27.636
Bws - Moisture content fraction 0.173
Moisture determined by wb/db (Y or N) N
37,032
18,363
22,204
1.332.235
Page 44 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lO:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: GM
DP
(in. HrO)
0.88
089
0.92
0.92
095
0.91
0.90
088
Sqrt.
DP
0.9381
0.9434
0.9592
0.9592
0.9747
0 9539
0.9487
0 9381
Temp
cF)
302.0
302 0
302 0
302 0
302.0
303.0
303.0
303 0
Velocity
(v)
69.49
69 88
71 05
71 05
72.20
70.71
70.32
69 54
DP
(in. H2O)
086
0.89
092
0.94
0.92
0.91
0.90
0.89
Normal
I
10t23t2024
12 37
12.57
AIR
6
Sqrt.
DP
0.9274
0 9434
0 9592
0 9695
0.9592
0 9539
0.9487
0 9434
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp Velocity
fF) U)
303.0 68.74
303 0 69 93
303.0 71 .10
303.0 71.87
303.0 71.10
303.0 7071
302 0 70.28
302 0 69 88
Port Point
AI
A2
A3
A4
A5
A6
A7
A8
Test Parameters
P6u, - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape.
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.86
0.70
25 91
302.6
Circular
333
871
0.9050
0.9512
70.492
o/o CO2 9.10
o/o 02 4.90
% Nz 86.00
Md - dry basis lb/lb mole 29.65
Ms - wet basis lb/lb mole 27.636
Bws - Moisture content fraction 0.173
Moisture determined by wb/db (Y or N) N
36,839
18,268
22.090
1,325,400
Page 45 of 1 57 OMostardi Platl
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Prob6 Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: GM
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pb., - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Temp Velocity
fF) (v)
302.0 69.54
302.0 70.33
303 0 70.76
303 0 71.54
303 0 71.92
303.0 71.54
303.0 72.30
303.0 71 .54
DP
(in. H2O)
086
088
090
0.91
093
094
0.92
0.91
Sqrt.
DP
0.9274
0 9381
0.9487
0.9539
0.9644
0 9695
0.9592
0.9539
Temp
(oF)
302 0
302.0
302.0
302 0
302.0
303.0
303.0
303.0
Velocity
(v)
68.75
69 54
70.33
70.72
71 .49
71.92
71 .15
70.76
DP
(in. HrO)
0.88
090
091
093
094
0.93
095
093
Normal
10
10t23t2024
13.15
13:35
AIR
6
Sqrt.
DP
0 9381
0.9487
0.9539
0 9644
0.9695
0.9644
0.9747
0 9644
25.82
070
25.87
302.6
Circular
333
8.71
0 9138
0 9558
70.884
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
O - ACFM
QSd. DSCFM
Qs - SCFM
Qs - SCFH
37,044
18,319
22,179
1,330,712
%coz 9 20
Yo Oz 4.90
% Nz 85.90
Md - dry basis lb/lb mole 29.67
Ms - wet basis lb/lb mole 27.638
Bws - Moisture content fraction 0.174
Moisture determined by wb/db (Y or N) N
Page 46 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW OATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, F€et:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: GM
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pb", - Barometric pressure, inches Hg
Po - Strack Pressure, inches of H2O
P. - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Temp Velocity
fF) U)
303.0 69 98
303.0 70.37
303.0 71.54
303.0 72.30
303.0 71 .54
303 0 70.37
303 0 69 19
303.0 68.39
DP
(in. HrO)
0.87
0.92
093
0.95
0.92
0.91
0.89
0.88
Sqrt.
DP
0.9327
0.9592
0.9644
0.9747
0 9592
0.9539
0.9434
0 s381
Temp
fF)
302.0
302.0
302.0
302.0
303.0
303 0
303.0
303.0
Velocity
(v)
69 15
71.11
71 .49
72.26
71 .15
70.76
69 98
69 s9
DP
(in. H2O)
0.89
090
093
0.95
0.93
0.90
0.87
0.85
Normal
11
10t23t2024
13:36
13:56
AIR
6
Sqrt
DP
0.9434
0.9487
0.9644
0.9747
0.96,44
0.9487
0.9327
o.9220
25.82
070
25.87
302.8
Circular
3.33
8.71
0.9056
0.9515
70.574
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
36,882
18,235
22.076
1,324.573
o/o CO2 9.20
o/o 02 4.90
% Nz 85.90
Md - dry basis lb/lb mole 29.67
Ms - wet basis lb/lb mole 27.638
Bws - Moisture content fraction 0.'174
Moisture determined by wb/db (Y or N) N
Page 47 ol 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #1 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
12
10t23t2024
13.57
14:17
AIR
6
Sqrt.
DP
0.9487
0 9592
0.9695
0.9644
0.9539
0 9487
0.9381
0 9381
TestTech: GM
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
P6", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
ts - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Re3ults
Average DP
Average Sqrt DP
Average Velocity Vs (fVsec)
Project No. M2442064
Boiler #l Stack and Boiler #2 Slack
DP
(in. HzO)
0.86
090
0.92
093
0.93
091
0.92
087
Sqrt.
DP
o.9274
0.9487
0.9592
0 9644
0.9644
0.9539
0.9592
o.9327
Temp
fF)
302 0
302.0
302 0
302.0
303 0
303 0
303 0
303 0
Velocity
(v)
68.75
70.33
71 .11
71 .49
71 54
70.76
71.15
69 1I
OP
(in. H2O)
090
092
0.94
093
0.91
090
0.88
088
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
O . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp VelocityfF) u)
303 0 70.37
303 0 71 .15
303.0 71.92
303.0 71.54
303 0 70.76
303.0 70.37
303.0 69.59
303 0 69 59
25.82
0.70
25.87
302.8
Circular
3.33
8.71
0.9063
0 9519
70 601
o/o CO2 9.20
o/o 02 4.90
o/o N2 85.90
Md - dry basis lb/lb mole 29.67
Ms - wet basis lb/lb mole 27.638
Bws - Moisture content fraction 0.174
Moisture determined by wb/db (Y or N) N
36,896
18,242
22.085
1.325,088
Page 48 of 157 OMostardi Platt
METHOD 4 MOISTURE DETERMINATION
Project Number: M244206
Client: Compass Minerals Ogden, lncFacility: Ogden Plant
Test Location: Boiler#1 Stack
Tost Date: 1012312024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
1
Normal
Start- 9r25
AIR
GM
Meter Calibration (YJ:
Meter Delta H (dH):
Sample Delta H (dH):
lnitial Vtrt:
Final Wt:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws):
End- 10 27
IMP FINAL INITIAL
776 6 710
765.9 715.4
791 7789
895.9 867
Pressure, Barometric(Hg"):
Pressure, Static (H2O"):
Pressure, Stack (Hg"):
Temperature, Stack (oF):
Meter lnitial Volume:
Meter Final Volume:
illeter Temperature:
Meter Volume dscf:
25.82
0.70
25.87
305
74 230
1 16.849
89 58
35 064
0 987
1 862
1 900
2204.3
2333.5
867.0
895.9
0.'t 75
Project Numberi M244206
Client: Compass Minerals Ogden, lnc
Facility: Ogden Plant
Test Location: Boiler #1 Stack
Tast Oate: 1012312024
Run Number:
Oporating Level:
Time:
Test Engineer:
Test Tech:
2
Normal
Start- 10:40
AIR
GM
Meter Calibration (Y):
M€ter Delta H (dH):
Sample Delta H (dH):
lnitial vt|t:
Final VW:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws):
End- 11.42
IMP FINAL INITIAL
777 .7 712 3749.5 714 6790.8 772.a
902.2 872 z
Pressure, Barometric(Hg") :
Pressure, Static (H20"):
Pressure, Stack (Hg"):
T€mperature, Stack (oF):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
Meter Volume dscf:
25.82
0.70
25.87
303
17.015
59.525
99.00
34 385
0.987
1 862
't.900
2199.7
2318.0
872.2
902.2
0.169
Project Number: M244206
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Test Location: Boiler#1 Stack
Test Date: 1012312024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
3
Normal
Start- 11:55
AIR
GM
Meter Calibration (Y): 0.987
Meter Delta H (dH): 1.862
Sample Delta H (dH): 1.900
lnitial tftft: 2199.4
Final Vtft: 2322.2
lnitial Volume: 875.3
Final Volume: 903.5
Water Vapor in Flue Gas (Bws): 0.173
End- 12.57
IMP FINAL INITIAL
77 5.7 713 7757.1 7162
789 4 769 5903.5 875 3
Pressure, Barometric(Hg"):
Pressure, Static (H2O"):
Pressure, Stack (Hg");
Temperatur€, Stack ("F):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
M€ter Volume dscf:
25.82
070
25.87
303
60.073
102 335
100 00
34.123
Project Numberi M244206
Client: Compass Minerals Ogden, lncFacility: Ogden Plant
TestLocation: Boiler#1 Stack
Test Date: 1012312024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech;
4
Normal
Start- 13:15
AIR
GM
End- 14.17
Preasure, Barometric(Hg"):
Pressure, Static (H2O"):
Pressure, Stack (Hg"):
Temperature, Stack ("F):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
Meter Volume dscf:
25 82
070
25 87
303
2.742
44.958
102.00
33.965
Meter Calibration (Y):
Meter Oelta H (dH):
Delta H:
lnitial VW:
Final VW:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws):
Page 49 of 1 57
0 987
1.862
1 900
2199.6
2323.1
874.8
902.8
0.174
IMP FINAL INITIAL
773.5 712 4
758.2 716 9
791 .4 770.3902.8 874 8
OMostardi PlattProject No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Project #: M244206
Test Location: Boiler #2 Stack
Date: 10117124
Time
7:40
7'.41
7:42
7.43
7'.44
7:45
7:46
7:47
7:48
7'.49
7:50
7:51
7:52
7:53
7:54
7:55
7:56
7:57
7:58
7:59
8:00
Run 1
NOx ppmvd 02% @rvl5.90 5.405.80 5.425.70 5.415.90 5.425.70 5.405.90 5.435.80 5.415.90 5.395.70 5.385.80 5.385.80 5.405.90 5.425.70 5.435.90 5.435.90 5.415.80 5.455.70 5.385.90 5.395.80 5.395.90 5.405.90 5.38
Run 2Time NOx ppmvd
8:01 5.808.02 5.708:03 5.708:04 5.808:05 5.708:06 5.908:07 5.908:08 5.908:09 5.708:10 5.908:11 5.808:12 5.808:13 5.808:14 5.808:'15 5.808:16 5.708:17 5.908:18 5.908:19 5.908:20 5.808:21 5.90
COZo/o (dwl
8.61
8.61
8.60
8.59
8.59
8.58
8.58
8.57
8.60
8.58
8.56
8.57
8.56
8.54
8.54
8.55
8.55
8.56
8.58
8.56
8.58
O2oh (d,wl
5.40
5.40
5.40
5.46
5.43
5.42
5.40
5.41
5.41
5.39
6.23
6.00
5.41
5.41
5.36
5.38
5.37
5.38
5.37
5.38
5.41
CO2o/o (dwl
8.58
8.56
8.55
8.54
8.54
8.56
8.57
8.57
8.57
8.58
7.97
8.12
8.55
8.50
8.56
8.57
8.60
8.59
8.60
8.60
8.58
Average
Time
8:22
8.23
8:24
8:25
8:26
8:27
8:28
8:29
8:30
8:31
8:32
8:33
8:34
8:35
8:36
8:37
8:38
8:39
8:40
8:41
8:42
5.82
Run 3
NOx ppmvd
5.90
5.70
5.70
5.90
5.70
5.80
5.80
5.90
5.80
5.70
5.80
5.80
5.80
5.90
5.70
5.80
5.70
5.90
5.80
5.90
5.80
5.41
02%Gwl
5.42
5.43
5.46
5.43
5.44
5.44
5.47
5.48
5.44
5.46
5.44
5.41
5.42
5.37
5.36
5.40
5.37
5.40
5.37
5.38
5.36
8.57
CO2 % (drv)
8.56
8.57
8.s6
8.58
8.58
8.58
8.57
8.56
8.59
8.58
8.58
8.61
8.59
8.62
8.64
8.62
8.63
8.63
8.63
8.63
8.65
Average
Time
8:53
8:54
8:55
8:56
8:57
8:58
8:59
9:00
9:01
9:02
9:03
9:04
9:05
9:06
9:07
9:08
9:09
9:10
9:1'l
9:12
9:13
5.81
Run 4
NOx pomvd
5.80
5.70
5.70
5.80
5.70
5.70
5.80
5.70
5.70
5.90
5.80
5.90
5.70
5.80
5.80
5.80
5.80
5.90
5.70
5.70
5.90
5.47
O2o/o Gntl
5.46
5.48
5.50
5.46
5.55
5.50
5.50
5.51
5.52
5.54
5.54
5.50
5.54
5.46
5.48
5.53
5.51
5.47
5.51
5.48
5.47
8.52
CO2o/o (drvl
8.81
8.82
8.81
8.82
8.78
8.80
8.79
8.80
8.78
8.78
8.80
8.80
8.80
8.84
8.85
8.82
8.84
8.86
8.85
8.86
8.88
Average
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Average
Page 50 of 1 57
s.78 5.50
OMostardi Platt
Client: Compass Minerals Ogden, lnc.
Facitity: Ogden Plant
Project #: M244206
Test Location: Boiler #2 Stack
Date: 10117124
Time
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
9:31
9:32
9:33
9:34
Run 5
NOx opmvd 02o/o {d,wl CO2 % (drv)
5.70 5.48 8.87
5.70 5.50 8.865.70 5.55 8.84
5.80 5.54 8.85
5.70 5.53 8.85
5.80 5.55 8.845.80 5.52 8.86
5.80 5.54 8.86
5.70 5.52 8.85
5.80 5.56 8.855.80 5.56 8.84
5.80 5.51 8.86
5.90 5.56 8.855.80 5.53 8.855.80 5.57 8.855.90 5.51 8.85
5.80 5.57 8.88
5.70 5.46 8.885.90 5.55 8.865.70 5.58 8.865.90 5.53 8.84
Run 5Time NOx oomvd9:35 5.709:36 5.709:37 5.909:38 5.7O9:39 5.909:40 5.809:41 5.709:42 5.909:43 5.709'.44 5.709:45 5.709:46 5.709:47 5.709:48 5.909:49 5.709:50 5.909:51 5.709:52 5.909:53 5.809:54 5.809:55 5.80
O2o/o (dryl
5.56
5.56
5.56
5.65
5.54
5.51
5.53
5.51
5.55
5.55
5.57
5.54
5.54
5.54
5.55
5.51
5.50
5.50
5.52
5.55
5.56
CO2 % (drv)
8.85
8.85
8.85
8.80
8.87
8.88
8.87
8.89
8.86
8.86
8.85
8.85
8.85
8.86
8.87
8.86
8.86
8.88
8.88
8.83
8.86
Average
Time
10:08
10:09
10:10
10:11
10:12
10:13
10:14
10:15
10:16
10:17
10:18
10:19
10:20
10.21
10:22
10:23
10.24
10:25
10:26
10"27
10:28
5.79
Run 7
NOx pomvd
5.70
5.70
5.80
5.90
5.70
5.70
5.90
5.70
5.80
5.90
5.80
5.80
5.80
5.70
5.70
5.80
5.90
5.80
5.80
5.90
5.70
s.53
O2o/o (drvl
5.52
5.52
5.52
5.54
5.52
5.52
5.55
5.54
5.52
5.53
5.50
5.51
5.48
5.48
5.55
5.55
5.51
5.54
5.54
5.50
5.50
8.85
CO2 % (drv)
8.70
8.72
8.72
8.71
8.71
8.71
8.70
8.69
8.69
8.71
8.72
8.71
8.72
8.72
8.69
8.68
8.69
8.70
8.66
8.70
8.71
5.78
Run 8
Time NOx opmvd 02o/o (drvl CO2o/o ldwl10:29 5.70 5.51 8.6810:30 5.90 5.49 8.6810:31 5.80 5.55 8.6810:32 5.90 5.51 8.66'10:33 5.80 5.53 8.6810:34 5.70 5.51 8.6610:35 5.90 5.54 8.6710:36 5.70 5.53 8.6610:37 5.90 5.52 8.66
10:38 5.90 5.54 8.6510:39 5.80 5.51 8.7010:40 5.80 5.52 8.6710:41 5.70 5.53 8.68
10:42 5.90 5.46 8.69
10:43 5.70 5.45 8.7010:44 5.90 5.50 8.68
10:45 5.70 5.52 8.67
10:46 5.90 5.55 8.6510:47 5.90 5.51 8.6810:48 5.70 5.54 8.6510:49 5.80 5.45 8.67
5.79
Project No. M2442068
Boiler #"1 Stack and Boiler #2 Stack
8.70 Average 5.81
Page 5l of 157
5.52 5.51
@Mostardi Platt
Client: Compass Minerals Ogden, lnc
Facility: Ogden Plant
Project #: M244206
Test Location: Boiler#2 Stack
Date: 10117124
Run 9Time NOx ppmvd
10:50 5.7010:51 5.8010:52 5.70
10:53 5.9010:54 5.7010:55 5.8010:56 5.9010:57 5.9010:58 5.7010:59 5.9011:00 5.8011:01 5.7011:02 5.8011:03 5.7011:04 5.90
11:05 5.7011:06 5.8011:07 5.9011:08 5.9011:09 5.90
11:10 5.80
o2 % (drv) CO2o/o Gryl5.50 8.675.51 8.65
5.48 8.675.51 8.655.53 8.655.49 8.675.54 8.645.50 8.65
5.53 8.64
5.51 8.655.54 8.625.54 8.62
5.53 8.625.53 8.62
5.49 8.64
5.52 8.635.52 8.645.54 8.625.48 8.645.53 8.635.51 8.61
Run 10Time NOx opmvd1120 5.80
11 21 5.80
11:22 5.9011:23 5.8011:24 5.9011:25 5.9011:26 5.8011:27 5.70
11 28 5.70
11:29 5.901'l:30 5.9011:31 5.90
11.32 5"8011:33 5.701',t'.34 5.90
11:35 5.8011:36 5.7011:37 5.9011:38 5.8011:39 5.8011:40 5.7O
02% (dryl
5.48
5.48
5.51
5.45
5.51
5.49
5.46
5.45
5.44
5.46
5.44
5.45
5.47
5.43
5.44
5.43
5.48
5.46
5.48
5.46
5.49
CO2oh Gryl
8.68
8.69
8.68
8.71
8.68
8.71
8.70
8.71
8.71
8.70
8.71
8.71
8.71
8.70
8.70
8.7',!
8.70
8.71
8.68
8.70
8.67
Average
Time
11:4'l
11:42
'11.43
11:44
11:45
11:46
11:47
11:48
11:49
'11:50
11:51
11:52
11:53
11.54
1'l:55
11:56
1'l:57
11:58
11:59
12:OO
12:01
5.80
Run 11
NOx opmvd
5.70
5.70
5.90
5.70
5.80
5.80
5.70
5.70
5.90
5.70
5.70
5.80
5.70
5.90
5.70
5.80
5.70
5.80
5.70
5.70
5.80
5.52
O2o/o (dll
5.46
5.46
5.47
5.53
5.47
5.49
5.45
5.49
5.51
5.54
5.50
5.49
5.51
5.46
5.55
5.60
5.56
5.58
5.58
5.61
5.58
8.64
CO2% (dryl
8.68
8.69
8.68
8.67
8.67
8.68
8.69
8.66
8.66
8.64
8.66
8.66
8.66
8.68
8.64
8.59
8.60
8.60
8.59
8.57
8.58
5.46
O2o/o (dwl
5.51
5.54
5.55
5.53
5.49
5.56
5.52
5.51
5.49
5.52
5.55
5.52
5.53
5.56
5.44
5.54
5.50
5.52
5.56
5.49
5.52
8.70
CO2 % (drv)
8.62
8.63
8.62
8.63
8.64
8.61
8.63
8.62
8.63
8.63
8.60
8.63
8.63
8.61
8.64
8.61
8.62
8.65
8.60
8.62
8.61
Run 12Time NOx oomvd12:02 5.90'12:03 5.7012:04 5.80
12:05 5.7O
12:06 5.70
12:07 5.9012:08 5.8012:09 5.8012:10 5.7012.11 5.8012:12 5.8012:13 5.80
12:14 5.70
12:15 5.7012:16 5.7012:17 5.9012:18 5.7012:19 5.9012:20 5.80
12:21 5.70
12:22 5.90
Average 5.76
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
8.65 Average 8.62
Page 52 of 157
5.78 5.52
@Mostardi Platt
Part 75 Stratification Test Results Summary
Gompass Minerals Ogden, !nc.
Ogden Plant
Boiler #2 Stack
October 17, 2024
Number of Ports Sampled: 2
Number of Points per Port: 6
Total Number of Traverce Points: 12
Port No.Point No.
Point
Marking,
lnches Time Oro/o
Mean
Difference
O,o/o NO, ppm
Mean
Difference
No, ppm
I 1 7.75824 7'.18 8.82 0.10 5.8 0.01
2 1 1 .83416 7.20 8.84 0.12 5.8 0.01
3 17.82816 7'.22 8.82 0.10 5.8 0.01
4 34.13184 7"24 8.79 0.07 5.7 0.11
5 40.12584 7'.26 8.77 0.05 5.9 0.09
6 44.20176 7'.28 8.75 0.03 5.8 0.01
2 1 7.75824 7'.32 8.71 0.01 5.8 0.01
2 11.83416 7'.34 8.68 0.04 5.9 0.09
3 17.82816 7:36 8.65 0.07 5.8 0.01
4 34.13184 7'.38 8.63 0.09 5.7 0.1 1
5 40.12584 7:40 8.62 0.10 5.9 0.09
b 44.20176 7.42 8.61 0.1 1 5.8 0.01
Averaqe 8.72 5.8
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 53 of 1 57 OMostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Temp lD:
Meter lD:
Pitot !D:
Pitot Type:
Pitot Tube Coefficient:
Probe Length:
Sample Plane:
Port Length:
Port Size (diameter):
Port Type:
Duct Shape:
Diameter:
Duct Area:
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Total Number of Traverce Points:
Operating Level:
Servomex Serial Number:
Moisture Balance lD:
Stack Liner Material:
Compass Minerals Ogden,
Ogden Plant
Boiler #2 Stack
M244206
2 (RATA)
AIR
RB
cM53
cM53
6001
S-Type
0.84
6.0
Horizontal
6.00
4.00
Flange
Circular
3.33
8.7',!
o
4.5
2
8
16
Normal
cAr 700
LV4
S
ln.
tn.
ft
Sq. Ft.
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 54 of 1 57 @Mostardi Platt
(6d6ooo=o
t
FN
N
@
F
o
o
N
9<
@
F
F
@
c
!
@
N
\
.:i
=
o
o
o
N
i
o
N
o
O@
t
s
F
F
F
F
F
N
go
9<9!
-
rc
o
o
o
o
o
o
o
o
;'6
Q
Q
q
q
q
q
q
q
.=
d
o
o
o
o
o
o
o
o
f=o2
E
go5;
o
o
o
o
o
o
o
o
I3
o

-
o
s

N

I
6

s
,a
tc!oF
3
9
0
0
0
v
i
E
H

*"

EB
H
$
;
g
$
H
B
S
E
S
8
3
E
B

q
c;
c
;

cj
c
i
c
j
o
d
o
Z-
=
F
F
-
<
<
c
i
g^
c
c
q
q
q
q
q
q
ET
.
N
N
N
N
N
N
N
69

N

N

N

N

N

N

N

N
F-
o
o
o
o
o
o
o
o
^
Q*
-
o
+
@
N
o
o
=E
@
@
.
q
6
O
o
O
@
-i
o
o
o
e
o
e
o
e
=
ol
FN
O
T
A
O
F
O
(gGo-t
r6.
9
o.
=
EEo
E
..

'i
E
E
*;

,E
E
g
H
E
Ez
.
.
F
i
=
.
o
J
o
=
-
ot
-
r
g
'E

6
5t
S

E.

b
o
.t

G.

o4
t
u
J
E
o
-
EoNtttr.EEoEo.
osiq,oo)oIe96=E
#
I
!3
d
e
r
Is
s
t
+E
-
g
l
+
SE
8
8
H
3
.
F-r)olJ
)
rJ
)o)cn(E(]
-
'6C-6
@
a
o
a
o
o
r
o
o
a
D
oE
goE,o
i
oF
F
@
o
o
-
N

:
!t
;
3
:
t
;
i
:
3

p
O@
N
F
t
s
F
F
F
t
s
'
>9
-ca
l;
-
-
o
o
o
o
o
6
;6
q
C
q
q
q
q
o
q
gG
o
o
o
o
o
o
o
o
a=a2
g05:
o
o
o
o
o
o
o
o
lg
{
6
F
o
@
6
@
@
te
!o(EaNt+OJ=38Rp
SGNx
=Eadz-6t
oi
6
p'
E
oo
g^
q
q
q
c
q
c
c
c
Er
O
-
F
N
N
N
N
N
OO
-
N
N
N
N
N
N
N
N
F-6
O
O
O
O
O
O
O
St
F
O
@
9
F
-
i-
N
o
@
6
0
!
@
@
L+
N
n
?
@
N
6
i
o
qo
6
6
6
0
0
6
6
6
o
oo

c
i
c
i
d
o
c
i
o
^
Q-

-
o
r

@
o
o

@
=E
@
@
0
1
o
o
o
o
@
-i
o
o
o
o
o
o
o
o
=oc
t
.E
.
u
E
€-
P
sr
H
E
E
i
i
o-
o
l
!
J
o
-
o
-
o
-
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: RB
0.'t71
N
DP
(in. H2O)
091
0.93
0.94
093
0.92
0.93
0.91
0.92
Sqrt.
OP
0 9539
0.9644
0 969s
0 9644
0 9592
0 9644
0.9539
0 9592
Temp
fF)
3220
322.0
322.0
322.0
323.O
323 0
323.0
323.0
Velocity
(v)
71.57
72.35
72.74
72.35
72.OO
72.39
71 .61
72.00
DP
(in. H2O)
0.88
0.89
092
094
092
092
091
093
Normal
1
10t25t2024
7.40
8:00
AIR
6
Sqrt.
DP
0 9381
0.9434
0 9592
0.9595
0 9592
0.9592
0.9539
0 9644
Port Point
B1
B2
B3
B4
B5
B5
B7
B8
O . ACFM
Osd - DSCFM
Qs - SCFM
Qs - SCFH
Temp Velocityfrr u)
322.0 70 38
322.0 70.78
323.0 72.00
323.0 72.78
323.0 7200
323.0 72.00
323.0 71.61
323.0 72.39
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pba, - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
! - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sec{ional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25.90
070
25 95
322.6
Circular
3.33
8.71
0.9188
0.9585
71.935
o/o CO2 8.60
o/o 02 5.40
% Nz 86.00
Md - dry basis lb/lb mole 29.59
Ms - wet basis lbnb mole 27.6'10
Bws - Moisture content fraction
Moisture determined by wb/db?
37,593
18,237
21,998
I ,3 1 9,906
Page 56 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lO:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
600 1
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: RB
Port Point
AI
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pb., - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t - Average stiack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
DP
(in. HzO)
090
092
0.94
092
0.92
0.91
0.90
0.90
Sqrt.
DP
0.9487
0 9592
0 9695
0 9592
0.9592
0 9539
0.9487
0 9487
Temp
("F)
322.0
322.O
322.0
322.0
322.0
322.0
323.0
323 0
Velocity
(v)
71 .18
71.97
72.75
71.97
71.97
71.58
71.23
71.23
DP
(in. H2O)
088
0.90
0.92
0.93
0.95
0.94
0.92
0.93
Normal
2
10t2512024
8.01
8.21
AIR
b
Sqrt.
DP
0 9381
0.9487
0 9592
0.9644
0.9747
0.9695
0 9592
0 9644
Temp Velocity
fF) ry)
323.0 70 43
323 0 71 .23
323 0 72.02
323.0 72.41
323.0 73 18
323 0 72.80
323.0 72.02
323.0 72.41
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
25 90
0.70
25.95
322.6
Circular
3.33
8.71
0 9175
0.9578
71.898
o/o COz 8.50
o/o 02 5.50
% Nz 86.00
Md - dry basis lb/lb mole 29 58
Ms - wet basis lb/lb mole 27.600
Bws - Moisture content fraction 0.171
Moisture determined by wb/db (Y or N) N
37,574
18,227
21,987
1,319,232
Page 57 of 1 57 @Mostardi Plaft
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
3
10t25t2024
8.22
8.42
AIR
6
Sqrt.
DP
0.9487
0 9434
0 9592
0.9539
0.9539
0.9644
0 9487
0 9592
TestTech: RB
Port Point
A,l
A2
A3
A4
A5
A5
A7
A8
DP
(in. H2O)
091
0.92
094
0.94
n02
0.91
090
0.91
Sqrt.
OP
0 9539
0.9592
0 9695
0.9695
0.9644
0 9539
0 9487
0 9539
Temp
fF)
323.0
323.0
323 0
323 0
323 0
322.0
322.0
322.0
Velocity
(v)
71 .61
72.00
72.78
72.78
72.39
71 .57
71 .17
71 57
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. H2O)
090
089
092
091
0.91
0.93
0.90
o92
Temp Velocity
(oF) (V)
322.0 71.17
322.0 70.78
322.0 71.96
322.0 71.57
323.0 71.61
323.0 72.39
323.0 71.22
323.0 72 00
Test Parameterg
P6,, - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
! - Average stack temperature, oF
Duct Shape.
Diameter, Feet
Cross Seclronal Area of Stack. Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fvsec)
25.90
070
25.95
322.6
Circular
3.33
8.71
0.9150
0 9565
71.786
o/o CO2 8.60
Yo Oz 5.40
%Nz 8600
Md - dry basis lb/lb mole 29.59
Ms - wet basis lb/lb mole 27.610
Bws - Moisture content fraction 0.171
Moisture determined by wb/db (Y or N) N
Q - ACFM
QSd - DSCFM
Qs. SCFM
QS. SCFH
37,515
18,200
21.955
1 ,317 ,271
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 58 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
Operating Level:
Run No.:
Test Oate:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
4
10t25t2024
8:53
9.13
AIR
6
Sqrt.
DP
0.9592
0.9644
0.9592
0.9695
0 9695
0 9644
0 9644
0.9539
Test Tech: RB
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0 840
6
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pb., - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape.
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average OP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442OOB
Boiler #1 Stack and Boiler #2 Stack
DP
(in. H2O)
0.88
0.89
091
0.92
092
0.94
093
0.93
Sqrt.
OP
0.9381
0.9434
0 9539
0.9592
0.9592
0.9595
0.9644
0.9644
Temp
(oF)
323.0
323.0
323.0
322.O
322.0
322.0
322.0
322.0
Velocity
(v)
70.35
70.75
71.54
71 89
71.89
72.67
72.28
72.28
DP
(in. H2O)
0.92
0.93
0.92
0.94
094
093
093
091
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
Temp Velocity
fF) U)
322.0 71.89
322.0 72.28
322.0 7'1 89
322.0 72.67
322.0 72.67
322.0 72.28
322.0 72.28
322.0 71.50
25.90
0.70
25.95
322.2
Circular
333
8.71
0 9213
0.9598
71.943
o/o COz
o/o 02
%Nr
Md - dry basis lb/lb mole
Ms - wet basis lbnb mole
Q . ACFM
QSd - DSCFM
Qs - SCFM
Qs - SCFH
Bws - Moisture contont fraction 0.169
Moisture determined by wb/db (Y or N) N
8.80
5.50
85.70
29 63
27 663
37,598
18,293
22.013
1,320,796
Page 59 of 1 57 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Oate:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: RB
DP
(in. HrO)
0.88
088
0.90
092
0.92
094
093
0.92
Sqrt.
DP
0.9381
0.9381
0 9487
0 9592
0 9592
0 9695
0 9544
0 9592
Temp
fF)
322.0
322.0
323.0
323.0
323.0
323.0
323.0
323.0
Velocity
U)
70 31
70 31
71.15
71 .93
71.93
72.71
72.32
71.93
DP
(in. HrO)
0.89
090
091
093
0.93
0.92
0.92
093
Normal
5
10125t2024
9:14
9:34
AIR
b
Sqrt.
DP
0.9434
0.9487
0.9539
0 9644
0 9644
0.9592
0 9592
0 9644
Port Point
B,I
B2
B3
B4
B5
B6
B7
B8
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp VelocitycF) (v)
323 0 70.75
323.0 71.15
323 0 71.54
323.0 72.32
322.0 7228
322.0 71.89
322.0 71 89
322.0 72.28
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameterg
Pber - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
! - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ftz
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25 90
070
25 95
322.6
Circular
3.33
8.71
0.9138
0.9559
71 .670
o/o CO2 8.80
o/o 02 5.50
% Nz 85.70
Md - dry basis lb/lb mole 29.63
Ms - wet basis lb/lb mole 27.663
Bws - Moisture content fraction 0.169
Moisture determined by wb/db (Y or N) N
37,454
18,213
21,917
1 ,315,030
Page 60 of 157 @lvlostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Op€rating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches
Normal
6
10t25t2024
9:35
9:55
AIR
A
Sqrt.
DP
0.9487
0 9592
0.9539
0 9695
0.9644
0.9644
0.9592
0.9539
Test Tech: RB
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
DP
(in. H2O)
0.89
091
0.90
0.93
0.94
0.92
0.93
0.93
Sqrt.
DP
0.9434
0.9539
0 9487
0.9644
0 9695
0 9592
0.9644
0.9644
Temp
fF)
323.0
323.0
323 0
323.0
323.0
323.0
323.0
323.O
Velocity
(v)
70.75
71 .54
71.15
72.32
72.71
71.93
72.32
72.32
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. HrO)
0.90
0.92
091
0.94
093
0.93
0.92
0.9'l
Temp VolocityfF) (v)
323.0 71.15
323.0 71 93
323.0 71.54
322.0 72.67
322.0 72.28
322.0 72.28
322.0 71.89
322.0 71.50
Test ParameterB
P6u, - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
25.90
070
25.95
322.7
Circular
3.33
8.71
0 9194
0.9588
71.894
o/o CO2 8.80
o/o 02 5.50
% Nz 85.70
Md - dry basis lb/lb mole 29.63
Ms - wet basis lb/lb mole 27.663
Bws - Moisture contsnt fraction 0.169
Moisture determined by wb/db (Y or N) N
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs. SCFH
37,572
18,269
21,984
1,319,043
Project No. M2442068
Boiler #'l Stack and Boiler #2 Stack
Page 61 of 157 @lvlostardi Platt
METHOO 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coeftici6nt:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
TestTech: RB
DP
(in. H2O)
089
0.92
093
0.95
093
0.94
092
093
Sqrt.
OP
0.9434
0.9592
0 9644
0.9747
0 9644
0.9695
0 9592
0 9644
Temp
fF)
323.0
322.0
322.0
322.O
322.0
322.0
322.0
322.O
Velocity
(v)
70.78
71.92
72.31
73.08
72.31
72.70
71.92
72.31
DP
(in. H2O)
091
0.90
090
092
091
0.93
094
o.92
Normal
7
10t25t2024
10:08
10.28
AIR
o
Sqrt.
DP
0 9539
0.9487
0 9487
0.9592
0.9539
0.9644
0 9695
0.9s92
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp Velocity
fF) u)323.0 71.58
323.0 71.18
322.0 71.14
322.0 71.92
322 0 7'.1.53
322.0 72.31
322.0 72.70
322.0 71.92
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pbar - Barometric pressure, inches Hg
Ps - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Seclional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25 90
0.70
25.95
322.2
Circular
3.33
8.71
0.9213
0.9598
71.976
% coz 8.70
o/o 02 5.50
% Nz 85.80
Md - dry basis lb/lb mole 29.61
Ms - wet basis lb/lb mole 27.638
Bws - Moisture content fraction 0.170
Moisture determined by wb/db (Y or N) N
37,615
18,279
22,023
1.321.396
Page 62 of 1 57 @Mostardi Platt
METHOO 2 VOLUMETRIC FLOW DATA
Project Number:
Cli€nt:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
I
10125t2024
10:29
10:49
AIR
6
Sqrt.
DP
0.9434
0.9434
0.9487
0.9592
0.9644
0.9539
0.9592
0.9644
Test Tech: RB
Port Point
AI
A2
A3
A4
A5
A6
A7
A8
DP
(in. HrO)
0.91
093
0.94
090
0.92
0.93
0.91
0.90
Sqrt.
DP
0.9539
0.9644
0.9695
0.9487
0.9592
0.9544
0 9539
0.9487
Tomp
("F)
322.0
322.0
322.0
322.0
322.0
322.0
322.0
322.0
Velocity
(v)
71 53
72.31
72.70
71 .14
71.92
72.31
71.53
71 .14
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
OP
(in. HrO)
089
089
090
092
0.93
0.91
0.92
0.93
Tomp Velocity
fF) U)322.0 70.74
322.0 70.74
322.0 71.14
322.0 71.92
322.0 72.31
322.0 71.53
322.0 71.92
322.0 72.31
Test Parameters
Pba, - Barometric pressure, inches Hg
Pe - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Seciional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
25.90
070
25.95
322.0
Circular
3.33
8.71
0 9144
0 9562
71.699
o/o CO2 8.70
o/o 02 5.50
% Nz 85.80
Md - dry basis lb/lb mole 29.61
Ms - wet basis lb/lb mole 27.638
Bws - Moisture content fraction 0.170
Moisture determined by wb/db (Y or N) N
Q - ACFM
QSd - OSCFM
Qs - SCFM
Qs - SCFH
37.470
18,213
21,944
1,316,618
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 63 of 1 57 OMostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Tost Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0.840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: RB
DP
(in. HrO)
0.88
090
0.91
0.93
092
093
091
090
Sqrt.
DP
0.9381
0.9487
0.9539
0.9644
0.9592
0.9644
0.9539
0 9487
Temp
fF)
323 0
323.0
323.0
323 0
323.0
322.0
322.0
322.O
Velocity
(v)
70.40
71.20
71.59
72.37
71.98
72.33
71.55
71.15
DP
(in. HrO)
0.90
089
0.90
091
093
094
o.92
0.93
Normal
9
10t25t2024
1 0;50
11:10
AIR
6
Sqrt.
DP
0.9487
0.9434
0 9487
0 9539
0.9644
0.9695
0.9592
0.9644
Port Point
B'l
a2
B3
B4
B5
B6
B7
B8
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp VelocityfF) ry)
322.0 71.15
322 0 70.76
322.0 71.15
322.0 71.55
322.0 72.33
323 0 72.76
323 0 71.98
323 0 72.37
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
Test Parametors
P5", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
! - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
25 90
0.70
25.95
322.5
Circular
3.33
8.71
0.9125
0.9552
71.665
a/o CO2 8.60
o/o 02 5.50
% Nz 85.90
Md - c,ry basis lb/lb mole 29 60
Ms - wet basis lb/lb mole 27.625
Bws - Moisture content fraction 0.170
Moisture determined by wb/db (Y or N) N
37,452
1 8,1 93
21,919
1 ,315, 1 54
Page 64 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0 840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
10
10t25t2024
11.20
11.40
AIR
6
Sqrt.
DP
0.9381
0.9487
0.9434
0.9487
0.9539
0.9644
0.9592
0.9487
Test Tech: RB
Port Point
A1
A2
A3
A4
A5
A6
A7
A8
DP
(in. HrO)
0.88
0.90
091
093
0.92
093
0.91
0.92
Sqrt.
DP
0.9381
0 9487
0.9539
0.9644
0.9592
0.9644
0 9539
0.9592
Temp
fF)
3220
322.0
322.0
322.0
322.0
322.0
3220
322.0
Velocity
(v)
70 30
71.09
71.48
72.27
71.88
72.27
71 .48
71.88
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
DP
(in. HaO)
088
0.90
0.89
0.90
0.91
0.93
0.92
0.90
Temp Velocity
fF) U)322.0 70.30
322.0 71.09
322.0 70.69
322.0 71.09
322.0 71.48
322.0 7227
322.0 7'1 88
322.0 71.09
Test Paramoters
P6", - Barometrrc pressure, inches Hg
Po - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stiack temperature, oF
Duct Shape
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fysec)
25 90
0.70
25.95
322.0
Circular
3.33
8.71
0 9081
0 9529
71.408
o/o CO2 8.70
o/o 02 5.50
% Nz 85.80
Md - dry basis lb/lb mole 29.61
Ms - wet basis lb/lb mole 27.673
Bws - iioisture content fmction 0.167
Moisture determined by wb/db (Y or N) N
Q . ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
37,3'18
18,205
21,855
1,311,278
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 65 of '157 OMostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M244206
Compass Minerals Ogden, lnc.
Ogden Plant
Boiler #2 Stack
600 1
0.840
b
Operating Level:
Run No.:
TeBt Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test T€ch: RB
DP
(in. H2O)
090
0.92
091
0.93
0.93
094
092
0.91
Sqrt.
DP
0 9487
0.9592
0 9s39
0 9644
0.9644
0.9695
0.9592
0 9539
Temp
cF)
323.0
323 0
323 0
323.0
323.0
323 0
322.0
322.0
Velocity
(v)
71.15
71.94
71 .55
72.33
72.33
72.72
71.89
71.50
DP
(in. HzO)
0.89
0.90
0.92
091
0.93
0.92
092
0.90
Normal
11
10t25t2024
1 1:41
12:01
AIR
6
Sqrt.
DP
0.943/
0.9487
0.9592
0 9539
0.9644
0.9592
0.9592
0.9487
Port Point
B1
B2
B3
B4
B5
B6
B7
B8
Q - ACFM
Qsd. DSCFM
Qs - SCFM
Os - SCFH
Temp Velocity
fF) (v)
322.0 70.71
322.0 71.11
322.0 71 89
323.0 71 55
323.0 72.33
323.0 71.94
323 0 71.94
323.0 71.15
Port Point
AI
A2
A3
A4
A5
A6
A7
A8
Test Parameters
Pb", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
PB - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
Project No. M2442068
Boiler #l Stack and Boiler #2 Stack
25.50
0.70
25.95
322.7
Circular
333
8.71
0.9156
0.9569
71.752
o/o CO2 8.60
o/o 02 5.50
% Nz 85.90
Md - dry basis lb/lb mole 29.60
Ms - wet basis lbflb mole 27.659
Bws - Moisture content frsction 0.167
Moisture determined by wb/db (Y or N) N
37 498
18.277
21 ,941
1,316,437
Page 66 of 157 @Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet
M244206
Compass Minerals Ogden, lnc
Ogden Plant
Boiler #2 Stack
6001
0 840
6
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Test Tech: RB
DP
(in. H2O)
0.91
0.93
0.95
0.92
0.91
0.92
093
0.93
Sqrt.
DP
0 9539
0.9644
0.9747
0.9592
0 9539
0 9592
0.9644
0.9644
Temp
fF)
323.0
323 0
322.0
322.0
322.0
322.0
322.0
322.0
Velocity
(v)
71.55
72.33
73 06
71 89
7l.50
71.89
72.28
72.28
DP
(in. HrO)
0.89
0.91
093
0.92
0.93
0.92
0.91
093
Normal
12
10t25t2024
12.02
12:22
AIR
6
Sqrt.
DP
0.9434
0.9539
0.9644
0 9592
0.9644
0.9592
0.9539
0.9644
Port Point
BI
B2
B3
B4
B5
B6
B7
B8
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Temp Velocityfrt u)
322.0 70.71
322.0 71.50
322.0 72.28
322.0 71 89
322.0 72.28
322.0 71.89
322.0 71.50
322.0 72.28
Port
A
A
A
A
A
A
A
A
Point
1
2
3
4
5
6
7
I
Test Parameters
Pb", - Barometnc pressure, inches Hg
Ps - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Seciional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fusec)
Project No. M2442OGB
Boiler #1 Stack and Boiler #2 Stack
25.90
0.70
25.95
322.1
Circular
333
8.71
0 9213
0 9598
71.946
o/o CO2 8.60
o/o 02 5.50
% Nz 85.90
Md - dry basis lb/lb mole 29.60
Ms - wet basis lb/lb mole 27.659
Bws - Moisture content fraction 0.167
Moisture determined by wb/db (Y or N) N
37,599
18,339
22,016
1,320,9s0
Page 67 of 1 57 OMostardi Platt
METHOD 4 MOISTURE DETERMINATION
Project Number: M244206
Client:
Facility:
Compass Minerals Ogden, lnc.
Ogden Plant
25 90
070
25 95
322
44.966
87.145
86 00
35 037
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
Meter Calibration (Y):
Meter Delta H (dH):
Sample Delta H (dH):
Test Location: Boiler #2 Stack
Test Date; 1012512024
Pressure, Barometric(Hg"):
Pressure, Static (H2O"):
Pressure, Stack (Hg"):
Temperature, Stack (oF):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
Meter Volume dscf:
lnitial tiJt: 2194.0
Final Y\lt: 2322.2
lnitial Volume: 870.5
Final Volume: 895.6
Water Vapor in Flue Gas (Bws): 0.171
End- 8 42
IMP FINAL INITIAL
776 5 710 3
755.3 715 1
790 4 768 6895.6 870.5
1
Normal
Start- 7:40
AIR
RB
0 987
1 862
1 900
Project Number M244206Client: Compass Minerals Ogden, lnc
Facility: Ogden Plant
Test Location: Boiler #2 Stack
Test Date: 1012512024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
Meter Calibration (Y):
Meter Delta H (dH):
Sample Oelta H (dH):
lnitial liJt:
Final tltJt:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws)
2
Normal
Start- 8:53
AIR
RB
End- 9:55
Pressure, Barometric(Hg"):
Pressure, Static (H2O):
Pressure, Stack (Hg"):
Temperature, Stack (oF):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
Meter Volume dscf:
25 90
070
25 95
322
88.010
1 30.1 07
88 00
34 841
0 987
1.862
1 900
2194.5
2316 6
872 1
900 6
0.169
FINAL INITIAL
771 .2 711 4
756.5 7i3 I
788 I 769 3
900.6 872 1
Project Numberi M244206Client: Compass Minerals Ogden, lnc.Facility: Ogden Plant
Test Location: Boiler#2 Stack
Test Date: 1012512024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
3
Normal
Start- 10:08
AIR
RB
Meter Calibration (Y):
Meter Delta H (dH):
Sample Delta H (dH):
lnitial VtJt:
Final tArt:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws):
End- 11:10
IMP FINAL INITIAL
771 3 714 j
763 5 717 3
788.1 770 I901.4 871.3
Pressure, Barometric(Hg") :
Pressure, Static (HrO"):
Pressure, Stack (Hg"):
Temperature, Stack ("F):
Meter lnitial Volume:
Meter Final Volumo:
Meter Temperature:
Meter Volume dscf:
25 90
070
25.95
323
31 102
73 170
89 00
34 754
0 987
1.862
1.900
2202.2
2322 9
871.3
901.4
0.'t 70
Project Number M244206Client: Compass Minerals Ogden, lncFacility: Ogden Plant
Test Location: Boiler #2 Stack
Test Date: 1012512024
Run Number:
Operating Level:
Time:
Test Engineer:
Test Tech:
4
Normal
Start- 1 1:20
AIR
RB
End- 12.22
Pressure, Barometric(Hg"):
Pressure, Static (HrO"):
Pressure, Stack (Hg"):
Temperature, Stack ("F):
Meter lnitial Volume:
Meter Final Volume:
Meter Temperature:
Meter Volume dscf:
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Meter Calibration (Y):
Meter Delta H (dH):
Delta H:
lnitial lrn:
Final vtrt:
lnitial Volume:
Final Volume:
Water Vapor in Flue Gas (Bws):
25 90
070
25 95
323
73 542
116 120
89 00
34 845
0 987
1 862
1.900
2202.2
2335.7
876.5
890.7
0.167
FINAL INITIAL
762 4 7152
750.1 7147
782.6 772 3
890.7 876 5
Page 68 of 157 OMostardi Plaft
Appendix E - Continuous Emissions Monitoring System Data and Plant Operating Data
UTAH DEPARTMENT OF
E NVI RC NIVIENTAL QUAL ITY
Proiect No. M2442068
Boiler #1 Stack and Boiler #2 Stack
DIVISION OF AIR QUALITY
Page 69 of 157 @Mostardi Platt
Boiler #1 Stack
TimeStamp Natural Gas Steam(lblhr) (klb/hr)
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
Boiler 102
(%l
TimeStamp
1.0/23/2024 09:26
1o/23/202a 09:27
t0/2312024 o9:28
to/23/2o2a 09:29
10/2312024 09:30
LO/23/2o2a o9:3t
Lol23/202a 09:32
tO/23/202409:33
L0/2312024 093a
tol23/202a 09:35
Lol23/202a 09:36
10123/2024 09:37
tO/23/2024 09:38
tO/231202a 09:39
to/231202a 09:aO
LO/23/2O2a O9:4L
tOl23l2o2a 09:a2
Lol23l2O2a 09:a3
tO/2312024 09:44
tOl23l2o24 09:45
Averages:
.FC800A .FT800B
4048.472168 77.967 88788
4042.244873 78.09705353
4037 .725586 78.22207 642
4049.577 88L 78.L090927 t
4046.94458 78.05661011
4057.44L406 78.10985565
403L.23828t 77 .703987 12
4035.516845 77.8953089
403r.337 402 78.0459442L
4044.890381 77.89788055
4045.224609 77.98730469
4042.896973 77.9626t597
4048.837891 77.99039459
4043.575293 78.0350647
4044.556L52 78.24475098
4040.sr.3915 78.31990814
4041.668213 78.7094574
4045.587158 78.41297046
4052.7 97 363 78.s3681 286
4042.887 939 78.05632019
4043.402 78.118
.Ar800Y
4.980
4.97L
5.285
4.972
4.983
4.995
s.006
5.018
5.Ot7
5.009
5.007
5.008
5.009
5.010
5.011
5.012
5.013
5.014
5.015
5.015
5.0L7
.Ar800x
6.0s9
6.L64
6.323
5.939
6.113
6.319
6.188
5.672
6.267
6.202
6.049
5.897
6.272
5.892
5.784
5.981
5.759
5.498
s.563
5.028
6.003
Nox
0.008
0.008
0.009
0.008
0.008
0.009
0.008
0.008
0.009
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 1
Project No M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 70 of 1 57 @Mostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lb/hr)
Steam
(klb/hr)
Boiler 102
(%)
Boiler l NOx
(ppm)
Nox
(lb/MMBtu)
TimeStamp
Lo/2312024 O9:a6
to/2312024 09:41
tol23/202a09:48
1o/231202a 09:49
1012317024 09:50
to/23/202a 09:51
10/23/2024 09:52
70123/202a 09:53
t012312024 o9:5a
L012312024 09:55
L012312024 09:56
tO/23/2024 09:57
Lol23/202a 09:58
L0/2312024 09:59
tOl23l2o24 Lo:00
LOl23l2O2a to:oL
to/231202a LO:o2
tOl23l2O24 70:03
LO/23/2024 LO:04
to/23/202a to:05
L012312024 Lo:06
Averages:
.FC800A
405L.t59424
4039.11792
4042,L5454L
4037.4546
4042.547779
4046.628662
4050.706299
4042.547607
4048.325928
4053.r.75049
4038.962158
40s1.319092
4032.755L27
4042.L65039
4060.5142]-9
4067.189209
4057.86328r
4039.235352
4048.34521.5
4039.113037
4043.829346
4046,20094
.FTSOOB
78.10596466
77.31495661
77.2778778L
77.35609436
77.44714355
77.57965088
77.5220642t
77.t256L798
77.224823
77.39756775
77.6377182
77.88337708
77.87377L67
77.63246978
77.54569244
77.4848938
77.54865265
77.77830505
77.75397497
77.85762238
77.72505t88
77.54886627
.Ar800Y
s.009
s.003
4.999
4.999
4.999
5.000
5.000
5.000
5.001
5.001
5.004
5.013
s.022
5.031
5.047
5.O72
5.056
5.042
5.025
4.972
5.01,4
5.015
.Ar800x
5.878
6.127
5.615
5.155
5.508
5.7t0
5.724
5.887
5.827
5.597
5.859
5.855
5.897
5.76L
5.009
5.503
5.780
5.084
5.944
6.220
5.986
5.852
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 2
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page71 ot 157 @Mostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lb/hr)
Boiler 102
(/")
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
Steam
(klb/hr)
TimeStamp
t0/23/2024 to:07
10123/2024 LO:08
10/23/2024 LO:09
!0/23/2024 LO:IO
L0/23/2O24 tO:tt
10/23/2024 Lo:12
70/2312024 Lo:L3
10/23/2024IO:1.4
10123/202a fi:75
10/2312024 to:1"6
to/23/20241o:t7
tO/23/2024 t0:L8
tO/231202410:t9
1O/23/202410:20
10/23/2024 tO:21
tO/23/202410:22
70123/202a Lo:23
tO/2312024 LO:24
10123/202a LO:25
70/23/202a LO:26
10/23/2024 LO:27
Averages:
.FC800A
4052.839844
4033.4071]-'5
4060.906738
4042.753662
4043.088379
4046.447266
4047.481201
4027.869L41
4062.458984
4057.883789
4053.193359
4033.5764L6
4036.388672
4043.7722t7
4038.079834
4044.776t23
4045.840575
4055.8393ss
4049.180654
4042.328857
4045.100098
4045.518552
.FT8OOB
77.6568756L
77.60L45559
77.60626984
77.55369568
77.17313232
77.83169556
77.7t96t975
71.7LL18927
77.65802002
77.43805695
77.54430389
77.469L0095
77.8690033
78.00904083
77.78007501
77.65306091
7732846069
77.23660278
77.24050L4
77.2048645
71.008s7544
77.56t83624
.At800Y
5.011
5.008
5.005
5.002
5.003
5.026
5.049
5.072
5.070
5.054
s.039
5.O24
s.008
4.993
4.964
4.940
4.939
4.937
4.935
4.934
4.933
4.997
.Ar800x
5.952
6.L78
6.080
5.972
6.164
5.220
5.976
5.854
s.930
5.t27
6.042
5.738
5.981
5.817
6.047
5.023
5.953
5.873
5.831
5.950
5.639
5.971
Nox
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 3
Proiect No. M2442068
Boiler #l Stack and Boiler #2 Stack
Page 72 ol 157 OMostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lblhr)
Boiler L 02
(/"\
Boiler l NOx
(ppm)
Nox
(lb/MMBtu)
Steam
(klb/hr)
TimeStamp
1012312024 LO:aO
L0l23l2O2a Io:4L
10/23/2024 t0:42
L012312024 to:43
L0/2312024 70:44
L0l23l2O2a tO:45
Lo/231202a LO:46
L0/2312024 t0:47
tol23l2o24 LO:aB
t0/23/2024 Lo:a9
L0/23/202a IO:5o
t0123/2024 LO:51
tO/23/202a IO:52
10/23/2024 t0:53
tol23l2o24 to:Sa
t012312024 Lo:55
LO/23/2024 t0:56
Lol23l2o24 tO:57
Lol73/2024 Lo:58
t01231202a fi:59
Lo/23/2024 t1:00
Averages:
.FC800A
4045.301514
4046.713193
4050.431152
4038.649902
4042.28t982
4046.948242
4043.800293
4024.427734
4035.993154
4045.082764
4040816162
4045.386475
4034.322998
4031.380859
4033.380371
4051.475098
4043.873232
4050.581543
4045.012595
4042.989074
4043.77661L
4041.866174
.FTSOOB
78.2t47522
78.13854136
77,98922729
78.4266037
77.96123505
78.20L51.52
78.08025123
17.9080429L
78.05935559
78.OL29775
77.9262390t
78.1s009308
77.46502686
77.48019409
77.74073029
77.8440094
78.11608887
78.31331635
78.24303436
78.00447845
78.LLL68671.
77.98863792
.Ar800Y
5.022
5.022
5.O2L
5.021
5.021
5.021
5.021
5.020
5.013
5.007
s.005
s.003
5.001
5.000
4.998
4.996
4.994
4.992
4.99L
4.985
4.979
s.006
.Ar800x
6.042
5.775
5.854
5.517
6,262
6.384
6.2tt
5.925
6.131
5.981
6.028
5.756
6.L27
6.02L
5.585
6.28L
6.009
5.145
6.347
s.981
6.425
6.043
Nox
0.008
0.008
0.008
0.008
0.009
0.009
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.009
0.008
0.009
0.008 RUN 4
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
l
Page 73 of 1 57 @Mostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lblhr)
Boiler 102
('/"1
Boiler 1 NOx
(ppm)
Nox
(lblMMBtu)
Steam
(klb/hr)
TimeStamp
t0/23/202411:07
Lol23/202a LL:02
Io/231202a n:03
1012312024 LL:04
Lol23/202a Lt:05
LO/231202a LL:06
tO/2312o241t:07
10123/202a LL:08
t0/23/2O24 tL:09
t0l23l2O2a LL:\O
tol23l2O2a t:fi
t0/23/2024 LL:t2
LO/231202a II:L3
7O/23/2o2a t:14
10123/202a fi;tS
10/23/2024 LL:L6
10/23/2024 tL:L7
10/23/2024 LL:18
10/23/202417:L9
7O/23/2o2a t:2o
tOl23l2O24 t1:21
Averages:
.FCSOOA
4042.87t826
4039.168457
405L.724509
4045.236572
4048.090575
4044.212t58
4026.787354
4046.62744L
4043.L20717
4048.013428
4043.822754
4042.Lr7788
4044.232666
4045.522705
4043.80L27
4050.22436s
4044.084473
4040.811035
4040.734L3L
4046.035133
4046.252451
4044.031494
.FT8OOB
77.94194464
77.881378L7
77.80927277
17.87L39L3
78.05185913
78.L6283417
78.73162231
18.LL999512
77.802t7743
78.04323578
77.86087036
77.96t16638
78.26753235
77.7850952L
77.82086945
77.7358322L
71.89855194
77.84900665
78.2L799469
78.07112885
77.9t673279
77.96342735
.Ar800Y
4.973
4.966
4.960
4.954
4.948
4.942
4.935
4.938
4.949
4.960
4.971.
4.983
4.994
5.005
5.0r.7
5.028
5.035
5.037
s.038
5.040
5.042
4.987
.Ar800x
6.277
6.277
6.066
6.361
6.080
5.958
6.272
6.rtz
6.066
5.831
5.91L
6.056
6.29s
5.838
6.t17
5.042
5.658
6.009
5.930
6.042
5.752
6.034
Nox
0.009
0.009
0.008
0.009
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 5
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 74 of 157 OMostardi Platt
Boiler #1 Stack
TimeStamp Natural Gas
(lblhr)
Steam Boiler L 02 Boiler L NOx Nox
(klb/hr) ('/,1 (ppm) (lb/MMBtu)
TimeStamp
Lol23l2o24 LL:22
L012312024 Lr:23
L0/23/202a fi:24
LOl23/2024 Lt:25
L0/23/2024 L7:26
r0/231202a L7:27
Lo/2312024 L7:28
10/23/2024 t7:29
L0/2312024 L7:3o
10/2312024 L7:31
to/23/202a LL:32
L0/23/202a 1133
tol23/202a L73a
t0/23/202a 11:35
L012312024 L1:36
t0/231202a LL:37
10/2312024 tL:38
Lol23l2o24 LL:39
LO/23/202417:40
LO/23/2024 t7:41
tO/2312024 71.:42
Averages:
.FC800A
4042.331543
4043.316895
4046.704346
4037.6L3525
4040.778076
405L.3t1279
4041.581543
4042.750732
4041.9129
4044.593018
4054.95L172
4043.746338
4044.01709
4045.476074
4045.448486
4046.57788t
4050.058604
4058.538818
4039.204345
4047.85620L
4050.145995
4045.132666
.FT800B ,Ar800Y
77.76934814 5.043
77.68522644 5.045
77.901.20697 5.047
77.91045898 5.048
77.7223053 5.035
77.95323t81 5.023
78.18157959 5.010
78.L92L6L56 4.997
77.85808563 4.992
77.94322205 5.000
77.83016968 s.007
77.63L06537 5.015
77.6955490L 5.023
77.8497t619 5.030
77.9295578 5.038
77.81367493 5.04s
77.81359863 5.053
77.8534L644 5.070
78.L4775848 5.091
77.69895t72 5.094
77.85406494 5.087
77.87625008 5.038
.Ar800x
6.028
5.897
5.752
6.2L6
5.953
5.941
5.789
5.859
6.066
5.738
6.040
5.897
5.981
5.927
5.775
6.276
5.831
5.595
5.615
5.7L4
5.808
5.890
Nox
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008 RUN 6
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 75 of 1 57 OMostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas Steam
(lb/hr) (klb/hr)
Boiler 102
%t
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
TimeStamp .FCSOOA .FT8OOB
LO/23/202a 7L:55 4054.429932 77.38L52313
LO/2312024 1.1.:56 4046.853027 77.43556158
t0/23/2024 Lt:57 4040.232666 77.52858734
LOl23/202a l:58 4043.958018 77.8824768L
tO/2312O2a l59 4043.9LL377 77.68948364
LO/23/202a D:00 4050.067383 77.7066L163
tO/231202a D:OL 4045.470703 77.49L93573
Lol23/202a L2:02 4040.9s3369 77.47085571,
ro/231202a D:03 404s.95ss75 77.49902344
lOl23l2O24 12:04 4043.62744L 77.58880515
L0123/202a L2:05 4048.526367 17.61304474
tOl23l2O2a L2:06 4048.699951 77.82483673
Lo/23/202a t2:07 4044.440918 77.66600037
lOl23/2024 12:08 4042.264LG 17.48778534
tO/2312024 L2:09 4042.31.44s3 77.13887024
tO/23/2024 12:tO 4047.6s2832 17.276545t
7O/231202a D:Ll 4042.307373 77.49430084
tOl23/2024 t2:12 4046.L33789 77Ss328s22
!0123/2024 L2:L3 4O4s.112949 77.84t27808
101231202a D:1.a 4043.75 77.9554O6t9
10/23/2024 L2:L5 4043.488281 77.3625t83t
Averages:4044.820032 77.5924t066
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
.At800Y
5.024
5.022
5.021
5.019
5.019
5.018
5.018
5.018
5.018
5.018
5.018
5.018
5.017
5.O17
5.019
5.O22
5.024
5.025
5.029
5.031
5.034
5.021
.Ar800x
5.930
5.784
5.794
5.755
5.988
5.981
s.609
5.911
6.047
5.755
5.653
5.817
5.634
5.934
5.933
5.752
5.859
5.972
5.780
6.089
6.009
5.853
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 7
Page 76 of 1 57 @Mostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lblhr)
Steam
(klb/hr)
Boiler 102
(%)
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
TimeStamp
t012312024 L2:t6
1o/231202a]2:I
to/23/202a L2:I8
101231202a D:79
1o/2312o2a D:20
10/231202412:2t
L0/231202a 0:22
70/2312o2a L2:23
t0123/202a L2:24
t0/2312024 t2:25
L0/23/2024 t2:26
Lo/2312024 L2:27
tol23l2o24 L2:28
to/23/202a D:29
LO/2312024 t2:3O
L0/23/2024 L2:3L
LO/231202 1-232
LO/23/2024 L2:33
t0123/202a t23a
LO/23/2024 t2:35
Lo/23/202a t2:36
Averages:
.FCSOOA
4046.80835
4042.524658
4045.681152
4047,0L8799
4044.098633
4047.518555
404t.772705
4055.592383
4048.609519
404s.89355s
4036.997559
4050.0847t7
4044.047363
4044.87LO94
4044.L162tL
4040.93872L
4042.52L973
4048.592529
4044.t54785
4049.342529
405L.L7334
4045.782544
.FTSOOB
77.s7629395
77.28069305
77.47708893
78.03990173
77.91537476
77.79071808
71.2LL24268
77.6L292261
77.8L950378
77.93808746
78.08649445
78.14388275
78.24909973
77.99276733
77.58909607
77.2557825
77.1503067
76.96279907
76.99643707
76.51048889
77.t283493
77.56302t85
.Ar800Y
s.036
s.039
5.040
5.039
5.037
5.035
5.031
5.027
5.023
5.019
5.036
5.058
5.O72
5.067
5.061
5.055
5.050
5.045
5.039
5.034
5.030
5.042
.Ar800x
s.939
5.864
5.733
5.897
5.782
5.803
5.972
5.672
5.937
5.949
s.688
5.489
s.985
6.L92
6.055
5.606
5.5s9
6.014
5.574
5.578
5.747
5.805
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 8
Project No. M2442068
Boiler #1 Stack and Boiler #2 Slack
Page77 ol'157 OMostardi Platt
Boiler #1 Stack
TimeStamp Natural Gas
(lblhr)
Boiler 102
(/"\
Boiler 1 NOx
(ppm)
Nox
(lblMMBtu)
Steam
(klb/hr)
TimeStamp
LOl23l2o2a 72:37
t0/23/202a ].238
LOl23l2o2412:39
tol23/2o2a D:4o
7o123/2024 L2:4t
70/23/2024 t2:42
to/23/202a L2:43
10/231202412:44
70/23/2o2412:45
10/2312024 D:a6
70/23/2024 L2:a7
IO/2312024 t2:48
tOl23/202a L2:49
L0123/202a L2:50
LOl23/2024 L2:5L
L0/23/2024 L2:52
LO/23/2024 L2:53
tO/23/2024 t2:54
t0/23/2a24 t2:55
L0/23/2024 L2:56
LO/23/2024 t2:57
Averages:
.FCSOOA
4048.562988
4051.71997L
4047.057373
4045.81372t
4044.910645
4045.182861
4043.18042
4054.422LL9
4044.398682
4047.02832
4048.305564
4041.514893
4051.710693
4044.04t748
40s0.1s3075
4049.737051
4047.775635
4043.7229
4046.510985
4046.t34277
4051.709961
4047.25L55
.FTSOOB
76.97624969
77.24412537
76.98564911
75.998LO797
77.2t404265
77.02L03424
77.72448883
77.77723846
77.44920349
77.5098L14
77.29754539
77.2L498871.
77.22853088
77.33224487
77.19406L28
77.33343506
77.21.64911
77.30601501
77.42604055
77.6LL49597
77.34456635
77.26145592
.Ar800Y
5.028
5.026
5.023
5.021
5.019
5.017
5.011
5.004
4.996
4.996
4.998
4.999
5.000
5.00L
5.002
s.004
5.004
5.000
4.996
4.992
4.988
5.005
.Al800x
5.789
5.094
5.993
5.525
5.784
6.033
5.798
5.911
5.841
6.075
5.536
5.826
5.892
6.089
5.541
6.019
5.014
6.169
5.822
6.080
5.953
s.905
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 9
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 78 of 1 57 OMostardi Platt
Boiler #1 Stack
TimeStamp NaturalGas
(lb/hr)
Steam
(klb/hr)
Boiler L 02
(%l
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
TimeStamp
1012312024 L3:L5
to/231202a B:$
L0/23/202a B:L7
r0/2312024 t3:L8
rO/2312024 L3:L9
L0123/202a B:20
LO/2312024 L3:2t
LOl23/202a B:22
t0/23/202a B:23
Lol23/2024 B:2a
10/23/202a B25
LOl23l202a 8:26
Lo/23/202a B:27
LO/2312024 73:28
10/23/202a B:29
Lo/23/202413:30
tO/2312O2a L3:31
L012312024 73:32
t0123/2024 t3:33
7O/23/202a 133a
7O/2312O2a ].335
Averages:
.FCSOOA
4048.610596
4040.842285
404s.622803
4039.3076L7
4048.53125
4044.427002
4039.265381
4048.262695
4047,8286t3
4042.759277
4045.592529
4042.592529
4043.87915
4044.536377
4045.318604
4042.979248
4044.7s9033
4042.43457
4041.455566
4036.048095
4059.40625
404/..292444
.FTSOOB
77.6179L992
77.60839081
77.76037598
78.08508301
78.23979t87
78.30543518
78.20367432
78.154106t4
78.0386352s
71.798622L3
77.50946808
77.40005493
77.61329407
77.56356872
77.73666382
77.77889252
77.535L6235
77.7451.5533
77.95871735
78.09986877
78.03466797
77.86648L4
.Ar800Y
4.976
4.973
4.970
4.966
4,970
4.975
4.980
4.985
4.988
4.992
4.996
5.000
5.004
s.008
5.012
5.016
5.020
5.003
4.984
4,978
5.009
4.992
.At800x
s.930
5.014
5.742
6.005
s.803
6.118
6.052
5.939
5.838
5.794
6.314
5.822
5.094
5.747
5.827
5.599
5.822
5.915
6.047
5.667
5.939
5.908
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 10
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 79 of 1 57 @Mostardi Platl
Boiler #1 Stack
TimeStamp Natural Gas
(lb/hr)
Boiler 102
%t
Boiler l NOx
(ppm)
Nox
(lblMMBtu)
Steam
(klb/hr)
TimeStamp
10123/2024 L3:36
LO/231202a 837
to/23/202a ]-338
LOl23l2O2a ].339
LOl23l2O74 B:aO
tOl23l2o24 B:aL
tO/23/2024 L3:42
tol23l2O24 73:43
tol23l2O2a B:44
7012312024 73:45
Lol23l2o24 73:45
101231202413:47
70/2312024 B:aB
LOl23l2O24 73:49
70/2312024 73:50
to/23/2o2a B:St
10/231202a B:52
].,O/23/2024 L3:53
10123/2024 t3:54
10123/202a B:55
L0/2312O2a 8:56
Averages:
.FC8OOA
4038.t78457
4036.4326t7
4050.624258
405L.072266
404L,794922
4047.75
4047.0979
4044.92456L
404s.s39063
4048.002586
4060.L71875
4044.237793
4047.740967
404s.657959
4037.L29L5
4047.509277
4049.056396
4043.9892s8
4047.742676
4044.053223
4039.908691
4046.021777
.FTSOOB
77.5540008s
77.01289368
77.4r7LL426
77.89295197
77.81988525
78.L3925L7L
77.73060608
77.7L335602
77.78443L46
77,67057037
77.57287598
77.65996552
77.8594L3L5
77.78894043
78.16855521
78.10978699
78.20674133
77.99732538
77.55534363
77.32067108
77.72507477
77.75698776
.At800Y
5.029
5.O27
5.O24
5.022
5.020
5.0r.8
5.015
5.013
5.011
5.008
5.028
5.032
5.O24
5.015
5.008
5.000
4.992
4.983
4.975
4.967
4.975
5.008
.Ar800x
5.930
5.958
6.778
s.897
5.934
5.915
5.874
6.351
5.911
s.893
5.864
6.108
5.64L
5.878
5.948
5.817
5.066
5.183
5.852
6.014
5.728
5.951
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 11
Project No. M244206B
Boiler #1 Stack and Boiler #2 Stad
Page 80 of 1 57 @Mostardi Platt
Boiler #1 Stack
TimeStamp Natural Gas
(lb/hr)
Boiler 102
%t
Boiler 1 NOx
(ppm)
Nox
(lb/MMBtu)
Steam
(klb/hr)
TimeStamp
tol23l202a B:57
LO/23/202413:58
L0/23/2024 L3:59
to/23/202a \a:oO
tO/2312024 t4:OL
LOl23/2024 74:02
1012312024 L4:o3
1012312024 L4:04
7ol23l2O2a M:o5
7012312024 La:06
L012312024 La:01
10/23/202a La:08
L0/23/202a La:09
t0123/2024 t4:Lo
t0/2312024 r4:tL
10/231202a M:I2
LO/2312024 L4:t3
L012312024 L4:L4
r0/231202a L4:L5
1Ol23l2O2a La:LG
tol23/202414:\7
Averages:
.FC800A
4047.055908
4040.359619
4051.550059
4041.919678
4044.L875
4042.85376
4047.989746
4035.435791
4039.359853
4042.790777
4044.9646
4045.039551
4043.98t445
4049.512695
4037.73999
4044.LL914L
4045.778564
4043.236815
4051.28418
4042.677734
4045.64L846
40,44.071667
.FT8OOB
77.8243L793
77.9320755
78.0123s199
77.43610382
77.7649002t
77.65983582
77.53747559
77.64t56342
77.72778048
77.3175354
77.50758362
7739717102
77.4t099548
77.2267t509
77.OO9LL7L3
77.23253632
77.78588L04
78.00939178
77.93384552
77.80387rLs
77.04403687
77.569s0836
.At800Y
4.983
4.990
4.998
s.006
5.014
5.021
5.029
5.037
5.O42
5.025
5.007
4.989
4.972
4.954
4.95L
4.979
5.007
4.933
5.018
5.013
4.993
4.999
.Ar800x
6.000
5.822
6.155
5.714
5.841
5.677
5.958
6.122
5.578
5.644
5.700
5.503
5.019
s.986
5.902
5.728
6.169
5.953
5.705
6.023
5.915
5.856
Nox
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0,008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 12
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 81 of 157 OMostardi Platt
Boiler #2 Stack
Timestamp Natural Gas
(lb/hr)
Steam
(klb/hr)
o2
l%l
NOx NOx
(ppm) (lblMMBtu)
Timestamp
t0/25/202a 07:a0
7012512024 O7:47
701251202a 07:42
7O1251202a 07:a3
7012512024 07:44
L012512o24 07.a5
1o12512024 07:46
L012512o24 07:47
L012s12024 07:48
LOl25l2024 07:49
L012512o24 07,5o
7012512024 07:5L
].012512024 07:52
7012512024 07:53
701251202a 07.54
t0/2512024 07:55
t0/25/2024 07:56
t0/25/2O24 07:57
tO/25/2024 07:58
tO12512024 07:59
10/25lZoZao8:oo
Averages:
.FC8O14
4078.691162
4082.840576
4078.982422
4085.321777
4082.044922
4083.64502
408t.786377
4079.090576
4081.01709
4080.447266
4083.708984
4079.572s7
4078.081787
4077.119873
4074.5t4t6
4080.870605
4080.223633
4080.631592
4083.452881
4083.543213
4081.452881
4080.917407
. FT8O 1B
81.44019318
80.96554565
81.01989746
80.84307098
80.88180542
81.62746759
81.40781403
81.84657288
81.70061493
81.55104065
81.40855408
87.97743469
81.48986053
81.23194885
8t.42246246
81.63485481
81.31867981
8t.42297363
81.62215424
81.64212036
81.79115295
81.€70018
.Ar800Y
5.43595314
5.56094s034
5.491111755
5.532086849
5.437589781
5.497933388
5.551580906
5.415629864
5.490L19457
5.499063492
5.548287392
5.529163837
5.572335777
5.572354794
5.440303802
5.614330769
5.392237186
s.3860001s6
5.415109634
5.490605354
5.527942657
5.495
.Al800X NOx
6.159349918 0.009
5.924972057 0.008
s.s68810463 0.008
s.8s479764L 0.008
6.74965774
5.507819176
5.660202503
6.178100109
5.803170204
5.934368134
5.845357895
5.592202663
s.050806046
5.714028835
5.915579796
5.475075245
6.007056236
5.597090727
5.63920784
5.592262268
5.770244s98
5.739
0.009
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 1
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 82 of 157 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lb/hr)
Steam
(klb/hr)
o2
(%l
NOx NOx
(ppm) (lb/MMBtu)
TimeStamp
101251202a 08:0t
70125/202a 08:02
1012512024 08:03
7012512o24 08:0a
L01251202a08:05
L0125/202a08:06
t012512024 08:07
tol25l2024 08:08
7012s1202a 08:09
1012512o2a o8:7o
70/25/2024 08:tt
701251202a 08:72
101251202a o8:t3
70/251202a 08:u
70125/202a o8:tS
101251202a o8:t6
1012512024 o8:t7
t012512024 O8:t8
7O12512024 08:19
101251202a 08:20
1O1251202408:21
Averages:
.FC8O1A
4080.3L5674
4074.050049
4073.806885
4077.399414
4080.230957
4083.237793
4078.86t572
4083.454346
4081.957764
4079.585449
4081.35376
4081.105713
4084.96167
4085.395264
4083.055396
4081.688232
4084.813965
4080.707031
408L.877L97
4076.986816
4076.987549
4080.575891
. FT8O1 B
87.62077997
87.5170577
81.282t4254
81.4509964
81.58848572
80.99719238
81.48258209
81.24786377
81.75730896
81.6411972
81.56736322
81.75481415
81.37913513
8L.72624969
81.69502258
81.51487732
81.57084656
81.66939545
87.4757843
81.81577301
81.42593384
81.52770081
.At800Y
5.651310921
5.515002251
5.433551311
5.545302868
5.519343853
5.4273t7142
5.58423233
5.549985409
5.534363747
5.52266264
5.429763794
5.473036766
5.419551849
5.414999962
5.396837234
5.53273201
5.395338535
5.444952488
5.45468235
5.548327923
5.525548386
5.483
.Al800X NOx
5.498567104 0.008
5.592191219 0.008
5.756227493 0.008
5.882788181 0.008
5.817742963 0.008
6.140545845 0.009
5.934391499 0.008
5.789098263 0.008
5.442209727 0.008
5.657812595 0.008
5.117059708 0.009
5.873437405 0.008
5.287499905 0.007
5.82626152 0.008
5.889932156 0.008
5.643856049 0.008
5.786716467 0.008
5.985937595 0.008
5.643598692 0.008
5.470470428 0.008
5.798263073 0.008
5.767 0.008 RUN 2
ProJect No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 83 of 1 57 OMostardi Platl
Boiler #2 Stack
Timestamp Natural Gas
(lblhr)
Steam
(klb/hr)
o2
%t
NOx
(ppm)
NOx
(lblMMBtu)
TimeStamp
70/25/202408:22
70125/202408:23
!o12s12024 08:24
tol25l202a08:25
L012512024 08:26
tol25l202a 08:27
L01251202a 08:28
7o1251202a08:29
t012512024 08:30
t0/25/2o2408:31
LOl25l2024 08:32
t0125/2024 08:33
L0/25/2024 08:34
LO/25/2024 08:35
L0/2512024 08:36
LOl25l2O24 08:37
Lol25l2o2a 08:38
Lol25/2o24 08:39
1o1251202a 08:a0
tol25l202a 08:a1
tOl25l2024 08:42
Averages:
.FC801A
4081.98291
4080.425293
4083.4204t
4083.68042
4087.949707
4083.589844
4082.453369
4087.763428
4078.656738
4081.783447
4079.L25
4079.725318
4081.967285
4085.84375
4084.46t9L4
4079.OOO244
4077.225098
4080.3125
4086.873727
4085.226807
4085.731201
4082.757825
.FT8O1B
81.35067749
81.45838165
81.55052948
81.64051056
81.3511734
81.22960663
8L.32876587
81.13581085
80.51069489
80.6496048
80.84999084
80.93093872
81.23828888
81.19153s13
87.42250061
81.69672394
8t.876274LL
82.14531708
81.77140808
81.83356476
81.90222931
81.39069748
.At800Y
s.52093792
5.49060154
5.34073019
5.504659176
5.439143658
5.490604401
5.463254452
5.450000753
5.541692734
5.568645
5.546855927
55t8082142
5.4226t7435
5.484366417
5.37501812
s.430848122
5.40381813
5.47030115 1
5.437498093
5.262562275
5.429675702
5.454
.Ar800x
5.676472664
5.629746437
5.690526485
5.779804707
5.446801662
5.579675674
5.548463821
5.798406601
6.773392296
5.747032166
5.615691185
5.910935402
5.709374905
5.27t907806
5.953181267
5.573560238
6.LL2354755
5.611036301
5.6t70277L8
6.131072998
6.028113355
5.796
NOx
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.009
0.008
0.008
0.009
0.008
0.008 RUN 3
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 84 of 157 @Mostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lblhr)
Steam
(klb/hr)
o2
(%l
NOx
(ppm)
NOx
(lb/MMBtu)
TimeStamp
tol25l2o24 08:53
Lo/2512o2a o8:5a
t012512024 08:55
701251202a 08:56
1012512024 08:57
10/251202a 08:58
1012512024 08:59
1012512024 09:oo
7012512024 o9:0t
t0/2512o2a o9:o2
10125/2024 09:03
701251202a 09:oa
101251202a 09:05
1012512024 09:O6
70/25/2024 09:07
701251202a 09:08
1012512024 09:09
t1l25l2o2a 09:70
1012512024 O9:tt
101251202a 09:72
701251202a 09:73
Averages:
.FC8O1A
4078.730713
4083.04126
4077.750977
4080.379883
4081.889648
4077.OO7324
4085.092529
4081.509521
4076.50t465
4079.s8252
4088.388916
4082.764893
4083.547607
4083.919434
4075.943115
408L.982422
4083.104736
4086.705566
4083.9375
4085.21997t
4080.663574
4081.946643
. FT8O1 B
81.50535583
81.04573059
81.30267334
80.9830246
81.1048584
80.71517181
81.20237732
81.08526611
80.9994s068
80.89505768
81.06739807
80.77991486
80.87759318
80.70584869
84.24295807
81.04348755
80.7926ss94
80.s 1332092
80.98265076
80.92738342
80.58260193
80.8974762
.Ar800Y
5.415620804
5.44375658
5.54298687
5.612500191
5.550948849
5.484382629
5.494515896
5.602050304
5.541930199
5.539011002
5.540603638
5.500747681
5.552013874
5.407186031
5.53438282
5.534779072
5.398s2s715
5.485931396
5.514080048
s.488025188
5.444273949
5.511
.Ar800x
5.98127222t
5.87109375
5.685990334
5.72812s095
5.84054184
5.700041294
5.592208385
5.686286449
5.8828L8222
5.653185368
5.296841145
5.728043079
5.638991356
5.817229748
5.840515614
5.367131233
s.699917793
6.05 1573753
5.587575436
5.611016273
5.929601192
5.710
NOx
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008 RUN 4
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 85 of 1 57 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lb/hr)
Steam
(klb/hr)
o2
%t
NOx
(ppm)
NOx
(lb/MMBtu)
Timestamp
70125/2o2a 09:7a
7012512024 o9:t5
rol25l202a 09:76
10125/2024 09:77
7012512024 09:18
tol25/202a 09:79
t0l25l2024o9:2o
t01251202a 09:27
t0125/2o2a 09:22
Lol25l202a 09:23
LOl25l2024 09:24
tol25l202a09:25
L0125/2o2a 09:26
tOl25l2O24 09:27
7012512024 09:28
LOl25/2024 09:29
tol2sl2o2a 09:30
tOl25l2O24 09:37
1O12512024 09:32
tol25l202a 09:33
1012512024 09:34
Averages:
.FC8014
4067.447266
4078.752197
4078.875732
4081.27724
4079.707178
4086.383301
4085.855479
4084.657775
4088.307517
408s.28833
4072.890869
4080.723877
4083.647705
4082.805664
4096.72119L
4091.045654
4081.015625
4078.781738
4077.095947
4082.010254
4086.913574
4083.1580/t4
.FT8O1B
80.71386719
80.89281464
80.58203125
80.9s668793
80.84605408
80.688591
80.75110626
80.84443665
80.545761 11
80.45679474
80.7758tO24
80.36262512
80.42246246
80.763626L
80.18162537
80.32045s09
80.5004425
80.57523956
80.37651825
80.11093903
80.329307s6
80.56916695
.Ar800Y
5.455275463
5.486744404
5.404847145
5.454748631
5.552052498
5.566918373
5.606181145
5.651562691
5.47766161
5.515650749
5.499271393
5.5226264
5.666588783
5.526540756
5.584389687
5.483537197
5.659376144
5.55858469
5.544291019
5.604198933
s.630000114
5.550
.Ar800x
5.784448747
5.503040791
5.882271767
5.948477268
5.798509121
5.498512745
5.615772724
5.915636063
5.6719594
5.517309655
5.653006077
5.695420265
5.683723927
5.601483345
5.456355572
5.99987793
5.821969032
5.507820129
5.79843759s
5.4609375
5.282865047
s.666
NOx
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 5
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 86 of '157 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas Steam
(lblhr) (klb/hr)
NOx
%l (ppm) (lblMMBtu)
TimeStamp .FC801A .FT801B .Al800Y .Al800X NOx
101251202a09:35 4o8s.299072 80.s5909729 s.701s19966 5.334566593 0.008
L0/25/202409:36 4085.502t97 80.56784058 5.643750191 5.699999809 0.008
tOl25/2O2409:37 4075.504395 79.98726654 5.723437309 5.tt642L7 0.007
t0/251202a09:38 4084.13501 80.2183609 5.558200836 s.6s7688618 0.008
t0l25l2O2a09:39 4089.143555 80.16403961 5.584270954 5.825031281 0.008
t012512O2409:40 4087.270264 80.0730896 5.517161369 5.803099155 0.008
t0l25l2o24o9:at 4083.688965 80.277492 5.541060448 5.051370144 0.009
tll25l202409:42 4079.68457 80.30522919 5.504695415 5.545355797 0.008
101251202409:43 4083.615967 80.14513397 5.49648428 5.798394203 0.008
101251202409:44 4078.590332 80.00319672 5.55233L924 5.573422432 0.008
t01251202a09:a5 4080.477969 80.04560034 5.698409081 5.175025453 0.007
t01251202409:46 4073.429688 80.33114624 s.587348461 6.0s62s9632 0.009
101251202409:47 4077.114258 80.t64L922 5.509878159 5.859352112 0.008
1012512024o9:a8 408s.307129 80.03798676 s.463015079 s.939093s9 0.008
!0125/202aO9:a9 4081.881835 80.14772034 5.512s53215 5.545331478 0.008
t01251202409:50 4081.80835 80.04710388 5.490624905 5.695323944 0.008
t0/25/202409:57 4086.990234 80.09s36743 5.4566483s 5.777340472 0.008
tOl25l2O2a 09:52 4088.393066 79.96337128 5.536079407 5.7L8682289 0.008
70/25/202409:53 4080.925537 79.9t583252 5.558195343 5.728074074 0.008
tol25l202409:54 4077.!23779 80.0398407 5.569479465 5.629462242 0.008
701251202a09:s5 4O83.62L826 79.78134155 5.601583958 5.301552309 0.008
Averages: 4082.257U0 80.11530762 5.556 5.675 0.008
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
RUN 6
Page 87 of 1 57 @Mostardi Platt
Boiler #2 Stack
Timestamp Natural Gas
(lblhr)
Steam
(klb/hr)
o2
(%)
NOx
(ppm)
NOx
(lblMMBtu)
TimeStamp
70/2512024 t0:08
t0/2512024 t0.o9
t012512024 t1Lo
L0/25/2024 t}:tt
to12512024 70:t2
t01251202a t0:t3
t012512024 to:t4
70125/2024 t0:75
L012512024 t0:t6
LO(2512024 L0:77
lol25l2O2a fi:B
1012512o2a 70:79
LOl25l2O24 t0:2O
LOl25l2O24 tO:2t
Lol25l202a 70:22
701251202410:23
t012512024 to:24
70/2512024 to:25
1012512024 70:26
t0/25/202410:27
101251202a fi:28
Averages:
.FC801A
4084.999756
4088.415504
4085.347656
4087.387207
4072.907471
4073.248047
4085.392578
4083.180908
4084.956787
4088.56665
4081.995338
4083.795654
4082.058359
4064.363037
4080.449951
4087.246094
4083.691406
4079.53247t
4075.774658
4088.611816
4083.716309
4082.032t195
.FT8O1B
79.97433472
79.88528442
80.03199768
79.96715546
79.736t4502
79.61373901
79.5967636t
79.67215729
79.73422247
79.67917633
79.77902222
79.69736047
79.69780731
79.s972323
79.66509247
79.75727747
79.73197937
79.s94s3583
79.71992493
80.2702484t
80.22969055
79.78223763
.At800Y
5.576537609
5.43687582
5.546859741
5.52576828
5.s15128136
5.517268658
5.51s63930s
5.592166901
5.514377594
5.549375965
5.460917751
5.473482609
5.432947!59
5.52341795
5.5740t2756
s.464103222
s.357817773
5.534377575
5.47743082
5.540600777
5.678070058
5.512
.Ar800x
5.377428055
5.662435055
5.709344864
5.698444366
5.484375
6.159347057
5.75620079
5.493772984
5.674197674
5.605277943
5.845312595
5.709374905
5.77962L60L
5.287668705
5.4375
5.751534939
5.482001781
5.2t7277527
5.4138484
5.756424427
5.156400204
5.604
NOx
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.007
0.008
0.008
0.007
0.008 RUN 7
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 88 of 1 57 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lblhr)
Steam
(klb/hr)
o2
(%l
NOx
(ppm)
NOx
(lblMMBtu)
TimeStamp
!0125/202a fi:29
t0/2512O2a fi30
t0/25/2o2a 70:3t
t0/251202a 70:32
7012512024 70:33
701251202a 70:34
101251202a 70:35
t012512024 t0:36
to/25/2O2a fi37
t0/25/2o2a 70:38
L0125/2O2a 1039
t012512024 t0:40
70/25/2024 70:41
10125/2024 to:42
70125/2024 70:43
7012512024 t0:44
701251202a 70:a5
L012512o24 fi:a6
7012512024 70:47
t0/25/2024 70:48
t012512024 70:49
Averages:
.FC8O1A
4080.31958
4083.855225
4081.293701
4087.11792
4078.865967
4079.864502
4085.936758
4080.776025
4083.10376
4078.81555
4083.057861
4082.877768
408s.512061
4086.432129
4082.0s0293
4082.6t4258
4075.496094
4074.548584
4081.348633
4093.163574
4080.530127
4082.339795
.FT8O1B
80.18029785
80.1033783
79.78781891
79.45618439
79.32979372
78.98294067
78.99663544
78.72740936
78.38743597
78.7933197
79.74450073
79.32356262
79.48554993
79.68346405
79.0930ss73
79.54965973
79.41981505
79.47583008
79.3614502
79.27739282
79.12554t69
79.27490692
.Ar800Y
5.492199898
5.507773399
5.629123688
5.512501717
5.614024639
5.510418415
5.55676651
5.577747203
5.580377579
5.4047t3631
5.467164474
5.575307846
5.590567112
5.455268383
s.443784714
5.595311642
5.5538225L7
5.5219426t6
5.567053699
5.621860981
5.492184L62
5.541
.Ar800x
5.779687881
5.74686718
5.582726002
5.620324t35
5.746967177
6.13 108 1 104
5.599291801
5.444394588
5.400043488
5.498381515
5.550048828
5.685914993
5.404798985
5.69985342
s.758626467
5.423520565
5.784263611
5.498381138
5.667311658
5.757457214
5.564059734
5.628
NOx
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 8
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 89 of 1 57 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lblhr)
Steam
(klb/hr)
o2
(%)
NOx NOx
(ppm) (lb/MMBtu)
Timestamp
t0/25/2024 t0.50
7012512024 t051
Lo/2512o2a to:52
tol25/202a t0:53
L0/251202a t0:5a
Lol25l202a 70:55
t0l25l2o2a 70:56
tol25l202a t0:57
Lol25l202a 70:58
tOl25/2024 L0:59
LOl25l2O24 tt:oo
Lol25l202a 77:01
LO{2512024 77:02
1012512024 71:03
L0125/2024 7t:O4
!Ol25l2O241t:05
tOl25/2024 7t:O6
t0/2512024 7t.o7
LO{2512024 7t:OB
tO{2512024 71:09
70125/2024 tt:to
Averages:
.FC8O1A
4080.841797
4085.427734
4085.707764
4088.106201
4088.437256
4085.340332
4076.410889
4078.82788t
4079.27724
4080.627686
4083.734131
4080.30102s
4083.527832
4087.244629
4078.920166
4087.243164
4083.669434
4079.671387
4081.005371
4083.739014
4080.899902
4082.60s6s2
.FT8O1B
79.32638ss
79.33989716
79.L6366577
79.09177786
79.39739227
79.05036926
79.2901001
79.t5844727
79.7L454773
79.77534637
78.83699799
78.91866302
78.99923706
79.08175659
78.89747949
79.16455841
78.78283691
78.71569061
78.97686005
78.924t0278
79.03681183
79.05549393
.At800Y
5.596033573
5.509346962
5.570314884
5.463561535
5.542006016
5.555077076
5.62555735
5.517995834
5.64745378s
5.502587795
5.526554585
5.58687L624
s.547637939
s.s31248569
5.455220222
s.51992178
s.482904434
5.517187595
5.428248882
5.60s633736
5.560936451
5.535
.Al800X NOx
5.455260681 0.008
5.645273209 0.008
5.568946838 0.008
5.423405647 0.008
5.730457783 0.008
5.995318413 0.008
5.639101028 0.008
6.192049026 0.009
5.395277023 0.008
5.8t2494278 0.008
s.268744469 0.007
s.6s7869339 0.008
5.53600502 0.008
5.376574039 0.008
6.009386063 0.008
5.377907234 0.008
5.789045811 0.008
5.653124809 0.008
5.68LLL4674 0.008
5.38595438 0.008
5.723304749 0.008
s.643 0.008 RUN 9
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 90 of 157 @Mostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas Steam o2
(%l
NOx
(ppm)
NOx
(lblMMBtu)(lblhr) (klb/hr)
TimeStamp
t0/2512024 tL:20
t0/25120241L:21
t012512024 tL:22
t012512024 tt:23
70125120241L:24
!01251202a fi25
1012512024 LL:26
t012512024 tt:27
t0/25/2024 LL:28
101251202a Lt:29
to12512024 Lt:30
1012512024 7L:31
70125/2024 LL:32
10125/2024 tL:33
70/2512024 LL:34
101251202a L7:35
70125/202a 1136
tOl25l2024 tt:37
tOl25l2024 LL:38
tol25l2024 tL:39
t01251202a Lt:aO
Averages:
.FC8O1A
4079.478707
4085.495605
4078.848145
4084.041016
4083.869385
4083.690186
4084.302734
4082.109619
4080.554443
4085.2tt9].4
4086.787LOg
4085.1O7422
4081.150391
4086.293945
4083.826416
4091.598242
4085.363525
4083.466309
4079.860107
4085.389404
4082.118408
4083.959216
.FT8O1B
78.54566193
79.01860046
79.0276947
78.55316162
78.45283508
78.54L96t57
78.08145t42
78.21986389
78.2155304
78.80810547
78.78133392
78.68054199
78.60289764
79.103546L4
79.2726593
79.50038147
79.29104674
79.04923248
79.1338501
79.3337t735
79.3L967163
78.84940414
.Ar800Y
5.433127403
5.45t923847
5.54208374
5.4832tt994
5.507801533
5.504589217
5.517972946
5.437506675
5.508592606
5.498423L
5.460943699
5.490631104
5.534070969
5.404738426
5.479728699
5.427566528
5.556130886
5.465174675
5.582793236
5.4432L3463
5.389109135
5.484
.At800x
5.470274925
5.685937405
s.601486206
5.567797227
5.934310436
5.798245907
5.695148945
5.676534176
5.57722908
6.O74958324
6.342718263
5.737567226
5.72807598t
5.437551498
5.745856703
5.737548828
5.728172779
5.939101219
5.706980705
6.046845913
5.615595818
5.771
NOx
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008 RUN 10
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 9"1 of 157 OMostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas Steam 02 NOx(lblhr) (klb/hr) (Y,) (ppm)
NOx
(lb/MMBtu)
Timestamp .FC801A .FT801B .Ar800Y .At800x
L01251202a t:at 4082.336182 79.OG124878 5.494957924 6.215487003
L0/25120241L:42 4080.63208 78.90682983 s.520306969 s.831250191
tOl25l2O2a]1:a3 4O8L.247803 78.78805542 5.384737968 5.90625
L0l25l2024lt:44 4084.345947 78.8968811 5.598449707 5.357999802
t01251202a77:a5 4080.238037 79.!!703497 5.576510906 5.592187405
t0l25l2024tt:46 4087.005859 79.05513 5.436089039 5.L72634725
L012512024 71:47 4082.321777 78.8L649Ot7 5.401648998 5.66242075
L012s12024 tt:48 4084.169922 78.7L076202 s.s84302902 s.344134331
L0/251202411:49 4081.938232 78.77537482 5.609684467 5.664116383
tOl25/2024 11:50 4082.865967 78.60887909 5.524999142 5.732676983
LOl25l2O24 11:51 4078.861572 78.84t77399 5.486774445 5.868577003
L01251202a fl52 4078.976074 78.59094086 5.609334469 s.967t473s
LO|25/2O247L:53 4078.853s2s 78.7109746L 5.51406765 6.028089045
LOl25l2O2411:54 4088.575439 78.64378357 s.39545393 5.807748795
L012512024 t7:55 4089.601807 78.44789124 5.620521681 5.538328648
tOl25/2O24 7t:56 4072.00293 78.27189636 5.490799427 5.674056067
tol25l2o24 t!:57 4O73.3994t4 78.15768433 5.57924366 5.549943924
L0125/2024 11:58 4073.734L3L 78.0357437L 5.456362247 5.58750391
7012512024 tL:59 4073.404297 78.2tOO9827 5.64s553112 5.306336403
LO12512024 t2:00 4079.02!729 78.05582428 5.64023447 5.596945286
L0l25l2O2a D:Ot 4090.228271 78.20737787 5.668758869 5.404706001
Averages:4081.077747 78.s9727832 5.542 5.630
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
NOx
0.009
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.008
0.008
0.008
0.009
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.008 RUN 11
Page 92 of 1 57 @Mostardi Platt
Boiler #2 Stack
TimeStamp Natural Gas
(lb/hr)
Steam
(klb/hr)
o2
(%)
NOx
(ppm)
NOx
(lb/MMBtu)
TimeStamp
7012512o2a L2:02
10/25/2024 t2:03
L0/2512024 72:04
7012512o2a t2:05
!01251202412:06
1012512024 t2:07
10125/2024 !2:08
tol25l202a L2:09
70/25/2024 L2:!0
LO/2512024 t2:17
LOl25l2O2 72:L2
101251202412:L3
70/251202412:L4
7012512024 !2:L5
70125/2024 72:76
1o1251202a 72:L7
7012512024 t2:t8
701251202412:19
1012512024 L2:20
to12512024 72:27
tol25l202a L2:22
Averages:
.FC8O14
4085.214844
4082.733789
4079.877197
4082.742578
4085.380127
4082.715088
4079.316L62
4080.300781
4082.526671
4078.374572
4079.O7t777
4074.050537
4083.277588
4078.876465
4083.152832
4089.731934
4083.733398
4079.528564
4082.091553
4077.20752
4082.125732
4081.280737
.FT8O1B
78.13053894
78.35063171
78.48656464
78.15826416
78.47342682
78.54277529
78.t7281342
78.32765t98
77.8535385 1
78.3770022
78.4L857L47
78.36438757
78.23722839
78.53990173
78.26025397
78.35928345
78.48488677
78.51656342
78.57539368
78.41542816
78.09334564
78.35006s61
.At800Y
5.399730205
s.631233692
5.628125191
s.s20328999
5.631187915
5.512462L39
5.554113388
5.503156662
5.494787216
5.537257629
5.523505211
5.459412098
5.595192432
5.58749342
5.486151218
5.496081829
5.438656344
5.s26869774
5.485568523
5.448854923
5.514082432
5.528
.Ar800x
5.568758488
5.596863747
5.878125191
5.395467281
5.203001022
5.367181778
5.72188139
5.343775272
5.807688713
5.6764s6928
5.510912323
5.82t984768
5.1704254t5
5.737506865
5.3s7851982
5.512486458
5.009334564
5.521927357
5.5545875
5.676670074
5.29772677
5.563
NOx
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.007
0.008
0.008
0.008
0.008
0.008
0.008
0.008
0.007
0.008 RUN 12
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 93 of I 57 @Mostardi Platt
Project No. M244206B
Boiler #1 Stack and Boiler #2 Stack
Appendix F - Field Data Sheets
Page 94 of 157 @Mostardi Platt
Cllent:C'annss lhtoz,r,tc rc*t.Pltot Tube Cp:o.t31o
Faclllty:6qdex, 2k n*Probe Length (Feet):L,O
Test Locatlon:Bol.ta. + \ Sterrr-Probe Llner Materlal:9+<rl
ProJecl #:Cnz,*rrt-oc.Sample Plane:l-3* or Vert.
Tect Method(e):2 (ct\)Port Length ("):6oo
Teat Engineer:4tc-Port Dlameter ("):{.e
Test Technlcian:Oor Port Type:fl.r.1q
Upotrcam Dlameteru:E Duct Shape:@. or Rect.
)ownstream Diameters:Lf.r Diameter (Feet!:3.rs
# of Portc Sampled:Z Length (Feet):
# of Polnts per Port:J Wldth (Feet):
Source Condltlon://otr>r1q Duct Area (Sq. Feet):8:t t
Diluent Model/SN:U4l Toct Minutca per Polnt:
it I Gas lD/concentratlon:/xcoz %o2 TotalTravenre Polnte:It
r Gee lD/concentratlon:lxcOz %Oz
Test Length (tlln.):
tlobture Belance lD:|..v*Train Type:
Mctsr !D:Urt SZ
Pitot lD:6ool
Fllter lD:
Fllter Pre-Welght (g):
Nozzle Dlameter (,,):
Mebr Cal Factor (Y):
Mr ar Orlflce Settlng (DH):
Nozzle Klt lD:
lndlvldualNozzle tD:
Prc Pitot Leak Check:@ 'HzO @ "HzO @ "HzO
tost Pltot Leak Check:(D 'HzO @ 'H2O @ 'HzO
re Nozzle Leak Check:@ 'Hg @ "Hg @ "Hg
F st Nozzle Leak Check:@ "Hg @ "Hg @ 'Hg
Br ometric Pro8su re,',Hg :
Static Prs$ure, "H2O:
COz o/":
Oz%:
lsoklnetic Samptlng Cover Sheet
R#R#R#
Sampling Cover Sheet Rev. 3.2
Page 95 of 1 57
1t,U2021
@Mostardi PlattProject No. M2442068
Boiler #1 Stack and Boiler #2 Stack
'cd l-ocdon:
Condfron:
'ad Englnst:
Tet
iahod2Fluerr
Numban
Volumctrlc Florr Rrtc Dctcrmtnaflon Flcld Dltr ghcath
TctNumba:
SailTlmc:
EndTlme:
TcrtTcclr:ffi,{ffij+-f tsffitiffitrffi*+-
.4{ x COr* + .3!l x Org6 + .20 x }tl6. _ (trtd)
(-tdx 1€rm)+(i8x_Bun)r_(Mr)
E6'4ex cp"ffi
-JaF
-
-tt/rrc(vr)-Vlx-FltlAlrxt0=
r,{h
.Ct7x rdlnr h =rdln x60 -_ acilt
Rrv, i..!
Page 96 of 1 57Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
ilis:f, Por'lff ';*h'P,it*ffir-s'ffifu g,;5"sidc-:IL'Hro S!! F grrarrlrrnr; d.E pre e,.l rn*rlrp'Tfqa,-{ ffi-E #;H* ,*,#k*
-
hm
twtztz
@Mostardi Platt
.A.Jrrral.r.t
(nz|4-q2Cr-
-
'cd tocdlon:
CondlUon:,bracal
Englnca:
.ul4 x COz% + .Sil x 0196 + .29 x }tg6, _ (lt d)
( }ld r_l&rr) + (ig x_hrn) r_(Mr)
tLlhod 2 Pfrot Sr.t Ra. l:3
Page 97 of 1 57Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Numbcr:
VolumoElc Flow Rde lhbrmlnltion Flctd Date ghcgtDde: /c>/zt /zL,
Tert Numbcr:
S:tttTIme:
EnrlTIme:
TedTectr:
1:zf,
?:qr
ecm
.F=
.Ot7x rdhr P!
TroR-o-rcfirx00._ !&{h
1twNZ|
@Mostardi Pl-att
ttlrcc(vr)
L.S<vn^r \
'ctLstbn:
Itdlod2Ph8r.i
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
/oht bv2
-
/a:oc
Number:ft\2.l.rzoq-
volumcfrlc Frow Retr Dctemrndon Fhrd h ghrd
Ddc
0oaraqs s ,a,l ^.*- ,*d. - f ac- Taat Number:
Conrlltbn:
Erglnccr *zt
Sf H1gT-gI Upcrrcom rxsturb.nor, Dtammn I .
.4{ x COr96 + .32 x Oa% + 28 x tt96 r _ ([tt)
( Md x ifrm) + (tg x_&rc)._(Mt)
ffeffiiq*H${o.zu +rp or* Tif,E# ffi,^ffi #jH*' ffi*FlffiB
$artTlmc:
Erd TIme:
TcrtTrch:
E5'4ex cP'ffi-.F-
-W
x-FlnArr x !0-- .cfrn
'c{7x rdln.#he-rcfitrx6oc_ rdtr
Rrv. 1r3
Page 98 of 1 57
1my&a
@Mostardi Platt
b*t
ttlecc(vr)
Numbr
Volumr8lc Flow Rab Dctrrmindon Flctd D.ta gheetoz\\+z("D6:h /ztlzq
-
Coaa( gs a'rtrr,.a. ,*,J"r, ir,a TcdNumbq: s
.44 x COe96 + .&l x Or* + 2g r ltt6 ._ gtq)
lld x _ 1€rm) + (tg x_Bm) a_ 1g.;
7'o{7x- efi'#. =- rd}nxoot- tdrr
fle0rdl2PU8b.t Rry. 1:3
Page 99 of t 57Project No. M2442OOB
Boiler #1 Stack and Boiler #2 Stack
1rutnw2
OMostardi Platl
Number
'crtl-ocdon:
Condltbn:
Englrmn *Tu
\/r r_RoAna x d) r
tftthod2 Ftor6[r.r
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
.44 x COa* + .92 r Ort6 + 2g x Nrj6. _ (!td)
l*ld r _t€nt) + (16 x_Bm) . _ (Mr)
E6'4ex cp-ffi-.ou.-
Volumofrlc Ftow Reb htrmlnaflon Fleld Dfi ghe.tAV)q?sN Da0rl r,lzrlz.r
-[.1oiter{t <.\q'. StrilTlms:*-, EndTlme:
-
TcdTch:
t7.Ort7x rdtrr r#k._rdtnx80,_dh
Rov. 1'.t
Page 100 of 157
t2rtxE2
@Mostardi Pl.att
Qo,
ttlroo(vr)
Number
'crt Locetlon:f\itcr.ct Sf,q^,L
Cordltbn:4"br,ac,t
Englrrcc *22-
.{4 x COr* + .32 x 0:96 + 2g x Na% . _ (itd)
iE x _t€uo) + (18 x_&r) -_ (Mr)
M.hod2 Ftorsra Ran l:E
Page '10'l of 157Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Ddr: k>/zz lztl
ToetNumbcr:
-
StadTlmc:
End Ilme:
TestTech:
I ltot
ao'4ex-cP-ffi-.F:
-w
x-FltaAlta x oo u_ dn
.*l x tdtn, h
T16..-rdlnx60._ dh
1rutt&zl
@Mostardi Platt
tilrc(vr)
Number
Locdion:
CordUon:
Englrpcc
.4{ x COr96 + .32 xoe95 + -2E r }egt r _ fltd)( ild x l-Bwr) + (18 x_Bn) =_(itr)
7.el7x adh* fu .Trt
ll.Urql2PUSra Rov. 1:3
Page 102 of '157Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Ddr: pl ZZlz.tTcdNumbcn
-
ShrtTlmc:
EndTlmc:
TcrtT*tr:
86.40x-cP"m-.rrF-
-Vr
x-FltrAne x E0 = rnftn
_Vrco(ve)
ilafM,
@Mostardi Platt
vorumctrrc Frow Reb Dctormrnrton Frcrd Drtr gh.'tHNumbcc .{hzqqz6(. Ddc: blzrlz.l'" ('/wr*:s, rr-taaas l3&n tng TrdNumbcr:
-
locdm: Ir^* tcr- { t <{<, , stett Tlmt: l r. ee-r,\t'Err1t \ Srcrrr' tIgI lmt: ll,Sf
-
condltlon: ,/.br.uzt EttdTlme; n.ttErElnen flzz
-
Trtrch:bm
&,lctDhnrbr 3')i ft rrd---NJ.-r---- -.@.rffi&t# Hm'DLturtancc'txarPon - 7
ffi.ffi
.44 x COr96 + .32 x Oe% + 28 r Nzg6, _ (ltd)
( l,ld x _t-Bra) + (ig x_Bun) ._ ([fi)
a6'4ex cp-ffi-.a- -
-tvrcc(Vr)
Wx-FltnArc x!0'_ lc*n
17'&}7 x t*'# t- rcfinxoor- .dtr
tLhod2 Fioter..t
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rar. 1..9
Page I 03 of 1 57
1f26tilrz2
@Mostardi Platt
Numbq:
Lstbn:
Cordltlon:
Erplnccr
lf.hod2PEE[rd
Project No M2442068
Boiler #1 Stack and Boiler #2 Stack
Volumctfc Flw Rrb Detcrmlne0on Flold Dltr ghocth 2urtzot
( txlar< r)rcnrs ..ndr.-, i-1hitc,r t+ I 3$.crr
Ja,.rtral
Atz-
Ddr:
TrdNumbcr:
StrrtTlmc:
End nme:
TotTrh:
lolz> l*t
a
12:tL
17:l
b,u
.41 xCOrtt +,3a x Or* + .29 r Nz%, _ (Md)
( itrd x _l€rrr) + (1g x_Brn) ._ (Mr)
a5'4ex cP-m-,.F -
-fi/noc(vr)-Vr
x_FltlArtl x !0 r_ racn
.G{7 x rcfin r h ._rdln x60._ rott
Flv. l:3
Page 104 of 157
t4tma
OMostardi Platt
Volumc&lc Flmr Rate Do0ermlnr0on Fietd Detr ghot
Numbsr:rX 2\rrZor_Hc to lz tt z*TrdNumbcr:
-
.et locdion:
Gondltbn:
Englnccn
tl&od2PluBh.a
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
CoorO,rU n t-r-,. ,^..Cik. l^q
Bor'rOr rl I Sr,<ctC
.\t)l.r*l
AZe-
l2t ?'l
,2.'s7
lt4ttea
OMostardi Plaft
StailTlmc:
EndTIme:
TcrtTch:
.4t x COrl6 + .3il x Oal6 + 2E r &t6 . _ (Md)
(- Md x _l.&na) + (.lg x_Brn) . _ (Mr)
E5'4ex cP-ffi
-.6F
-
-tvrao(vr)-vax-FltrArtx60a_
rrrr
.C{7x edh, P!
Te6. =- rdlnx60r- rdh
Rlv. 1:3
Page 1 05 of 1 57
ctLocatim:
Conrllthn:
Enghrr:*r-r-;
lldlrd 2 PIoaSh.r
Project No. M2442OGB
Boiler #1 Stack and Boiler #2 Stack
fnz*q:,o'-c*a.r^*GI.
Boile- rf t S,r,*..,,.-
4Ior*.ar,
Numban
Volume0ic Flow Rete Drtemlna0m Fleld Drtr EheotDdr
Tcrt Nunbcr:
$artTlmc:
EndTlme:
TotTccfi:
tolzrlej
lo
17tt{l):79
?gr.9
.44 x COrS + .32 x 0196 + .29 x &t6 . _ ffi)( tld x _t8m) + (i8 x_Bm) , _ (Mr)
Ec'4ex cP-ffi
-.F
=
-_ft,/.ca(vr)
-lbx-FItrAIExfi)a--
lclln
l7'cl7 x ertn ,#h .- rc{tn x6o =- rdh
Rrv. 1:3
Page 1 06 of 1 57
taiwz,
OMostardi Platt
Volunctlc Flow Ratc Dctrrmlneflon Flclrt Ddr ghtcttl?\l4zc4,. Ddc ,.t,,-' . a zGe,L uMl b/ZltZtl
Jor,rrfflr ntrlert-rc otntoi tn" T0ftNUmbcr: l,-l2or't<.rr4l Sf,<cra SlfrtTlmo:
-
' r<rr+ | s,t{.ala uElI ltma; )": lC4%, EndTtme:
-
'.]tEEln on Aza- rdr; A
.44rCOr96+.SilxOrg6+28x1t96._ (Md)
I Md x _ iguo) + (i8 x_Brm) __ (Mc)
66'4ex cP"ffi
-.F
-
-ft/rco(vr)-
\b x
-
Fluc Anr x d) '-- rcfn
7.47 x rroiln l<#t- ._rc0rr x60 r_ sfi
Number
rd Locdon:
Gondl0on:
iffi2PUBrra
Proiect No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rer. l:t
Page'107 of '157
tatttYu2
@Mostardi Platt
,Lb.atl
Volumohlc Flow Ralo Drtrrminrffon Fhld Drtr gh.GtNumber:t4atq?a-
Ctrxih:J frtncrAf Ctale.fr taglocdon:Brer rr t Srlcx-
@ndHon:
Ddr
TcCNwnbor:
ShrtTlmc:
End Tlrnc:
TertTct:
l,lz, lzl{
ILt7;)Alot4\'ct Englnor:*;*
tLhod2Prdh
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
l*rt
bn
.*t x Ge't + .32 x Or* + 2E x i&'6 r _ ffi)(- t d x _t-Bun) + (lg x_Bn)._(M.)
86'4ex cP-ffi--ffi-
\6x-FlnAlrx!0r_ ec6n
.C{7x rdh * Pr
Te n- '- rdrn x 00 . - rcftr
Ran 1:0
Page 108 of 157
1tlrtM|
OMostardi Platt
Itlrcc(vr)
Projsc{ tlarnc/Number
Tert
To3t
z44zo Data:
MobrAH
Mollturs Oila SlrcetProject No. M2442068
ID:
NONJSOKINENC MOISTURE FIELD DATA SHEET
t o/ts le4
fsnp.rdJro:-!3of (f-nrrt"tod -r*O*l
scare lD Number Lv 4
Scate Catibratlon Cnear oau:_Lo/ zt l e
Scale Cellbratlor Chcck (scc OS€.06C for orooathre)
250grams ?EO
500granrs 60
lUPl[tlGER wasHTtntfld Finai--
lmpingelt: 716.0 I 1?L.L 1
tmpingorz: -?t{'9 I 't(8.1 1
lmprnger3 )78.'l I ?jt.O I1r .T
lmphger4: *-zo t 0!5.1 I
Iryrg(B')--ff:;:TET-r$r*.3.3__frro*ucu,oa_.,1l rao"rt
HfiHBltr5ffittr ron.,
lmoinocr 1: t t
lmplnger2: _l _l
lmohoer 3: t t
lmoinoer 4: t r
Awrtt lr6r7rnpcrnrn:bt thtdtdotwilqfue)
Boiler #1 Stack and Boiler #2 Stack
eaFtot$t rsz @Mostardi Pldl0EO23
Projec-t |.lerneNumber:
Tcst
Tc!t
Mehr
Mobtu6 Dsti SlEt
Project No. M2442068
NOTSISOKINENC MOISruRE FIELD OATA SHEET
Q4c S 3 agdca i nc orzuqnog o*a;tolzt c4
YEH-{
Rev. 1.5
Page 'l 1 0 of '157
T.nu,ra,n'__EO!___trr-, u4lr-t oul
scal6 lD Number tJ' rt
Scale Cetibrstbn Check Dae: I c./4/r{
ScsL CallbrClfi Ch.d( (.e. OS6.OECfUpirardnc)
250grame Z*)
5@gnntz *
7il}srarrrs 15O
#EBlufiHttr rotar
lmolnoer 1: t t
lmginocr 2; t t
lmpinoor 3: t t
lmpinger4:_/ _l
AwrurirltrTabhhnndotMt
-'sruE rru tn t_ga:*_-ln. Flgfsnpaetru ?! tp*nU.c,oo_jZ _f"*o"r")
ilotorVdume
(Vin)ItllsL
(Clrdc Ono)
lmolner 1: t t
lmpinger2: _l _l
lmpingor3:_t_t
lmolnoer 4: t _r
Boiler #1 Stack and Boiler #2 Stack
@Mostardi A&l1v823
lsokinetic Sampling Cover Sheet
Client:C'Orn?cl 5 tn,nerut< tt-)Pltot Tube Cp:o E{oFaclllty:(hJc*., Tlaal Probe Length (Feet):t-<S
Test Location:*lter lZ S+<ao Probe Liner Material:
Project #:fi)z+4zoc Sample Plane:l@. or Vert.
Test Method(r):Z Ces+*l Poft Length (,,):C.@
Tect Englneer:A zrz Port Dlamcter (,,):*o.,
Test Technlclan:LB Port Type:F1*to
Upstream Dlameters:q Duc{ Shape:@. or Recr.
)ownstream Diameters:(,{.t Diameter (Feeg:553
# of Ports Sampled:Z Length (Feot):
# of Polnts per port:6 Wldth (Feet):
Source Condltion:x)ot^,- I Duct ArEa (Sq. Feet):9zI
Dlluent Modet/SN:I AT too Minutes per Point:
i,I Gas lD/concentraUon:lxCOz %Oa Total Traverse Polnts:l6
lxcoz %Oz
TeBt Length (iiin.):sa:r tlrrconcenuauon
illoirsture Balance lD:L./ I Train Type:
R#R#R#
Meter !D:Cnnf:
Pltot lD:b%l
Fllter lD:
Fifter Prs-Welght (g):
Nozzte Diameter (,,):
lleter Cal Factor (y):
er Orlfice Setting (DH):
Nozzle Kit lD:
lndivldual Nozzle tD:
Pre Pltot Leak Check:@ 'HzO @ 'HzO @ "HzO
,ost Pitot Leak Check:@ "HzO @ "HzO @ "HzO
re Nozzle Leak Check:@ "Hg @ 'Hg @ 'Hg
P st Nozle Leak Check:@ 'Hg "Hg@ @ 'Hg
D.rmetrlc Pressu t€,,,H9 :
Statlc Preasure,',HzO:
COz %:
Ozoh:
Rev. 3.2
Page 'l 11 of 157
1t,U2021
OMostardi Platt
itack
Project No. M2442068
Boiler #1 Stack and Boiler #2
Number:
est Location:
Conditlon:
Vs x_Flue Area x g0
vorumetrrc Frow Rate .lctermrnation Frerd Data sheet
:q?.|q' Date: prtsk,4
Engineer:Ar.t
9,lr.1Plamet€.J13-r Upeheam Disturbance, Diamctcrs Irnlo Arca-*&Lt--ft2 DtrurQrra.a Fricn.a---^ -,l#ffi-ffit^ff '.&'tffi m'ry&**rffistdici,'jls 'H2o ?"* @ ory eurb r;; - pre_6,__rncr,$ Hao!b$g-"Hg r*r% Fo B- a li.f, Etaar c r--r-- , r r
Test Number:
Sbrt Time;
End Time:
Test Tech:
1oo
-7'. a>-
Q,g
fJity-*r* ff"h-ffis fi[*"*ffio ["tHrD i'd';;[o
*4 x QOzo/o + .32 x Oz% + .29 x Nz% =_(Md)
(-Md r-1-Bws) + (18 x-Bwr) =_(Me)
as'4ex-cp"ffi-J^P : ft/aec(vs)
scfin x 60 =
OMostardi Platt
1t1no21
tscint iledtlilt{pfl€ft rrocrBoiler #1 Stack and Boiler #2 Stack
Paoe 112 of 157Ran. 12
scfti
Number:
Location:
Condition:
Englneer:
volumehrc Ftorv Rate lhterminaflon Fierd Data sheot{fiTrlqZo" Date: t^,assrE. lol6l ?1._
/VottYLq, I
-
Test Number:
Shrt Tinrc:
End Time:
Test Tech:ls
Leak Chec*e passed@
Prsl_lnchec FhbPost_ 'L_tncher HzO
Umbilical tD _
44 x COz% + .32 x Ozvo + .Zg x N2% =_(Md)
( Md,._1-Bwg) + (18 x_Bws) =_(Ms)
Bs.4ex-cp-ffi
-.,,m
: ft/sec (vs)
Vs x_Flue Araa x 60
7.&47 x acdn x Ps = scftn x60 o_Ecffr
Ts oR
@Mostardi Platt
1nm21!ts{ffiffiBr.gtstacr Paoe 'l 1 3 of '157
Hcv. 1.2
Number:
Locatlon:
Engineer:
4 x CO2oh + .32 x OzVo + .Zg x N2% -_(Md)
( Ud *-_l-Bws) + (18 x_Bws) =_(Me)
85.49 x_Cp x
Ve x_Flue Area x 60
volumetrrc Ftow Rate Determinauon Fierd Data sheet
- ht44?u. Dare: btrlzl
Test Number:
Start Time:
End Time:
Test T6ch:
8'7 I
Z
8',-t
Leak Ched<s passed@Pre 6 _lnches rhoPost-_?_lncfres HzO
Umbllical tD _
G: ft/eec (ve)
'647x acfrn,=+=- scfixoo.-*fr,rTs oR
@Mostardi Platt
1t1t2U21
Ts OR
Page 1 '14 of 1 57
Rev. 1.2
Numben
est Locauon:
Conditon:
Enginccr:ka-
Vs x-.Fhte Araa x fl) r ..!f,n
Volumctrlc Flow Rate llctcrminaflon Flcld Date ghcct_!nl4,l?.% Date: tolzs I et
9r-, ".4,,,""Test Number 3
Shrt Timo; 6-.2
End Time:
Test Tech:
44 x COz% + .32 x Q% + .29 x th% ._1gd)
( Md x--f -hr:) + (18 x_Bua) a_(Ma)
ao.4'x_cp-ffi*_./,IF _ ft/nec (ve)
7'a17 x acftn ",ft =- sctnroor- 8cfri
Page115of157
R.v. 1.2
@Mostardi Platt
1ll/a,A
,/orAq+l
Number
'egt Location:
CondiUon:
'est Englnecr:*=e
-
Volumotsic Flqr Rrb llctermlnaUon Fleld Data SheetDate: ol 6l?+TegtNumber,F
-
4lr3
-
Shrt Tirnc:
End Tlme:
Teot Tech:
I'1,:,18-:ffi#-_^._ ^ _ @;H:iffi13"ffi,"4PortLcngthlsL' p.ft size {zr, "pffiyp;;,,'ff*ffi;bLor_rnrcoetficienr (cp) o 8.16Pr '51o'l'lg cor%: $-pypI.rne
-:-
Leakched6pa$ed@st'dc-re 'r-r20 ?% : oryeuiurem; - pr. 1 _frfisr{p
4lxCOz% + .32 r Oz% + .29 r Nz% ._(Md)
( l,td r_i-Brs) + (ig x_Brw) - (Me)
8'.4ex-cp"ffi,_.ffi _ */scc(ve)
Vs x-Fluc Arae x 00 = rr{m
7.617x aoftnr+ =_ cctrnxfr)._lcfhT8 oR
Page 116of157
RcY. 1.2
OMostardi Platt
1nnm1
Qts-
iHffi*#_-i#-c,.-{^.^ffi?Hffidffif; ,&_
Number:
LocaUon:
Corditlon:
Englnecr:
x@z% + .32 x Oz% + .29 x trl2% ._(Md)
x_l-&re) + (i8 *_Bm) =_(Mr)
ShrtTirnc:
End Tlme:
Test Tech:
. --!t /sec (vc)
port Lcrpth_r,.o " portsrzr._.{o._. pffiffi?UfiHfibfll'fuifr*dmt (cp) q".roP-=6ao 'Hg co.%
-
vrhtE[i5"Tcnrp --
Leak chidc parr.dostrticr, "Ho ?%
-
DryBurbr"ri - pro a.
-rnchcsH2offi--'#' il*-Gr, it";.# *" il,,*'#;
7.&17 x rctn x P8 =scl?nr60-_scitrTg "R
No. M2442068 Page 117 ol 157
Rcv. 1.2
@Mostardi Platt
1t1lXP1
iHffiHH* ab^ Ll,_, ^8mlHffi'ffiH*fuPort Lensm tq'-" Port sEe--ts'-' piliffi:dlffifrbffi*t cie'r (cp) or?r*o
;1lt
-
vveiEEFa;t --
r-ear qd*" pa$od@
P'lS,eI-'Hg Ma.rno.g& ilXrc*EL Umbtflcat tD
4 x COz% + .t2 x e% + .26 x Nz% -_(Md)
d '--1-Bm) + (18 x_Buo) ._(Mc)
Vr x_Flue Area x 00
No. M2442068 Page I18of157
Rlv.1.2
.,EF - rtlscc (ve)
7'817x alfnr# =- actnx8o.-rcfti
@Mostardi Platt
1t1lN21lRlstCbrc stacr
Number:Inuq?"L
Volumetrlc Flw Rab llrobrmlnafron Flcld DaE ghcct
Dab:
Test Numben
Start Timc:
End Tlrne:
TestTech:
blZtz,+
1est Locetion:
Condlton:
Engincer:
lo:oO
@Mostardi Platt
1t1tt21
F,ll,H5## xmg*r?p:er-s J-
4lxCOzo/o + .& x Oz% + .2gx N2%._(Md)
( Ud '--1-Bnrs) + (18 x_Bwe) ,_(Ms)
ao.4ex cp"-GY Msx_pe
Vr x-Flue Aroa x 60 --- acltn
-6F: n/eec (vs)
.8{7 x adin * PB =actrn xfl)._E6tlTs oR
No. M2442068 Page119of157
Rav. 1.2
l,l,itfrffi-8":IeP . rmbffiffi*t (e) o a.roPu'?f,'9o-'Hs cq%:-'-"'j ffiEi6Te;r:_ Leak,pckrp$scd@statc '1o "Heo or%
-
orv aurtr;; - p.-{_rnctrcc lraoP,l&jd-'Hs MctcrnoEfu FiLrc*Ef umbltcd tD
aftfit8bl2 Stack
Bot[e,r lf 2 Sf-<urr-
Number:
eet Locauon:
Condltion:
'ed Engineer:
Volumctrlc Flry Retc llrbrmlneflon Fleld Datr Shoet! Z'lq\oc Date: lotzsle,t
TeetNumbor A
4rbttt c, t
4vo
i;;,ffiH#,* ' Hffi.Hffi#:H*f;*+
m-'*3oT*5'ffiffiffi'Ffuug
P,-zt,( "Hs rffiarN;E iiil"*@ Umurcd rD
Start Timc:
End Tlme:
Test Tech:
tn-2q
'!"'{5
x COz% + .32 x @% + .2gx Nz% -_(Md)
x.-_-1-8we) + (iB,_Bwr) a_(Mr)
7.617x acfinl<,ft =_ rctnx60._lcfir
Page 120 of 157
R€v. 1.2
OMostardi Platt
il1tn21
85'49 x-cp " ffi
-'F
----Jt /ncc (vs)
Vr x_Flue Atle x (X) o **6
c
-
l^'s
ll' ,s
igffiffi_*-' .^ffirHiiffi:ffi5*ft_Port Lcngffi r''q, -; eort scc-Jse-' r;rfi?';;frfib":rffi*%rd.r,r (ce) p8{ oP*-?'p "Hs coxl rnrstniioiemp :_ u**rd*rpss!.@statrc-.:o-"no ?y
-
gwarrorern; - prc_L__hctrcclto
P,-&te.-'He M6rcrxi@g.: Fito*Ec- Umuncat tD
Number:
Location:
Conctiilon:
Englncor:a--
( ud r_-r-Br,ve) + (i8 x_Bw) : (Mo)
volumetrrc Frow Rab .lrbrmrnrron Frerd oeta ghert%::::L Test Number:
Start Time:
End Tlrne:
Test Toch:
.6-p'- rtleec (ve)
7.@47x actnr=+ =_ scfrnxfl)=_ocfrrTs oR
@Mostardi Platt
1t12g21
Page 121 ot 157
Rcv. 1.2
Number:
Volumcblc Flw Rate DobrmlneUon Fietd Deta ghoet
LocaUon:
fiL+YZob
-
O*1{\t9 tt: ^tt>tt,*-tt^'. -e
B.itcr t " ,f,t<-L
l,Wrn^t
Date:ta lzs lz*
Tcgt Number I a
Gondltlm:
Englno.L'
Porl LangfrrJcgt_"
Pr,_Ts.v'Hg
Stdc .?o ,Hp
Slatic ,Hg
Pr ?54o '1.1g
4 xCOz% + .32 x Q% + .28 x Nz% -_(Md)
'_l-Bws) + (18 x_Bws) r_(Mr)
Vr x-FlrrArea x00=
7.017 x acilin, PS =sc,linx60._Ecfil
Ts oR
No. M2442068 Page 122 of 157
Rcv. 1.2
Start Timc;
End Tlme:
TeEt Tech:
,t.,?a
I t i.l6
es
a.'49x cp- ffi
-.,F
--ft/eec (ve)
OMostardi Platt
'lt1lNI21?ftliilblf stacr
VolumcHc Flow Ratc DebmlneUon Fleld Drta ghecttt?l Uznc Date: blr,..-1 n c+rb [JaIg: lO/g1 hOsrloqxr ril*ztts ord--,.,,rrc. TestNumbot frLocaUon:?-iVr *t *,*-t l:+t
(Z.olCondilion:
Enginocr:lzp-
"4
4 xCOz% + .32 x Oz% + .26 x Na% =_(MO
d *_1-&r!) + (19 x_Brre) =_(Me)
Number
4ttrttu- r
Ve x-Fluc Arca x EO = ..frn
7.A(I x acftn " P8 =ccfirx60-_3cil1
Ts "R
No M244206B Page 123 of 157
Rev. 1.2
Start Timc:
End Time:
Tcst Tech:
85'4ex-cp-ffi-J^P :- :t /ecc(va)
OMostardi Platt
u1ng21erRlttl$d Stack
est Location:
Condition ,Lr?a\r3l
est Engineer *to-
.M x COzo/o + .32 xOzoh + .28 x NzYo = _ (Md)
Md ^ _1-Bws) + (18 r_Bws) = _ (Ms)
85.49 x Cp-
Number:
Vsx_FlueArear60
17.647 x actm r-Ps- -
DS-001 Method 2 Pitot Shed
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Volumetric Ftow Rate Determination Fietd Data Sheet
Date;
Test Number
Start Time:
End Time:
Test Tech:
tolZStLr+
IL
lzt o?
IZ,,LZ
-
-JZP
:
e-n
Duct Diamete\)23_1 upstream Disturbance, Diameters i.rFlue Area . t9.t t ft2 Downstream Disturbance, Diameters tt.<PortLength ('<o " Portsize 3[oa 'Ponrypefrsra-pitotiolif- pitotcoefficient(cJ cl.g..toPo' z(9o "Hg 9or'r
-
' wet fiitTem;- -* Leak chegks passed@
e- tjr*n- raerer No-grq# Ft*" *-r;r- ,!ffi1,,#rnches H2o
sctrnx60=_sclh
Rev. 1.3
Page 124 of 157
1t25t?V22
OMostardi Platt
filZ*4bc
BAtcrr: &z *rr....
ft/sec (vs)
Pir*rct
Tcst
Tsst
Mebr
NOiI.|SOKINETIC iIOISTURE FIELD OATA 9HEET
Dab: lo/t-rlulourccffiy: o.trr -----ffiiiEr:'xrgauon: rrr!!l\Dattwiffi
ddrpth Motsturt Dlta sheetProject No. M2442068
rrnpc*rrr,_-&____(r,or, ^r"r,oaZ'i* or"t
Scale Calbration Check Dab:
25Ogam; ZSO
5o0 grams S@
750grams 79
ITPINOER WEIGHTtntuat --Finei- Totat
lmpingerl: l_ t_
lmpinger2:_/_/
lmpinger3: _t_t_
tmrinoer 4: t t
250 gramr _2
mrruet'flcxildr
,*.r-v_31.>e!_ h. l.lgt-p.r.l|I* -t-- F-nu"ctoo_ll r.n o*t
ItItPtNGER WETGHTtniliat -Flil
lmpingerl:_l_t
lmplnger2: _/_/
lmprngor3: _l_l
lmoinoer zt: t t
. A,tagoitoi-ffiffi:
fr, h ot,k,til.frt&,,!*,)
Boiler #1 Stack and Boiler #2 Stack
P#ll$of tsz OMostardi Pt2l\UZtEg
NON.ISOKINETIC MOISTURE FIELD DATA SHEET
o116,, lo/2s(24
ourcaCondition: i.F{rt
-Pre-GalibrauonData:
rort,TeatEngineer: eZL
ft ecsurc p5.1_{F------TlFi
T*np.rrrr", jl__rr,o, u.oooZr"rt ort )
Scale Calibration Check Date:_
Scale Calibretlon Chcct (sao OS€.OSC fur oroceduer
IMPINO R WEIGHT
b*t inlcf and.dH il
rgnpqatre: 323 (rronl,r"ooo_Froto"u)
lmpinger 1: _ /,
lmpinger2: _/_
lmpinger 3: _ /
lmpinger4: _l
IMPINGER WEIGHT
W, intet 0d ottut it aSgtaUcl
MoisturB Data Shect
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rev. 1.5
Page'126 of 157
?/1w2023
@Mostardi Platt
l
Appendix G - Calibration and Response Time Data
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 127 ol 157 @ltilostardi Platt
ou
,
=oBI
-P
g
=crd
ooo
ooo
ooo
ooo
ooo
ooo
ooo
cIcost
:t6.
!
g=
iosE
so@oI
sIT
s6oo
troEr
LNac
x!
(z
LIIc
IIIT
(z
ooNoNN
IIrtNn
{z
c(!CLoosatocooi5
sooo
i!
sl:
s33
sc
sooo
{:
t
j:
LOSE>!
!;ad
ooo
)2o
oao
f
!3
tto^iN
))j
o.:
,qNN
oEot.Eo
3!!
f:x
o?
!toNN
o
,oN
eotco
co:zo
rg
rxt
troIczoo!
af
IrY
trctrE!o
q
)c,)c
otrEoo
Eo
EI
EsI
to
I
EoI
sc
oE
E.9I
tF
!EClo.xoz
eIsNo
at,soo
o(LEoo=@
oo
o
o
oo
o
o
l!
l
r
-

L
L

l
!
FN
F
(
O
-@
@
@
N
ooqN60NO
C,,Eot
o
-
ge

i;
s,
E

S
t:,o.EoE')nG=c'6

it
o-
=
oo.
NO
F.
loocoNod)(!o-
o)oEE

o)
LO
O6=
-
.
4
6u

U
6
oE
:
A
e
Ea
9
6=
^

ts
0
9:
6
EE
H
g
=*
6
9
8
--
a
9
E
E

OO
I
l
l
o
E
E
_
-
EE
S
R
==
!
!

E
,o
,l
l
E;o
gU
,

troyoLeGo
tr
q
rO
O
9E

a,

!
H:

E
E'
'
-
E
'
E
:

:'
*
k
O

L.
r
tu
-
ogU')Nt*o)
EERp
V6Nx
=o;6z-
-t
t
oq
.!
q

o)
96
(L
(
D
ri
t
i
i
g
g
f
$
E
i
E
t
E
l
i
E
;

i
3-
#

EE
i
F
i
55

#=

E

i
i
t
t
E
sg
E
*
E
e

;
-E
!
!
!
ET
F
E
E
E

E
6oF
Client: Compass Mherals Ogden, lnc
F.cility: Ogd€n Plant
Fuel Typ€: Nalu.al Ga3
Fuel Frqtor 8710
To.t Loc.tion: E],orler *1 Slack
O.la: 10123124Op.6tor RODS
Proi@t a: M244206
02*Comction Datr
Cma = Concentration of Cal Gas C = Avsage value of t6t
Cqas = Corected sas valre of t6tCm=Awraae PE and Post Sgan
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rrh t ame Prtral Po(aal Pod 7em Co am Coas Sdn Bias SBn Drifl Zero Elias 7so Dnft
889 870 880 000 000 000 875 660 67 055 055 0m 000
2 889 880 880 000 000 000 880 548 55 055 000 000 000
3 889 880 880 000 000 000 880 665 67 o55 o00 0m 000
4 889 880 8.80 000 000 000 880 628 53 055 000 0m 000
5 889 880 880 000 000 000 880 637 64 0.55 000 0m 000
6 889 880 880 0.00 000 000 880 529 54 055 000 000 000
7
4
to 4
Run #lma Prel PostGl Pre ztro Post zero Cn Cfr Coas Sdn Bias Sen Drift Z€m Bas Zao Drift
10 97 000 -o 02 -0 01 11 02 49 ,0 05 045 009 -0 09
2 -o 02 -o 02 -0 02 50 -0 05 000 009 000
3 t1 02 -0 02 11 4 6 49 000 00s 000
4 49 -0.05 000 0.00 009
5 0 000 000 49 -0 05 000 000 000
6 11 00 4 -0 05 0 0 000
t non
oon noo
000 noo
l1 o Ilo
11 {) 0{,0 llo
000 t) 0t)ooo
Run I Run
O.te Shd Tim.End
Time
NOx
ppmvd NOx lbrhr 02 Y. (dry)co2ttr
(drv)NOx
lbrmmBtu
iioittuG,02 'A (w.t)
Flow- DSCFH
1 )7 q
ao
t 1
I 111 1 o t 1()1
7 10123124 11 55 12 ',15 62 o 817 4S 91 0m8 I 101 157
E 10123n1 12 16 t2 36 63 o a2a 49 9'l 0m9 1 tot 758
1?o 49 1 o.009 1 096 106
n 49 0m9 40 1 0s9 168
f4 4
Page '129 of 157 @Mostardi Platt
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Test Location: Boiler#1 Stack
Date:10123124
Project #: M244206
Linearity Cal/Pre I Cal
NOx opmvd
0.10
0.10
0.10
0.10
0.00
0.00
0.00
0.00
6.60
17.00
18.20
18.30
18.20
18.20
8.80
0.00
0.00
0.00
0.00
7.40
8.60
8.90
7.90
0.20
0.10
0.10
0.00
0.00
0.00
4.40
8.70
8.70
8.70
8.70
5.20
0.10
0.'t0
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Time
6:18
6:19
6"20
6:21
6'.22
6:23
6"24
6"25
6:26
6.27
6:28
6:29
6:30
6:31
6:32
6:33
6:34
6:35
6:36
6:37
6:38
6:39
6:40
6:41
6:42
6:43
6:44
6:45
6:46
6.47
6:48
6:49
6:50
6:51
6:52
6:53
6:54
02 % (drv)
17.80
17.80
17.77
'17.80
18.73
20.17
22.04
22.04
9.10
-0.05
-0.04
0.00
0.00
-0.01
5.42
11.14
11.07
11.06
11.06
1.67
0.00
0.00
1.54
20.14
20.37
12.33
10.97
10.97
10.96
5.64
0.03
0.02
0.00
-0.01
7.74
20.29
20.31
CO2 % (drvl
0.09
0.10
0.12
0.1 1
16.11
22.80
22.69
22.68
8.98
-0.09
-0.08
0.00
0.00
0.00
5.52
11.17
11.13
't1.13
11.12
1.51
0.02
0.01
0.35
2.49
0.28
10.44
11.13
11.13
11.12
5.64
0.15
0.11
0.00
-0.01
0.02
0.15
0.16
Page 1 30 of 1 57 OMostardi Platt
(!dEGoo=o
d3e

x;
8

s
B
P:
:
Il
-

o
9
9

o
P
=
=
=
olol
d3e

s
8
B
s
E
P
P

P
Il
-
o
?
9
c
r
P
=
=
=
olol
Gr
I
(
V
)

$
tf
,

(O

l'
-

@
O)

O
-
EI
S

$

s

S

$

$

s

r'

rr
)
Lt

..
.
.
?-
r
r

r

F

-
r
-
F
F

-
Fl
-
-

r
r

r

r

r

r

r
(l
,
l
o
,

O
r
N
c/
)

$
lr
)

(O

F-
El

N
(o

(
o

(
f
'

(
f
)

(
f
)

(
,

co

(f
,
'=
l

ci

o
o

o

o

o

d

ci

o
FrF

F
F
F

r
r
E9s

p
I
I

B
E
5I

I
;e
l
d

d
o

o

o

P
=
=

=
NIol
zl9s

*

I
I

R
I8

5
E
5l
*

o
e
?
".
i

P
=
=

P
ol
lOEE
x
o.t=
t
-o

2l
t
El
s

R
R
s
B
R
8I

I
"-
l

"j

",

ci

d
c,

o
ci

c
i

cj
olzl
(tEE
N
o-Np
t
-o

2l
I
El
a

B
s
s

I
P
I8

P
,,
1

.-
c
c
,
G
t
d
c
i

ci

do
olzl
d3a

s
B
B

s
E
P
P

P
li
l
-
o
?
?
c
.
i
P
=
=
=
olol
d3a

s
B
B
s
q
e
e
P
L-
l
-

o
9
?
c.
i

P
=
=

=
olol
E9u

s
I
I

R
I8

E
A
I-
l
o

o
9
9

".
i

P
=
=
P
ol
F.
|r
)o(.
)q)u)
(o(L
rE
N
os:
t
E
fl
B

8
E
B
A
e
E
8
P
d
xl

@@
c
o
@
(
o
o
o
o
o
olzl
E9s

s
I
I

R
E
I5

E
Sl
s

ci

?
9

or

P
=
=

I
(\
r
lol
6r
E
N
Eo-

El
\>
l
-
El
o
o

o

o

o

o

o

o

o
EH
e
c
?
o
q
q
o
?
:
9
9
.
:
d
xl

@c
o
@
c
o
(
o
o
o
o
o
olzl
occoto,oa6c,

-Y
tr
9=E

ti
Hd
Q
-
r
Qc
K
*
Q
:+
o
s

x(
o
ED
S
:
N
8
8S

8
P
rt
#
E
a
i
L-
^
-
(D
=
;
i
.
Y
(
E
6
E
5E

"
IJ
PooF
vosaN:l
ta)
ESRpa6Nx
>Hadz-
-
:l
t
oq
.!
q

o)
9'E
(L
m
(t
,
I
O
)

O
r
N
(O

$
rr
,

(O

l-
cl

N
(f
)

(
f
,

(
f
)

(
o

(
o

(Y
)

(f
)

(Y
)
:=
l

d
o

6

o

6

d

o

o

o
Ft
r

r
r
r

r

r
ol
o
)

o
r
N
(o

$
rr
)

(o

l*
EI
N

(f
'

(
f
'

(
f
)

(
o

(
o

(Y
,

(o

(f
)
'=
l

ci

c
i

o
d

ci

c
i

c
i

d
c;
Ft
r

r
r

F

-
-
r
-
r
o0-€(Eoo=I9
)
zl3e

x
E
8
s
E
P:

r
li
l
-
o
?
?
o
P
=
=
=
olol
9*

*;

I
E
p
p

N
p
El
-
'
o

e
..
i

=
=
e
o'
E9s

s
E
I
E
I3

s
s
Xl
=

-
ci

c
i

6i

E
5
aj

s
ol
il9s

p
B
B
B
E
5I

I
*l
-

-
o
o
o
3:

=
:
ol
C')EE
N
o.Bo
t
;z
l
^o

El

o
o

o

o
o
o

o

o

o
rX
l
r
o
@
@
@
t
r
l
r
o
o
-
1.
.

d
cc
,

d
ci

c
i

c.
i

<r
l
olzl
EE
N
G6r
t
6:
l
^o

El

o
o

o
o
o

o

o

o

o
E
=l
s

N
N

@
|r
)

(\
t

O
O

O
il
-

d
d

d
d

o

o

o

cj
olzl
EI3s

+
E
I
B
p
p

N
=
l;
l
"
i
.
c
j
9
c
.
i
5
5
P
o
,
otold9s

B
E

I
E
I
I

s
g
l-
l
*

-
cj

cj

c.
i

E
E

at
.
r
ol 0)
l
(
O

$
1r
)

(O

l-

@
O)

O
r
cl

O
O

O

O

O

O

O

-
-
r=
l

c.
j

c
.
j

c
.
j

c
.
j

cr
i

c.
j

c
.
j

c
.
j

c.
j
l_
l
r

r

r

-
r
r

F
r
r
(t
,
l
(
O

.(
t

tO

(O

N
@
O)

O
e
El
s

s:
:

s
s

s
Y?

I
:r
t
r

r
r

r

-
F
F

r
r
Fl
-
-

r
r

r

r

r

r

F
N|r
)oc\
too('to(r
zl3e

x
E
8
s
E
q
r
:
li
l
-
o
?
9
c
i
P
=
=
=
olol
or
r
E
N
Io-

El
F=
t
r=

ll

o

o

o

o

o

o

o
o
o
PX
l
t
o
@
@
@
t
r
l
-
o
o
r
d;
l
@
t
o
d
c
c
,
@
d
o
e
.
i
c
c
i
olzl
el9s

p
B
B
B
E
5
3
8
i*
1
.

o
o
o
o

I
=
=

=
OI
(D
f
x
oip
l
b=
l
E
fl
E

R
R
B

3
E
E

E

E
d,

xl
@

@
@
6
@
o
o

o

o
olzl
ocioEo)oog0,
L
c(
J=E

#
3d
9
-
s
Q
cH
*
e
!
=o
r
t
h
(
f
)
tE

$
.
:
c
N
s
8s

I
P
ii

5#

I
s
o=
t
i
,
g
o
6
E
}E

"
o.
J
#o0,F
IogCDN+0)=
33Rp
VGNx
Z6;6z-
-i
toq
.!U

o)
9o
o-

d
l
ol

c.
,

s
ro

(o

r.
-

@
o)

o
r
El
o

o
o

o

o

o

o

F
r
,=
l

rj

c.
j

c
.
j

1r
i

c.
j

c.
j

c
.
j

c
.
i

c.
j
Fr
r

F
r
F
F
Ol

cr
,

$
lf
)

@
F-

@
O)

O
r
El
!
-

ll
.

s
s

v

$

$

ro

rf
,
Lt

..
.
.
:-
t
-

-
r
-
F
r
r

r

r
Fl
-
r
r

F
F

r
r

r

F
(EE6ooo
d3s

s
I
E
I
P
q
P
Il
"
i
"
i
9
?
d
:
=
=
olol
ul3=

s
I
E
B
e
P
P
L-
l
-
-
?
9
,
r
i
=
=
=
olola3s

+
E
I
B
p
p

N:
L-
l
-
.
o
q
c
.
i
=
=
P
-
otol
e9;

x
8I

E
I5

5
Sl
+

-
ci

c
j

+
=
=

=
NIol
zl9;

x
B
B

E

I5

5
Il
*

t
d
ci
.
r

=
=

=
ol
NE
x
HE
I
ll

o
o

o

o

o

o

o

o
xN
O
)
O
)
O
T
O
T
O
O
O
il
.
*
c
i

Gi

+c
j
d
c
;
olzl
EI>lEl

o
o

o
o
o

o

o

o
dt

q
q
q

q
c
q
q
xl

@
N
@
@

$
o
o

o
olzl
zl3=

s
I
E
I
e
q
P
E'
l
-

-
e
?

d
=
=

=
d9s

x
B
I
I

E
5
5
a-
l
o

-
o
o
-r

=
=
=
ol
zl9s

p
E
8
E
E
3
s
s
ES
l

+.
"
j

cj

o
c.
i

I
I
.
c
i

v
(\
r
lol
N;E
N
Eo-

El
\>
l
-
El

o
o

o

o

o

o

o

o
;
a
\

q
q

q

q

q

q

q
o
-l

(o

F-

co

@
$
o
o

o
c6
l
zl
ot
r
N
oiE
l
;F
I
-
=l

o
o

o

o

o

o

o

o

o
eA
q
o
q
o
q
o
q
9
r
9
9
r
t
gl
.

(o

co

@
(o

o
o

c.
,

(o
oo-oooo-
Ol
@

O,

O
r
N
c.
)

$
lr
)
Fl
:
:

f
!

9!

fl

n{

$
q!
:E
r
v

s

s

s

s

s

v

v
Fr
r

r

r

r

r

r

r

r
0r
l
@

O,

O
-
N
(f
)

$
ro
CI

r
r

N
N

N

N

N

N
,=
l

1'

r
+
+
+
+.
r
.
r
Flr

r

F

r

r

-
r
r
F-
|r
)o(f)(f)q)g)oL
(JEU)
(\
l+E
3ERp
S6&x=Ha6z-
-t
tEu
9'
E
(L
d
]
c,
I
O
O
)
O
-
N
(
Y
)
$
|
r
)
El
:

:
l
l

l
l

f
l

C!

C
!

C!
:-
l
*
i
f

.t

$
s

s

s

t

s
Ft
F

-
r
r

r

r

r

r
ol
o

v
rr
)

(o

t-

@
c,

o

r
cl

O
O

O

O

O

O

O

-
-
,=
l

<r
j

r.
j

e.
j

c.
j

c.
j

6r
j

c.
j

6r
j

c.
i
Fl
r
r

r

r

r

r

r

-
F
oCcoDo,oa(Eo.
y
.
-(
J
.=
-
d>E

i;
l?
d
9
-
+
Qc
X
*
Q
!L
o
s
:
(
o
tE
$
:
N
6
8S

I
=
I
l
#

E
id
o=
x
.
Y
G
5
E
$E

"
o.
J
IooF
@u
,
ioErEi=o
rd
ooo
ooo
ooo
Iosi
:r6.
!
aoIE
so,qo$
o0
soooI
coE*ac
xIJ
z
\
ooN\'N
ooNoNN
ooN!tNn
gt!ELoosoto(,oi5
s333
a
):
sa3c
sCCC
L(s!>cE'
id
3J
)DD
E
l?f
o
ofN\
f)
:
f,\\
oEot,=o
3
3
(oo
soNN
oo!,=o
Cooo=zooN
q)odzzoOJ!
r6N\iUU
\I,T
o,Eo(1
,
oo
oo
EI
E9I
cII
tF
tECICLxo2
FIso
bgsoo
o0-o(Eoo=(o
J
oo
o
q
)
oo
o
o
)
l!

l!

l
!

l
!
\\
\
q
-@
@
(
O
N
oo
,
ONri
oNO
E,
,ot
o
-
3.
P

c
q,
t

S
E3Er:}oEDt!IE=c'=
+
d=
oo-
NO
F-r)o\t
(f)o)o)
(E(L
o)ogE

o
>t
4

I
#o

I
h
6J
A
F
d
r

a
-
$;
6
F
AE
E
g
=*
E

g
E
ee
a
j
c
c

ao
f
l
-
A
,=
,
=

o
6
!!
o
o==
E
.

E
.o
T(
E
;o
E<
,
,

trof(EL€E(J
r=
g
;
.
"
5
g
r
r
.
:
IogU)NIto)
md6c
oRp
SGfi
-
x
z6a6
z?
-
:l
t
o.
.o

iD
Yo
o-
d
]
ri
E
i
E
E
g
i
f
E
i
E
E
E
l
t
H
-
o-

ni

.!

EE
-
o
'
5
6
F
o

U,

o

o
r
O
-
.
L
gg
s
E
s
*
E
g
E
l
i
E
si
E
f
E
f
l

E
o.
J

O
6o
Cliant: Compass Mrnerals Ogden. lnc
F.cility: Ogden Plant
Fuol Typa: Natural GasF6lFlctor: 8710
DilEnt: 02 ryo
Cm=AwBge Pre and PoS Span Cgas = Corcted qas valE of test
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
T6l Location: Borlsr *2 Stack
Orlat 10117124
Op€ntq: ROOS
Prciact * M24426
C6 Cm Mn Bra!S€n Dnft Ze6 Bias Zero Drin
8C0 000 000 000 am 542 5a 000 000 000 000
m ooo 000 or 890 5Al 58 000 000 000 000
RS 5AO 5A ooo 0 rx)000 0 rx)
1il 1U o55 -o 55
I 8al 1
I 889 890
10 849 890 0
11 aa9 490 890 000 ooo oo0 890 576
1)8BC ss0 890 000 oo0 890 574 58 ooo ooo ooo ooo
Run I Run
Dlto Stsrt Tim€End
Time
NOr
ppmvd NOx lb/hr 02%ldryl co2%
(drv)
02 b.!6d
NOr
lb/mmBtu
lrloittuE,
Elws
02%
(wct)
1 1U',17 t24 740 400 58 0 760 54 a6 0 004 o1t'l 45 1 094.202
10117 121 8 0'1 a2'l 5A 0 754 a5 0 004 o 171 15 I O93 &t3
10t17/2l 422 412 58 0 755 54 a5 o ff)a o '171 45 1 092 018
10117 121 453 I '13 59 o 771 55 aa 0 004 o 159 46 1 097 5al
10117t21 914 934 0 785 aa 0 009 0 149 4a ! o92 790
10117t21 935 955 0 784 55 a8 0 004 o 169 4A I O95 124
10 0a 10.24 59 o 772 a7 0 004 o 170 46 '59'to 29 10 49 58 o757 a7 0 004 0 170 4a )92 793tD410 50 11 10 58 0 756 86 0 004 0 170 46 t os1 578
11 ?O 11 40 58 o757 B7 0 004 0 167 46 1 092 295
92
Page 135 of 157 @Mostardi Plaft
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Test Location: Boiler#2 Stack
Date: 10117124
Project #: M244206
Linearity Cal/Pre 1 Ca!
NOx ppmvd
0.00
0.00
16.80
18.30
18.30
7.60
0.00
0.00
0.00
5.30
8.90
8.90
8.90
5.20
0.00
0.00
0.10
0.00
4.10
8.70
8.90
6.00
0.00
0.00
0.00
0.00
0.00
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Time
6:48
6:49
6:50
6:51
6:52
6:53
6:54
6:55
6:56
6:57
6:58
6:59
7:00
7"01
7'.02
7"03
7"04
7:05
7:06
7"07
7:08
7:09
7:10
7
"117"12
7"13
7:14
ih
02 % (drvl
20.51
20.51
2.17
0.02
0.00
12.98
21.99
22.05
22.05
8.68
0.01
0.00
-0.01
4.90
11.07
11.05
13.68
18.63
10.68
0.15
-0.02
3.65
11"00
11.08
11.09
11.06
18.37
CO2 % (drv)
0.16
0.17
0.06
0.01
0.01
13.72
22.70
22.70
22.70
8.60
0.04
0.00
0.00
4.99
11.13
11.14
8.01
2.30
0.91
0.08
0.00
3.74
11.04
11.14
11.14
1 1.13
2.71
ihih
Page 1 36 of 1 57 @Mostardi Platt
oo-E(goo=oF-()oF.
(f)ocn(5o_
xosaN:l
to)
3ER:
YEXv=HaGz-
-
rt
t
og
.!2
-

o
9E
(L
c
o
E3g

e
=
3
5
P
g;
8

g
Ll
-

-
3
=
=

E
o
?
?

o
otola9s

n
B
E
E

I
x
s

E
x
;S
l

,r
i

,r
,

-
3
P
=
c,

o
9
o
(\
r
lOI
(,

u)
EE
x
9
N
E
o.
GNs
t

tu
t
E>
l

ro

^E
E
l
-
o
o
o
o
o
o
o
o
o
t
El
s
8
8
3
P
8
[
.
o
o

E
=r
$
(
o
.
.
,
N
N
\
:
r
(
o
.
o
@
il
*
.

ci

d
do
o

N
il
-

-c
.
j
c
i

ci

?
ct

c
t

c
t

ct
ol

ol
zl

zlPI
e

u
3

3
E
F
E
E

E

E
Fl
-

-
oi

o
i

3I

P
:

P
P
d3:

s
I
P
E
e
E
s
ii
l
*

o
g
oo

E
=
=.
c
i
olOId9s

s
E
p
I5

3
s
i*
l
o

o
?.
.
,
5

E
P

-
ol
rE
N
os:
t
E
HR

I
I

I
P
8
B
8
d
xl

N
@
@
tr
)

o
o

o

r-
olzl
lP
l

s,
o

(o

t*

co

o)

o
r
El

t
$

rt

tt

!
t

!t

1r
,

1r
)
i=
|
,
b
6
6
r
b
6
r
b
6
a
i
E3:

s
I
p
I
P
8
u
i"
-
l
s

o
9
".
i
:

I
I

o
ololel9s

s
E
p
I5

3
s
Sl
+

ci

I
o.
r

E
E

3.
ct
lot
ll
l

q,
o

(o

N
@
6)

o
r
El

t
$

$

s

$

$

ro

1o
i=
|
<
j

,b

di

6

cc
,

rb

lb

dc
i
zl3:

c
I
p
I
P
I
s
Xl
*

o
g
oo

E
=
=

ci
ololzl9s

s
5
P
I5

3
s
5l
*
.
9
.
o

E
5
P
-
ol
NE
N
oS:
I
E
HR

I
I
B
P
I
B
8
d
xl

N
@
@
ro

o
o

o
r\
olzl
lP
l

s,
o

(o

N
@
o)

o
r
El
t

$
s

t

$

$

rr
,

ro
i=
l
c
c
i

6
@
tb

6
6

ai

6
ociq,Eo)oooov-(
)
.=
-=E

6
!?
d
9
o
r
r
Qc
X
*
Q
=o
$
:
r
.
-
Eo
$
I
-
8
8S

I
I
I
;
#

E
A;
L-
^
-o=
x
.
Y
.
E
E
E
AE

"
o.
J
IooF
=(E(LE(!oo6)
E3s

e
=
P
E
P
B
s
8
S
Ll
*
;

-:

=
=

E
o
?
?
o
olol
d3r

c
P
I
n
I
B
e
li
l
-
=
E
E
s
9
?
.
"
,
olol.l9:
*

8
5

3
x
E
I
e
sl
6
=
:
=
;
?
?
o
,
NIol
E9s

s
B
3
E
I
s
s
E
r
:S
l
,
r
i
,
r
j

-
P
P

=
ci

c
i

g
d
Gr
lol
NO
r
Ex
E
E
r
.
r
E
o.
0
.
Ds
t

Er
t
-o
2
l

7'
-
l
I
EI
e
B
s
R
R
P
P
B
B
B

t
EI
s
B
P
P
p
B
B
R
;l

,.
i
,
t
i

c.
i

c;

ci

?
ai

d
c,

d
;l

,.
i
.
i

9
9
,
r
i

d
d

ci
ol

ol
zl

zlrl3r

a
P
I
x
B
B

E
Ll
-

=
E
E

s
?
I
".
,
ololel9s

I5

3
u
E
I
P
Sl
,
o

E
5
5
s
?
?

er
(\
r
lol
ox
t
oLo-

El
Fz
t
E
EI
R

8
E
?
P
8
8

R
d;
l
,
o
c
;

??
r
i
d
d
c
c
i
olzl 0,
l
r

N
(O

t
lJ
)

(O

l-

@
Et
r

r
r

r

r

r

r

r
Lt
.
!-
r
r

r

r

r

r

r

r

r
Ft

-
-
PI
e

u
3

B
E

F
E
E

E

8
i=
l
-

-
-

oi

P
P

3
P
P

P
F-
roo@('
)o)(nGo-
E3s

e
=
I
E
e
s
s
3
s
l-
l
-

-
P
=
=
E
o
?
9
o
otold9s

e
B
E
E
3
s
s
;
N
51
.
.

"i

I
P
=
o
d
?
c;
ol
(o
N
E
o*:
t
U
El
s

B
B
R
R
p
p
B
I
I
d;
l
"
i
d
c
.
i
c
;

o?
d
d
d
d
olzl
oEco)1'o,oa(Eo-
Y
c
..

I
>E

ti
Bd
P
e
.
r
s
a.
X
*
S
!
!+
o
s

hr
-
hE
$
.
:
g
r
s
8s

I
=
I
;
#

E
A;
L-
^
3o=
x
.
Y
o
6
fi

$E

"
o.
J
flooF
o!oo,tIto)
m6
6d
rR:
S6Xv=H
;6z-
-
:lt
OL
.g
l

a)
9E
o-
d
)
or
l
F
N
(
f
)
t
t
o
(
o
l
.
-
@
El
r

r
r

r

r

r

r

r
Lt
..

.
.
lr
r
r

-
r
r

F

r

r

r
Fl

-
-

F
r
F
EI
E

N
3
E
E
E

E

8
E
E
i=
l
o
,
-
o
,
o
i
:
P
P
P
P
P
(!dE(Eoo=o
fl
*

=
E
::
,
;

B
;
$*

*
E:
:

r
;
B
;
B
F.()oo)c,
)oE')
(u(L
af
l
9x

e
s
E
5
b
8

3I

9x

e
s
5
E
b
I8

s
€
5l
-

-
o,

I5

r-

ci

Q
s
;*
l
-

-
o,

I
I

r.
-

o
Q
s
ft
ol

ol
=EN
E
N
N
E
o.i
El
.

o
o
o
o
o
o

o

o
,g

El
-

o
o
o

o
o
o

o

o

o
d
E
i
l
t
\
u
?
q
:
q
c
c
o
l

d
t
t
'
r
,
o
:
(
o
o
r
o
r
c
r
r
o
*;
l

d,
r
i
-
c
j
q
c
r
i

cc
i

dd

il
*
i
-
-
o
?
c
.
i

dd
d
o
ol

ol
zl

zl
oN
E
S
x
!
Foo
is
t

{s
t
I
E
l
-
o
o
o
o
o
o
o

=
El
-
o
o
o
o
o
o
o
o
o
HE
=
3
;
;
;
3
3
I

Ef
*
;
:
3
;
R
3
s
3
3
dr
l
(
f
,

$
Lr
,

(O

I'
-

@
O)

O
r
o,
I
(
Y
)

$
rf
,

(g

l*

O
O)

O
r
N
El
c
!

9.
{

|l

tl

q!

q
!

q
!

q?

ql

El
c
!

c!

tl

s!

c!

c
!

s
!

q?

q
?

q?
:-
l

NN
N
N
N
N
N
N
N

!-
l

NN
N
N
N
N
N
N
N
(
\
I
Ft
F

r
r

-
r
r

r

r

F

F
t
r

r

r

r

r

r

r

r

r

r
Eil
l
*

3
*:
:

r
E
F
s
H
zl9U

s
5
3
u
E
I
e
;F
l
@
:
5
5
s
9
?
c
.
j
6r
lol
d3a

a
I
P
P;

B
E
B
B
l]
-

-
P
=
=

r-

?
?

I
?
olol
il3r

s
P
s
N
s
E
E
?l
l
-
=
=
=
$
?
?
.
o
olol
CJgoOI
t*o)
3ERpW6Xv=HoOz-
-
:l
t
o.o
69.
E
(L
c
o
(D
l

(o

S
rr
)

(O

F.
-

@
O)

O
r
N
El

c!

c!

q!

c!

|l

9.
t

9!

s?

c
?

q?
:=
I

N
N

N

C\
I

N
N

N

N

N

N
Ft
r

r

r

r

r

r

r

r

r

r
Ol

r
N
(e

$
rr
)

(O

F.
-

@
El
r

r
r

r

r

r

r

r
.-
r
-

r
r

r

r

r

r

r
Ft

-
-
(,cioo(,
)oo(Eol-(
)>E

d
EE
H
S
x
:+
o
$
k
r
-
EE
$
:
:
-
8
83
I

P
!
;
#

E
a,
L9
^
-
o=
x
.
Y
.
!
6
fi

$E

"
o-
J
yool-
MOSTARDI PLATT
Procedures for Method 5 and Flow Calibration
Nozzles
The nozzles are measured according to Method 5, Section 10.1
Dry Gas Meters
The test meters are calibrated according to Method 5, Section 10.3 and 16.1. and "Procedures for
Calibrating and Using Dry Gas Volume Meters as Calibration Standards" by P.R. Westlin and R.T.
Shigehara, March 10, 1978.
Analytical Balance
The accuracy of the analytical balance is checked with Class S, Stainless Steel Type 303 weights
manufactured by F. Hopken and Son, Jersey City, New Jersey.
Temperature Sensing Devices
The potentiometer and thermocouples are calibrated utilizing a NIST traceable millivolt source.
Pitot Tubes
The pitot tubes utilized during this test program are manufactured according to the specification
described and illustrated in the Code of Federal Regulations, Title 40, Part 60, Appendix A,
Methods 1 and 2. The pitot tubes comply with the alignment specifications in Method 2, Section
10.1 ; and the pitot tube assemblies are in compliance with specifications in the same section.
CN&F-002 Cal Procedures M5 & flow Rev. 2.2 111t2021
Pro.ject No M2442068
Boiler #1 Stack and Boiler #2 Stack
Page'140 of 157 @Mostardi Platt
Dry Gas Meter/Gontrol Module Calibration Diagram
Temperature Sensors
ATD-090 Dry Gas Meter Calibration
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Rev. 1.2 1t1t2021
Page 141 ot 157 @Mostardi Platt
{
o,€
\o
F
O)
a
F
oNco;
Nri.6
F
o)(oo)
F
(oog);
NO)o,6
O)oO)6
locoo,ci
F.6o,6
ao)ei
N6o,6
o ..Ss
t\lr)(.,lr)N
o-
F<
o)c{o o)co (o
9uo)>s3,6p
r cir5i
o)6 66 Nco (o6 lf)co tt6
Eu-So-atr3e89tA=dE
oO)@a O)o oo t-6 aa t\co
(oo N6 (oo tr,6 (o6 lr)6 \t6 |oa vo \tco
\i6
ELL6>s3.6E(DF>bos
oO)aa O)a co6 N6 coa t\a (oo l.-a (oo lr)6 (o6 |.)@ \t6 roa \t6 \t6 \tco
o
{D6Eu-
E F*EPE(h
N6 F-o t-o F-6 N6 t\a No (o
co N.o (o
co
(oa (oo (o
co
(oo (oa ra)a too roa
9qlss@-ob(D>>Oo
s3
(.)roo6
(r)
o
'do
o\fo
'rj
ooo)\to
oNo
o;o)
a(7)o
'd
co(o
r..-
oio)
o)
Nvo)
O)\to
'ai
rf)(.)\t
!to)
(?,
O)(?)
o;6
N\no
'd
C!
o,
cci6
F\
@('j6
l.r)o)orri
N\t\t('j
co
|oc\\t
eit\
N(\o
'd
!eEss}f,oco(! rno
N(o
c.)
c.jlf)
$rr)(.)
6\t
aoo
'rj
l.-rf)Nei\
Nlr)
C\t(.j\t
lf)oo
'rj
\+
(.j\t
lo
(f)
e,(F)
(ooo
'd
\tt\t6
r.-t,
oc\oN()
(o
orrj
la)(,
c.i()
O)o)c{NN
Nrr)or.j
\t(,
O)(o
c.l
a
o,
FN
(o
o
'd
o
orto-.-E=or,: o)cU,SO
Q)v)
oN6
..
o)o
C)EECiisd
ora,6
_)
o)o
!l)Eeecso
oN6
\t
q)o
o)EEEd E6
oO)ci
",
q)o
q)Fes,iSd
oN
F
c\
q)
0)6 .o "g)stE
'fSO
ooN
q)o
c)E€Etrso
o)a
a
t
Gd
6oo
@
(\(oa
€o)o
rt
6N
o-(N
vc\oN\t
()aoo
q)o(DI
r()
o
C!s
0)o)o(L
e
tnq.0)6' a_cSd\E(E=q)vlue(E",nxr-r!=YoGo6QOoo
(E
e(Eo
o)
c)
=o(E(,
bo
o
l9a
(Eoxoo
Q)
q)
o,lf()o,o,ci
ao
(o(o(oo
C.)r)
o
vog
U)
N:lt
I38RpS6Xv
=HaGz-
- :ltog
.!P- o)EEo_ co
:i=
t$$EppOG(D(r 'b 'b
aEl!Qc/)(r)
Stack Temperatu re Sensor Cali bntion
Temoerature lD:100770 Name:ZRP
Ambient Temperature, o F :88.1 Date:October 4. 2024
Temoerature Cali brator
Model#cLg40A Ceftification Date:Februarv 1. 2024
Serial # :526 Expiration Date:Februarv 1. 2025
Primary Sfandards Directly Traceable National lnstitute of Standards and Technology (NIST)
Reference Source Temoerature (" F)
Test Thermometer
Temoerature lo Fl Temoerature Difference %o
0 0 0.0
250 250 0.0
600 600 0.0
1200 1204 0.2
(Ref. Temp.. "F + 460) - (Test Therm. Temp.. "F + 460) r 100 <= 1.5 yo
Ref. Temp., "F + 460
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 143 of 157 OMostardi Platt
!oba
aCDa
q)o(u
0)
+'
5*
\t(oo
F
@oo
F
t\6;
o)ra,6;O)o;
rr,(r)a;
coao)6
(oao)
c;
oo)o,ci
co6O)6
F.-6O)6
(oao)6
Or'
SE
(oro N o(.)O)o \t
o-
l:<
o)C\J o o)6 (o
I tr-o)>s3,Ep
\5Q<
t\(o o)(o O)(o a(o F-(o (o(o
d tr-8".atr3P8o6>=!o
N(o (o(o N-(o o)(o O)(o O)(o O)(o a(o O)(o a(o N(o o(o 1..-(o N(o t\.(o (o(o ro(o
(o(o
Iu-o)>s3,EEo:st
N(o (o(o FT(o O)(o O)(o O)(o o,(o 6(o o)(o 00(o f.-(o a(o t.-(o tr(o F\(o (o(o tr)(o
(o(c|
EOoE tr-Pss
TEsU)
(o(o ro(o (o(o t-(o (o(o 4..-(o (o(o (o(o (o(o (o(o (o(o (o(o (o(o (o(o (o(o rf)(o \t(o l()(o
fiP>So-obo>>Oor.3o-
NNovt\
(')aN
oi(o
o)oo
'ai
oo
1..-o)
(.)o
cricr)
Nt-otri
lf,o,(oic,!
c.lIr)(o
(oo
(?)\to
'd
F-oC{
(c,6
(-)(o
Fo
v\no
'ri
\$\i.
c;o
ao)(.)
rdN
c.)\to
raj
\tF-l.-
e,(o
e!Nt\t-j(o
Nloor.j
$e<5Ess!ocoG (4
U)
tr)os
'd
()(o(t
ci
(\lrto
'aj
o)\t
NN
o)F.-\t
o.iN
N
ord
(oF-o
C\i(\I
l()F.-oN
oord
(.)v(o
6
o(f)(o
F
rooord
\t(')
O)6
o)NO)rd
rooor.j
(.)(o(.)
oio)
(f)\q(.,\to)
oNotd
o
oIi,Qc-E-O
^\ orQu.so
q)o
oN6
q)o
q)
G,Q"SctsrISo
olr)6
N
oo
o)EEE,iS6
oF-
c;
(?)
0)o
0)FSC
'I= Ed
oo)ci
v
oo
EE$Lr=SO
oc.l
lr)
Q'o
0)EEE|rso
oo
c\i
(o
o)o
C)EESIs6
oa
a
f(
(!
o_
Yoao
=o
coN6N
o-tN
ttNoN
(o
Q)a
o)
oe
t--rI)
ottt
o)(,)oo-
E
u,utoat'bP
(E=q)EoEEOAGCsQOa.goxsSrt(E=r\ aE;oALdsLOg=go
(9
bo
o)rt6O)o,ci=l*
Io(E
U)
N:+t
o)=38Rps6&xAGadz--ttood
(Ico
s€a
hg9EssEppOGG(r'b'b
AOG4(r)(,
Stack Temoerature Sensor Calibration
Temoerature lD :100769 Name:ZRP
Ambient Temperature, o F :67.3 Date :November 6, 2024
Temoerature Calibrator
Model # :cL940A Ceftification Date:February 1,2024
Serial# :526 Expiration Date:February 1, 2025
Primary Standards Directly Traceable National lnstitute of Standards and Technology (NIST)
Reference Source Temoerature (" F)
Test Thermometer
Temoerature (" Fl Te moeratu re D iffere nc e %"
0 1 0.2
250 252 0.3
600 602 0.2
1200 1206 0.4
(Ref. Temp.. "F + 460) - (Test Therm. Temp.. 'F + 460) * 100 <= t.5 yo
Ref. Temp.. "F + 460
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 145 of 157 OMostardi Platt
Pitot Tube No 6001
Type of Probe: (mark one)
S TYPE PITOT TUBE INSPECTION WORKSHEET
Date: 81112024 lnspectors Name:
Probe Length 6ft
JSC
f
l
r---1r-I-)_1
cIlln
LONGITUDINALluEE AX|S
a-stot Putt----- -'
ti,
)rl
TRAilSV€RSE
TUBE AXIS
-
ri,t.-,--t\L- + -.;J-
T:=) ETt::;-<i' .'."'
Pitot tube assembly level?
Pitot tube openings damaged?yes (explain below)
o (i1 oo)
o (<5o)
X yes
3r=
br=
o o (<100)
1 0 (S50)
1 " e=oo A= 0949 (in)
a2-
bz=
M2 M5 Ml7
x
.on",rro,*o,'f-q o -ruEt axrs J -- -i''-...-
.... .-_t ...
0..8 cM <Dr <0.95 cv 8-slot PuNt
(5/r6 ril.) (1,/E rN.)
E;re
--
I
TRANSVERSEilll-Ils ,r r lt-J1l l
I . r.l-1t_"- .1
IACE, OPENING
PUNES
NOIEI
[
1.05 q<Pr < r.so D
!no
z=Asiny=
w=Asin0=
0.017 (in.); (<0.125 in.)
0.00000 (in.), (<0.03125 in.)
Pa = 0.475 (in.), PB =0.475 (in.), D, = 0.375 (in )
Calibration required?
PIS{01 S Typ€ Pilot Tub€ lnspoction Fom
ProJect No. M2442O68
Boilsr #1 Siack and Boiler #2 Stack
yes no
Rev. 1.0
Pago 146 of 157
2t17t2020
OMostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No 6001 Date: 111412024 lnspectors Name:JSC
Type of Probe: (mark one)Probe Length.6ft
I
r-l:fl-!-------------- -,1"- -l
g
|ilr[r
'ii8{i?,i11
A-SIOT PUNE
aono,rro,no, -1--------j-IUBE^xrs \ s -
._..-.J-._-
o.4B cv <or <0.95 cM B-slDE PUNF
(3,/15 rN.) (3/8 rN.)
B
NOTT:
F os q<Pr <r.50 D
I
L A 'B
TRANSVERSE
-.
TUEIAXTSI r oi e1.- ,,t Ilr.._-]L" j
i
FACII oPEN|NG
PUNES
7
dt o::-
TRANSVERST TruBr {\rs Lra.{ B I tl ,}t---:-:--=z -t- - vih -=-..:<:-'
'
Pitot tube assembly level?
Pitot tube openings damaged?
!Yes
yes (explain below)
o (s1 oo)
o (<5")
Xno
or=
br=
1 o (sl 0o)
1 0 (<50)
1 " e=
2z=
bz=
,|
0
z=Asiny=
w=Asin6=
0.017 (in.); (<0.125 in.)
0.00000 (in.); (s0.03125 in )
0.475 (in.), D, = 0.37s (in.)oo A= 0950 (in.)Pr = 0.475 (in.), PB =
Calibration required?yes no
PlS401 S Typo Pitot Tube lnspaction Fom
Polst No M24/206B
Borbr #1 Stsck and Boiler #2 Stack
Rev. 1.0
Pags 147 of 157
2t17t2020
OMostardi Platt
M2 M5 M17
Appendix H - Calibration Gas Cylinder Data
Project No. M244206B
Boiler #1 Stack and Boiler #2 Stack
Page '148 of 157 @Mostardi Platt
CERTIFICATE OF AIYALYSIS
Grade of Product:
E03Nt99E15A03N0
cc317148
124 - Los Angeles (SAp) - CA
832023
CO,NO,NOX,BALN
Airuas
on Ai LquE€ comparry
AirT$ Spectdty Grrcs
Airgas USA LLC
rtTu S. Alameda Street
Los Angeles, CA 9oo59
Airgas.om
EPA PROTOCOL STAIYDARI)
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
2028
484027s2987-1
144.3 CF
2015 PStc
660
Jun 01.2023
Roquccted ActualConcentratlon Concentrsdon
CARBON MONOXIDE 9.OOO PPM
NITRIC OXIDE 9.OOO PPM
8.890 PPM
9.014 ppy
8.843 PPM
G1
G1
G1
+h0.7% NIST Trac€8ble
+/- 0.8% NIST Traceable
+l- 1.'lYo NIST Traceabla
05124t2023,06/012023
05124n023
o5t21r202106t01t2023
Lot lD Cyllnder No ConcentraUonNTRM 21060+37 Ce84138 9.942 PPM CARBON MONOXTDErflTROGEN +/- 0.8%
+t-o.5%
+l- 1.0o/o
+l-0.6%
Ju|23,2O27
Dec23,2022
Jun 07,2026
May 11,2024
PRM 12402 APEX132426$NOxNTRM 't80.t0107 1(AL004.113GM|S 16010107 KAL0g11$NOX
10.01 PPM NO,NITROGEN
9.95 PPM N]TRIC OXIDENITROGEN
9.95 PPM NO,dNITROGENIhc SRM, NTRlt, PRt , or RqU mt.d abovc ir onlv to to th6 OMIS us.d ln tla r...y .nd nol pert d thi
ANALYTICAL EQUIPMENT
Thenno 481-TLE 1 13?2SOS57 CO
nCLD 844 S 844M213 NO
NOIR
Chemilumins*encc
Chemfuminesconcs
May 02,2023
May 02, 2023nCLO &44 S &44M)213 NOx
Trlad Data Avallable Uposr Requect
Approved for Release
Project No
Boiler #1 Stack and Boiler #2 Stack
Page 149 of 157 Paoc I of I@MostardiPlafl
Airgas
an Air Liqurde comOany
Airgas Specialty Gases
Airgas USA LLC
rrTrr S. Alameda Street
Los Angeles, CA 9ooS9
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
Part Number: E03N199E1540707
Cylinder Number. CC437385Laboratory: 124 - Los Angeles - CA
PGVP Number: 832024
Gas Code: CO,NO,NOX,BALN
Expiration Date:
Reference Number: 48-403065002-1
Cylinder Volume: 144.0 CF
Cylinder Pressure: 2015 PSIG
Valve Outlet: 660
Certification Date. Jun 18,2024
Jun 18,2027
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certification of Geseous Calibration Standards (May 2012)" document EPA
600/R-1 2/531, using the assay procedures listed. Analytical Methodology does not require correction for enalytical 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 celibration mildure. All concentrations are on a
mole/mole basis unless otheMise noted. The results relale only lo the items tested. The report shall not be reproduced except in full without approval of lhe laboratory. Do
Triad Data Available Upon Request
Sinnafrrrc on fila
Project No. ulmPwed for Release
Boiler #1 Stack and Boiler #2 Stack
below 100 t.eUNOt USe
ANALYTICAL RESULTS
Component Protocol Total RelativeMethod Uncertainty
Actual
Concentration
Requested
Concentration
Assay
Dates
NOX 18 00 PPM 18.26 PPM G1 +l- 0.7o/o NIST Traceable 0611012024, 0611812024
CARBON MONOXIDE 18.00 PPM '18.08 PPM G1 +l- 0.5o/o NIST Traceable 0611012024
NITRIC OXIDE '18.00 PPM 18.24 PPM G1 +l- 0.7o/o NIST Traceable 0611012024,0611812024NITROGEN Balance
Type Lot lD
CALIBRATION STANDARDS
Cylinder No Concentration UncertainW ExpirationDate
+l-0.4%
+l- O.5o/o
+l- 0.60/o
+l- 0.5%
+l- 0.60/o
Jun 28,2027
Dec 22,2023
Sep 27,2025
Dec22.2023
Sep 27,2025
NTRM 20060904 CC714645 26.54 PPM CARBON MONOXIDE/NITROGENPRM 12403 APEX1324265 2O.OO PPM NITRIC OXIDUNITROGENGM|S DDCK0927202219 CC733221 19.50 ppM NtTRtC OXTDE/N|TROGENPRM 12403 APEX1324265-NOx 20.02 PPM NOx/NITROGEN
GMIS DDCKO9272O2219 CC733221.NOX 19.52 PPM NO'NITROGEN
The SRM, NTRM, PRM, or RGM noted above is only in reference to the GMIS used in the assay and not part of the analysis.
lnstrumenUMake/Model
ANALYTICAL EQUIPMENT
Analytical Principle Last Multipoint Galibration
SIEMENS 6E N1R431O CO
nCLD 844 S 844N0213 NO
nCLD 844 S 844N0213 NOx
NDIR
Chemiluminescence
Chemiluminescence
May 28,2024
May 28,2024
Mav 28,2024
Page 150 of 'l 57 OMostardi PF&ge 1 of 1
Aitgas
an Air Liquide company
Airgas Specialty Gases
Airgas USA LLC
rrTrr S. Alameda Street
[.os Angeles, CA 9oo59
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARI)
Part Number: E03N178E1540225
CylinderNumber: CC147517Laboratory: 124 - Los Angeles - CA
PGVP Number: 832023
Gas Code: CO2,O2,BALN
Reference Number: 48-402927178-1
Cylinder Volume: 152.0 CF
Cylinder Pressure: 2015 PSIG
Valve Outlet: 590
Certiflcation Date: Dec29,2023
Expiration Date: Dec 29, 2031
Certification performed in accordance with "EPA Traceability Protocol for Assay and Certificatron of Gaseous Calibratron Strandards (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 iotal 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 repoft shall not be reproduced except in full without approval of the laboratory. Do
Triad Data Available Upon Request
Sionalure on file
Project No MAF@ed for Release
Boiler #1 Stack and Boiler #2 Stack
Not Use lhrs below 100 e megapascals.
Component Requested
Concentration
ANALYTICAL RESULTS
Actual ProtocolGoncentration Method
Total Relative
Uncertaintv
Assay
Dates
CARBON DIOXIDE
OXYGEN
NITROGEN
't1.00 0/o
11.00 Yo
Balance
I 1 .'13 0/o
11.06 Yo
G,I
G1
+l- 0.60/o NIST Traceable
+l- 'l.Oo/o NIST Traceable
12t29t2023
12t29t2023
CALIBRATION STANDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM
NTRM
0801061 I
98051 1 1 3
K005428
SG916301OBAL
13.94 O/O CARBON DIOXIDUNITROGEN
9.507 O/O OXYGEN/N ITROGEN
+l- 0.60/o
+l- 0.7o/o
Jan 30,2024
Mar 22,2030
ANALYTICAL EQUIPMENTlnstrumenUMake/Model Analytical Principle Last Multipoint Calibration
SIEMENS 6E CO2
SIEMENS OXYMAT 6
NDIR
PARAMAGNETIC
Dec22.2023
Dec 01. 2023
Page 151 of 157 OMostardi PFlge I of I
Aitga$.
illfftlffimtrflffill
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
CcrtifrcStim podorrcd h accordam with'EPA
Date: Mav 24. 2031
Protocol br A$.y and Cortific€tion
Airgac Spectdty Gases
Airgas USA LI.C
rtTtt S. Alameda Street
l,rx Angeles, CA 9oo59
Airgas.corn
Stendards (Mey 2012)'documnt EPA
Grade of Product:
E03N156E15A1055
cc189827
124 - Los Angeles (SAP)- CA
832023
CO2,02,BALN
CERTIFICATE OF ANATYSIS
EPA PROTOCOL STANDARI)
Reference Number: 484027 50152-1
Cylinder Volume: 162.0 CF
CyliMer Pressure: 2015 PSIG
Valve Outlet: 590
Certification Date: May 24,2023
OOOnf-tZglf, u,eing lhe assay procedurer lbted. Anatyilc€l Mothodology docs rol rcquire cotredion for onrMical intBtfet8nco. This cylinder has a total.analylical
uncgrtctnty as stated belot mth i tmlidcrrco levcl ot $5*. There are rc tigntlkrnt impurilies whhh allect th€ uto of thb crllbratioo mixturo. All conccfltratbnE atB on a
mole/mole'bagls unb.s othe(wbe notod. The rilldlr rclsts only lo tha item! lastod. Tho roport shall nol b€ reproduced oxcqpl tn fll wihout appro\ral ot tho l6bo.atory. Do
Trlad Data Avallable Upon Requeet
OMostardi Platt
Pagc I of 1
l',lot Us€ Thi6 b€low 100 p6rg, r,e. 0./ m€g8pt$a18.
.1U{r6 I ITI()AI - RES.UI]TT-
3equested Actual Protocol Total RehtiveConcentratlon Concentration Method Uncertainty
Arsay
DatesGomponent
C'fi,BON DIOXIDE
OXYGEN
NITROGEN
22.69%
22.04 o/o
+l- O.7o/" NIST Traceable
+l- o.7o/" NIST Traceable
22.OOo
22.OO olo
Balanca
G1
G1
05t24n023
o5t24t2023
CALIBRATION STAIYDAR.DS
Type Loi lD Cylinder No Concentratlon Oncertalnry ExPiratlon Date
NTRM
12061520
08010226
'l 9.87 o,'o CARBON DiOXID9NITROGEN
23.20'fo OXYGEI'I/NITROGEN
+/- 0.6%
+l.O.ZYo
NTRM cc3g777
K016648
Ju\ 11, 2024
Jun 01, 2024
lnstrumanUliake/Model
--
SIEMENS 6€ CO2
SIEMENS OXYMAT 6
Analytlcal Prlnclple
-
NDIR
PARAMAGNETIC
A}IALYTICAL EQIII PMENT
[ast MultlPolnt Callbratlon_ -
-
Apr26,2023
May22,2023
of 157
Appendix l- NOz to NO Converter Efficiency Test
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 1 53 of 1 57 @Mostardi Platt
NO2 to NO Converter Test
Client: Compass Mlnerals Ogden, lnc.
Facility: Ogden Plant
Test Location: Boiler#1 Stack
Date: 1012212024
Project #: M244206
Pre-Calibration Test
Conv. Temp: 326.3 oC
Test Type NO2 DirectMax: 49 0 ppm
Conversion: 97.30 Yo
Requirement: 90.00 %
Post-Calibration
Time
12 58
12.59
1 3:00
13:01
13 02
13:03
13:04
13:05
13:06
!o,
000
660
17.70
18 10
18 30
18 20
13 40
880
000
Cal Flao
z
h
m
Time
13 25
13 26
13 27
13 28
'13:29
'13:30
13:3'l
13 32
No.
47.9
48.8
49.0
48.8
487
48.9
48.6
447
Time
13.40
13.41
13.42
13:43
13.44
'13:45
'13:46
13 47
13:48
Cal Flaq
Max
mid 0.05%
!o.
0.0
6.9
8.8
8.9
5.1
0.0
00
00
0.0
PRE.CAL RESULT
zero 0.00%mid -0.49o/ohigh O.22o/o
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
TvDe RM Analyzer Make/Model RM Analvzer s/n Analvzer Soan RM Gas Soan
NOx DDmvd 700 LX Series CLD Nox 2405059 20 't8.26
Type Sefting Cylinder lD Cylinder Value Analyzer Response Difference, % of Spar trxPrrauon
Date
NOx ppmvd
Zaro Zero Nitrooen 0 o.00 0.00%N/A
Mid cc317148 8.89 6.80 o.490/o 611t2026
Hioh cc437385 14.26 1 E.30 -O.22o/o 6t1412027
NO2 ppmvd CEG cc510742 50 35 6nt2025
Page 154 of 157 @Mostardi Platt
NO2 to NO Converter Test
Client: Compass Minerals Ogden, lnc.
Facility: Ogden Plant
Test Location: Boiler #2 Stack
Oate: 1012412024
Project#: M2442Oa
Pre-Calibration Test
Conv. Temp: 315 3 oC
Test Type NO2 DirectMax: 49.0 ppm
Conversion; 97.30 o/o
Requirement: 90.00 %
Post-Calibration
Time
12.58
12:59
13:00
13:01
13 02
13:03
'13:04
13:05
1 3:06
!o.
000
9.70
17.40
18.20
1 8.30
'18.30
11.50
8.90
000
Cal Flao
z
h
m
Time
13:25
13.26
13 27
13 28
13:29
13:30
13:31
13.32
!o.
48.5
48.8
49.0
48.9
48.7
48.2
48.0
48.0
Time
13:40
13.41
13 42
't 3:43
13.44
13:45
'13:46
13 47
13:48
!o.
0.0
4.1
8.9
8.9
2.2
00
0.0
00
0.0
Cal Flao
trlax
PRE-CAL RESULT
zefo 0.00o/o
mid 0.05%high 0.22o/o
Project No. M2442068
Boiler #1 Slack and Boiler #2 Stack
POST.CAL RESULT
zeto 0.00%
mid 0.05%
TvDe RM Analvzer Make/Model FaM Analvzer srn Analvzer Soan RM Gas Soan
NOx oomvd 700 LX Series CLD Nox 2405059 20 18.26
Type Setting Cylinder lD Cylinder Value Analyzer Response Difference, % of Span ErPtralton
Date
NOx ppmvd
Zeto Zero Nrtrooen 0 0.00 0.000/o N/A
Mid cc317144 8.89 E.90 -0.050/o 6t1t2026
Hioh cc437385 14.26 1A 3rl -o.224/o 6114t2027
NO2 ppmvd CEG cc510742 50 35 6nt2025
Page 155 of 1 57 @Mostardi Platt
Airgas
an Air Liquide company
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial toop Road
Tooelc, LIT 84o74
Airgas.com
CERTIFICATE OF AI\ALYSIS
Grade of Product: EPA PROTOCOL STAIYDARI)
Part Number:E024t99E15W0021 Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
1 53-402449685-1
146.0 CF
2015 PS|G
660
Jun 07,2022
Cylinder Number: CC510742
Laboratory:
PGVP Number:
Gas Code:
124 - Tooele (SAP) - UT
872022
NO2,BALA
Expiration Date: Jun 07, 2025
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 20 12)" 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 g5o/0. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This below '100 psiq, i.e 0.7
Triad Data Available Upon Request
Sionafrrre on fila
Project No. MiltPp@/ed for Release
Boiler #1 Stack and Boiler #2 Stack
ANALYTICAL RESULTS
Protocol Total RelativeMethod Uncertainty
NITROGEN DIOXIDE 50.00 PPM 50.35 PPM G'l +l-2.Oo/o N|STTraceable 0513112022,0610712022AIR Balance
CALIBRATION STANDARDS
Lot lD Cylinder No Concentration Uncertainty Expiration Date
GM|S 15340020205
PRM 12397
EBO13OO59 60.0SPPMNITROGENDIOXIDE/NITROGEND887665 74.2PPM NITROGEN DIOXIDUAIR
1.4o/o
1.3o/o
Apr 30,2024
Feb 02,2022
The SRM, NTRM, PRM, or RGM noted above is only in reference to the GMIS used in the assay and not part of the analysis.
ANALYTICAL EQUIPMENT
Analytical Principle Last Multipoint Calibration
MKS FT|R NO2 018143349 FTIR May 27,2022
Page 1 56 of 1 57 OMostardi PFlge I of I
I
i
I
I
I
I
END OF THE REPORT
Project No. M2442068
Boiler #1 Stack and Boiler #2 Stack
Page 1 57 of 1 57 @Mostardi Platt
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name Compass Minerals Corporation
Company Contact:Demise Hubbard
Contact Phone No.801-732-3312
Stack Designation:Boiler 1
Test & Review Dates
Test Date:10/23/2024
Review Date: 7/9/2025
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.2000 0.009
lbs./hr.
ppm 9.0 6.434
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
39.25 8.402 0.9870 1.862 0.84 25.82 0.7 25.871471
Contractor Information
Contact:Richard Sollars
Contracting Company: Mostardi Platt
Address: 888 Industrial Drive, Elmhurst IL 60126
Phone No.: 630-993-2100
Project No.:
8710

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
Lignite
Natural
Propane
Butane
10100
COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Wet CEM
Correct For O2
CO2 Interference w/CO
Yes
Yes
Yes
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 1
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
10/23/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 10/23/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 9:25 9:46 1 9:25 9:46 8.9
2 9:46 10:07 2 9:46 10:07 8.9
3 10:07 10:28 3 10:07 10:28 8.0
4 10:40 11:01 4 10:40 11:01 9.1
5 11:01 11:22 5 11:01 11:22 9.1
6 11:22 11:43 6 11:22 11:43 8.9
7 11:55 12:16 7 11:55 12:16 9.1
8 12:16 12:37 8 12:16 12:37 9.1
9 12:37 12:58 9 12:37 12:58 9.1
10 13:15 13:36 10 13:15 13:36 9.2
11 13:36 13:57 11 13:36 13:57 9.2
12 13:57 14:18 12 13:57 14:18 9.2
13 13
14 14
15 15
16 16
Average = Average =
Sd Standard Deviation = Sd Standard Deviation = Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = Confidence Coefficient = Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy = RA RA RA - Relative Accuracy =
n = 0 0 0 n = 0 or RA of 1%
t0.975 = t0.975 =
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;0
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
13.2 Relative accuracy Performance Specification. The RA of the CEMSS must be not greater than 20 percent when RM is used in the denominator of Eq. 2-6
(average emissions during test are greater than 50 percent of the emission standard)or 10 percent when the applicable emission standard is used in the
denominator of Eq. 2-6 (average emissions during test are less than 50 percent of the emission standard).
Up dated January 17, 2006
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
13.2 CEMS Relative Accuracy Perfromance Specification.
The RA of the CEMS must be no grater than 20 percent of the mean value of the reference method (RM) data. 1 percent O2 or CO2.
The results are also acceptable if the absolute value of the difference between the mean RM value and the mean CEMS value is less than or equal to 1.0 percent O2 (or CO2).
Up dated September 14, 2016
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Division of Air Quality
Relative Accuracy Test Audit of
Compass Minerals Corporation
Boiler 1
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:9.00 0.2
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
10/23/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 9/30/2014 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 9:25 9:46 6.7 6.003 0.009 0.008 0.86 1 9:25 9:46 Y 4.9 5.017 -0.072
2 9:46 10:07 6.6 5.852 0.009 0.008 0.85 2 9:46 10:07 Y 5.0 5.015 -0.017
3 10:07 10:28 6.7 5.971 0.009 0.008 0.87 3 10:07 10:28 Y 4.9 4.971 -0.104
4 10:40 11:01 Y 6.3 6.043 0.3 Y 0.009 0.008 0.001 0.82 4 10:40 11:01 4.9 5.006
5 11:01 11:22 Y 6.4 6.034 0.4 Y 0.009 0.008 0.001 0.83 5 11:01 11:22 Y 4.9 4.987 -0.101
6 11:22 11:43 Y 6.4 5.89 0.5 Y 0.009 0.008 0.001 0.82 6 11:22 11:43 4.9 5.038
7 11:55 12:16 Y 6.2 5.853 0.4 Y 0.008 0.008 0.000 0.81 7 11:55 12:16 Y 4.9 5.021 -0.086
8 12:16 12:37 Y 6.3 5.805 0.5 Y 0.009 0.008 0.001 0.82 8 12:16 12:37 Y 4.9 5.042 -0.098
9 12:37 12:58 Y 6.4 5.905 0.5 Y 0.009 0.008 0.001 0.82 9 12:37 12:58 Y 4.9 5.005 -0.091
10 13:15 13:36 Y 6.4 5.908 0.5 Y 0.009 0.008 0.001 0.83 10 13:15 13:36 4.9 4.992
11 13:36 13:57 Y 6.6 5.951 0.6 Y 0.009 0.008 0.001 0.85 11 13:36 13:57 Y 4.9 5.008 -0.111
12 13:57 14:18 Y 6.2 5.856 0.4 Y 0.008 0.008 0.000 0.80 12 13:57 14:18 Y 4.9 4.999 -0.079
13 13
14 14
15 15
16 16
Average = 6.4 5.9 0.443 0.01 0.008 0.001 0.83 Average = 4.920 5.000 0.084
Sd Standard Deviation = 0.11 Sd Standard Deviation = 0.000 Sd Standard Deviation = Sd Standard Deviation = 0.03
Confidence Coefficient = 0.081 Confidence Coefficient = 0.000 Confidence Coefficient = Confidence Coefficient = 0.021
RA - Relative Accuracy =8.20%Relative Accuracy = Relative Accuracy = RA - Relative Accuracy =2.13%
n = 9 9 0 n = 9 or RA of 1%0.08%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 = 2.306
E.L. Relative Accuracy = 71% EMRA 4% 0.50% EMRA
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
4. Performance and Equipment Specifications
4.3 Relative accuracy. The RA of the CEMSS shall be no grater than 20 percent of the mean value of the RM test data in terms of the
units of the emission standard or 10 percent of the applicable standard, whichever is greater
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
For SO2 emission standards below 0.20 lbs./MMBtu use 20 Percent of the emission standard;
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
12. Calculate the arithmetic difference between the RM and the CEMSS output for each run. The average of the nine (of more) data sets constitute the RA.
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 1 percent O2 or CO2.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
0241708662/1000ABB
Fuji Electric Co. LTD A1K6856T HF
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
PassedPassedPassed
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Division of Air Quality
Relative Accuracy Test Audit of
Compass Minerals Corporation
Boiler 1
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Date CO Dry CO Dry CO
10/23/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 9:25 9:46
2 9:46 10:07
3 10:07 10:28
4 10:40 11:01
5 11:01 11:22
6 11:22 11:43
7 11:55 12:16
8 12:16 12:37
9 12:37 12:58
10 13:15 13:36
11 13:36 13:57
12 13:57 14:18
13
14
15
16
Average =
Sd Standard Deviation =
Confidence Coefficient =
RA - Relative Accuracy =
n = 0 0 0
t0.975 =
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification Compass Minerals Corporation
Point Source Boiler 1
Contact Phone No.Demise Hubbard
Stack Designation:Boiler 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024
Start Time 9:25 9:46 10:07 10:40 11:01 11:22 11:55 12:16 12:37 13:15 13:36 13:57
Stop Time 9:46 10:07 10:28 11:01 11:22 11:43 12:16 12:37 12:58 13:36 13:57 14:18
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25
As ft^2 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40
Cp (Pitot Tube Coefficient)0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84
Yd Meter Y Factor (unit less)0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870
Pbar Barometric Pressure ("Hg)25.82 25.82 25.82 25.82 25.82 25.82 25.82 25.82 25.82 25.82 25.82 25.82
Pq (Static Pressure)0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70
Ps (Pressure of the Stack)25.87 25.87 25.87 25.87 25.87 25.87 25.87 25.87 25.87 25.87 25.87 25.87
Ts Stack Temp Avg. oF 303.50 304.00 303.00 302.60 303.00 302.50 302.80 302.60 302.50 302.50 302.70 302.70
Tm Meter Temperature oF 89.00 89.00 89.00 100.00 100.00 100.00 100.00 100.00 100.00 102.00 102.00 102.00
CO2 (carbon dioxide)8.93 8.93 8.01 9.15 9.07 8.90 9.08 9.07 9.15 9.16 9.18 9.16
O2 (oxygen)4.95 5.00 4.87 4.90 4.89 4.92 4.94 4.94 4.91 4.87 4.90 4.92
Md Molecular Weight Dry 29.63 29.63 29.48 29.66 29.65 29.62 29.65 29.65 29.66 29.66 29.66 29.66
Ms Molecular Weight Wet 27.92 27.92 27.79 27.91 27.90 27.87 27.89 27.89 27.90 27.89 27.89 27.89
N2 (nitrogen)86.13 86.07 87.12 85.95 86.05 86.19 85.98 85.99 85.94 85.96 85.93 85.93
Vm Sample Volume (cf)42.62 42.62 42.62 42.51 42.51 42.51 42.26 42.26 42.26 42.22 42.22 42.22
Vm std Standard Volume (dscf)34.90 34.90 34.90 34.12 34.12 34.12 33.93 33.93 33.93 33.77 33.77 33.77
Vlc Moisture (g)128.10 128.10 128.10 128.10 128.10 128.10 128.10 128.10 128.10 128.10 128.10 128.10
Vwstd Moisture Volume (scf)6.03 6.03 6.03 6.03 6.03 6.03 6.03 6.03 6.03 6.03 6.03 6.03
Bws Moisture Content (%100)14.73%14.73%14.73%15.02%15.02%15.02%15.09%15.09%15.09%15.15%15.15%15.15%
S Bws (saturation moisture)99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%
AvgSqrtDlp √∆P 0.947 0.951 0.953 0.948 0.948 0.952 0.956 0.956 0.951 0.956 0.952 0.952
Vs. Gas Velocity (ft./sec)69.92 70.23 70.47 69.98 69.98 70.26 70.57 70.59 70.20 70.55 70.25 70.27
Qa (stack actual flow rate) acfm 35,248 35,404 35,525 35,278 35,278 35,419 35,576 35,586 35,389 35,566 35,414 35,425
Qs (stack std. flow rate) dscfm 17,972 18,040 18,126 17,949 17,939 18,023 18,080 18,090 17,992 18,069 17,987 17,993
Qsd (stack std. flow rate) dscfh 1,078,340 1,082,412 1,087,534 1,076,926 1,076,361 1,081,376 1,084,784 1,085,376 1,079,521 1,084,143 1,079,250 1,079,557
Qw (stack flow rate) wscfm 1,264,655 1,269,431 1,275,438 1,267,234 1,266,570 1,272,471 1,277,583 1,278,280 1,271,384 1,277,723 1,271,956 1,272,319
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification Compass Minerals Corporation
Point Source Boiler 1
Contact Phone No.Demise Hubbard
Stack Designation:Boiler 1
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024 10/23/2024
Heat Input - BTU/hr.
F factor - scf/MMBtu 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0
Fuel Analysis - ft3/min 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0
Fuel Flow - ft3/min 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
Heat Input - BTU/hr.0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
SO2 Concentrations
Uncorrected
Dry Corrected
Wet Corrected
NOx Concentrations
Uncorrected 6.60 6.48 6.65 6.28 6.37 6.29 6.15 6.23 6.30 6.40 6.61 6.22
Dry Corrected 6.71 6.55 6.72 6.34 6.44 6.35 6.21 6.29 6.36 6.43 6.60 6.21
Wet Corrected
CO Concentrations
Uncorrected
Dry Corrected
Wet Corrected
CO2 Concentrations
Uncorrected 8.93 8.94 8.02 9.16 9.08 8.91 9.11 9.11 9.19 9.19 9.19 9.17
Dry Corrected 8.93 8.93 8.01 9.15 9.07 8.90 9.08 9.07 9.15 9.16 9.18 9.16
Wet Corrected
O2 Concentrations
Uncorrected 4.87 4.94 4.86 4.90 4.89 4.92 4.94 4.95 4.92 4.88 4.90 4.92
Dry Corrected 4.95 5.00 4.87 4.90 4.89 4.92 4.94 4.94 4.91 4.87 4.90 4.92
Wet Corrected
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 1
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.009 Average % concentration
lbs./hr.CO2 O2
ppm or % 6.43 8.98 4.92
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)9.14E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 8.010E-07
lbs./hr.0.86 8.93 4.95
ppm or %6.71 8.93 4.87
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.95E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.819E-07
lbs./hr.0.85 8.93 5.00
ppm or %6.55 8.93 4.94 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)9.11E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 8.025E-07
lbs./hr.0.87 8.01 4.87
ppm or %6.72 8.02 4.86 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.62E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.578E-07
lbs./hr.0.82 9.15 4.90
ppm or %6.34 9.16 4.90 Raw Value
Run 5
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.74E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.687E-07
lbs./hr.0.8274 9.07 4.89
ppm or %6.44 9.08 4.89 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 1
O2
CO2
Clear
lbs./MMBTU
Run 6
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.64E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.590E-07
lbs./hr.0.8207 8.90 4.92
ppm or %6.35 8.91 4.92 Raw Value
Run 7
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.46E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.421E-07
lbs./hr.0.81 9.08 4.94
ppm or %6.21 9.11 4.94 Raw Value
Run 8
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.58E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.518E-07
lbs./hr.0.82 9.07 4.94
ppm or %6.29 9.11 4.95 Raw Value
Run 9
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.66E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.602E-07
lbs./hr.0.82 9.15 4.91
ppm or %6.36 9.19 4.92 Raw Value
Run 10
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.72E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.679E-07
lbs./hr.0.83 9.16 4.87
ppm or %6.43 9.19 4.88 Raw Value
Run 11
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.97E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.887E-07
lbs./hr.0.85 9.18 4.90
ppm or %6.60 9.19 4.90 Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Compass Minerals Boiler #1 RATA RM 1, 2, 3A, 7E (tested 10-23-2024)
Calibration Error Test
Test Date October 23, 2024 O2
CS - Cal. Span 22.69
Units %
Cylinder No. Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.00% Passed Cal.
Mid-level 11.06 11.06 0.00 0.00% Passed Cal.
High-level 22.69 22.04 0.65 2.86% Failed 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 48.74%
100% of Cal. Span High-level 100.00%
Test Date October 23, 2024 CO2
CS - Cal. Span 22.69
Units %
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
Mid-level 11.13 11.13 0.00 0.000% Passed Cal.
High-level 22.69 22.69 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 49.05%
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 October 23, 2024 NOx
CS - Cal. Span 18.26
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
Mid-level 8.89 8.90 0.01 0.055% Passed Cal.
High-level 18.26 18.30 0.04 0.219% 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 48.69%
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
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Reference Methods 2, 3A, 6C, 7E, 10, & 19
Source Information
Company Name Compass Minerals Corporation
Company Contact:Demise Hubbard
Contact Phone No.801-732-3312
Stack Designation:Boiler 2
Test & Review Dates
Test Date:10/17/2024
Review Date: 7/9/2025
Observer:Not Observed
Reviewer:Rob Leishman
Emission Limits Emission Rates
SO2 NOX CO SO2 NOX CO
lbs./MMBtu 0.2000 0.008
lbs./hr.
ppm 9.0 5.836
%O2 Correction as a whole #
Test Information
Stack I.D. inches
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
39.25 8.402 0.9870 1.862 0.84 25.90 0.7 25.951471
Contractor Information
Contact:Richard Sollars
Contracting Company: Mostardi Platt
Address: 702 West 48th Ave, Denver, CO 80216
Phone No.: 630-993-2100
Project No.:
8710

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/MMBtu wscf/MMBtu scf/MMBtu Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
Lignite
Natural
Propane
Butane
10100
COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Wet CEM
Correct For O2
CO2 Interference w/CO
Yes
Yes
Yes
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 2
SO2 Analyzer:Serial No.:
CO2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Test Date SO2 Dry SO2 Dry SO2 Test Date % CO2 Dry
10/17/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 10/17/2024 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 7:40 8:01 1 7:40 8:01 8.6
2 8:01 8:22 2 8:01 8:22 8.5
3 8:22 8:43 3 8:22 8:43 8.6
4 8:53 9:14 4 8:53 9:14 8.8
5 9:14 9:35 5 9:14 9:35 8.8
6 9:35 9:56 6 9:35 9:56 8.8
7 10:08 10:29 7 10:08 10:29 8.7
8 10:29 10:50 8 10:29 10:50 8.7
9 10:50 11:11 9 10:50 11:11 8.6
10 11:20 11:41 10 11:20 11:41 8.7
11 11:41 12:02 11 11:41 12:02 8.7
12 12:02 12:23 12 12:02 12:23 8.6
13 13
14 14
15 15
16 16
Average = Average =
Sd Standard Deviation = Sd Standard Deviation = Sd Standard Deviation = Sd Standard Deviation =
Confidence Coefficient = Confidence Coefficient = Confidence Coefficient = Confidence Coefficient =
RA - Relative Accuracy = RA RA RA - Relative Accuracy =
n = 0 0 0 n = 0 or RA of 1%
t0.975 = t0.975 =
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;0
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
13.2 Relative accuracy Performance Specification. The RA of the CEMSS must be not greater than 20 percent when RM is used in the denominator of Eq. 2-6
(average emissions during test are greater than 50 percent of the emission standard)or 10 percent when the applicable emission standard is used in the
denominator of Eq. 2-6 (average emissions during test are less than 50 percent of the emission standard).
Up dated January 17, 2006
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
13.2 CEMS Relative Accuracy Perfromance Specification.
The RA of the CEMS must be no grater than 20 percent of the mean value of the reference method (RM) data. 1 percent O2 or CO2.
The results are also acceptable if the absolute value of the difference between the mean RM value and the mean CEMS value is less than or equal to 1.0 percent O2 (or CO2).
Up dated September 14, 2016
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Division of Air Quality
Relative Accuracy Test Audit of
Compass Minerals Corporation
Boiler 2
NOX Analyzer:Serial No.:
O2 Analyzer:Serial No.:
Acquisition System:Serial No.:
Acquisition System: Serial No.:
Equivalent Emission Limit:9.00 0.2
Date NOx Dry NOx Dry NOx Test Date % O2 Dry
10/17/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff 9/30/2014 RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr. Run#
Start
Time End Time %c %c
1 7:40 8:01 Y 5.8 5.739 0.1 Y 0.008 0.008 0.000 0.73 1 7:40 8:01 5.4 5.495
2 8:01 8:22 Y 5.8 5.767 0.0 Y 0.008 0.008 0.000 0.73 2 8:01 8:22 Y 5.5 5.483 -0.013
3 8:22 8:43 Y 5.8 5.796 0.0 Y 0.008 0.008 0.000 0.73 3 8:22 8:43 5.4 5.454
4 8:53 9:14 Y 5.9 5.71 0.2 Y 0.008 0.008 0.000 0.74 4 8:53 9:14 Y 5.5 5.511 -0.016
5 9:14 9:35 6.0 5.666 0.008 0.008 0.75 5 9:14 9:35 5.5 5.55
6 9:35 9:56 6.0 5.675 0.008 0.008 0.75 6 9:35 9:56 Y 5.5 5.556 -0.026
7 10:08 10:29 5.9 5.604 0.008 0.008 0.74 7 10:08 10:29 Y 5.5 5.512 0.003
8 10:29 10:50 Y 5.8 5.628 0.2 Y 0.008 0.008 0.000 0.73 8 10:29 10:50 Y 5.5 5.541 -0.031
9 10:50 11:11 Y 5.8 5.643 0.1 Y 0.008 0.008 0.000 0.73 9 10:50 11:11 Y 5.5 5.535 -0.015
10 11:20 11:41 Y 5.8 5.771 0.0 Y 0.008 0.008 0.000 0.76 10 11:20 11:41 Y 5.5 5.484 -0.019
11 11:41 12:02 Y 5.8 5.63 0.1 Y 0.008 0.008 0.000 0.76 11 11:41 12:02 Y 5.5 5.542 -0.012
12 12:02 12:23 Y 5.8 5.563 0.2 Y 0.008 0.008 0.000 0.76 12 12:02 12:23 Y 5.5 5.528 0.002
13 13
14 14
15 15
16 16
Average = 5.8 5.7 0.104 0.01 0.008 0.000 0.74 Average = 5.500 5.520 0.014
Sd Standard Deviation = 0.07 Sd Standard Deviation = 0.000 Sd Standard Deviation = Sd Standard Deviation = 0.01
Confidence Coefficient = 0.057 Confidence Coefficient = 0.000 Confidence Coefficient = Confidence Coefficient = 0.008
RA - Relative Accuracy =2.80%Relative Accuracy = Relative Accuracy = RA - Relative Accuracy =0.40%
n = 9 9 0 n = 9 or RA of 1%0.02%
t0.975 = 2.306 t0.975 = 2.306 t0.975 = t0.975 = 2.306
E.L. Relative Accuracy = 64% EMRA 4% 0.00% EMRA
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 2 For SO2 and NOx Continuous Emission Monitoring Systems
4. Performance and Equipment Specifications
4.3 Relative accuracy. The RA of the CEMSS shall be no grater than 20 percent of the mean value of the RM test data in terms of the
units of the emission standard or 10 percent of the applicable standard, whichever is greater
For SO2 emission standards between 0.30 and 0.20 lbs./MMBtu use 15 Percent of the applicable standard;
For SO2 emission standards below 0.20 lbs./MMBtu use 20 Percent of the emission standard;
40 CFR 60 Performance Specification 3 For O2 and CO2 Continuous Emission Monitoring Systems
12. Calculate the arithmetic difference between the RM and the CEMSS output for each run. The average of the nine (of more) data sets constitute the RA.
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 1 percent O2 or CO2.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
PassedPassedPassed
0241708662/1000ABB
Fuji Electric Co. LTD A1K6854T HF
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Division of Air Quality
Relative Accuracy Test Audit of
Compass Minerals Corporation
Boiler 2
CO Analyzer:Serial No.:
Acquisition System:
Acquisition System: Serial No.:
Equivalent Emission Limit:
Date CO Dry CO Dry CO
10/17/2024 RM CEMS Diff RM CEMS Diff RM CEMS Diff
Run#Start
Time
End
Time ppm lbs./MMBtu lbs./hr.
1 7:40 8:01
2 8:01 8:22
3 8:22 8:43
4 8:53 9:14
5 9:14 9:35
6 9:35 9:56
7 10:08 10:29
8 10:29 10:50
9 10:50 11:11
10 11:20 11:41
11 11:41 12:02
12 12:02 12:23
13
14
15
16
Average =
Sd Standard Deviation =
Confidence Coefficient =
RA - Relative Accuracy =
n = 0 0 0
t0.975 =
E.L. Relative Accuracy =
a For steam generators;b Average of three samples;
c Make sure that RM and M data are on a consistent basis either wet or dry.
40 CFR 60 Performance Specification 4 For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
applicable emission standard is used to calculate RA.
40 CFR 60 Performance Specification 4A For Carbon Monoxide (CO) Continuous Emission Monitoring Systems
13.2 Relative accuracy. The RA of the CEMSS must be no greater than 10 percent when the average RM value is used to calculate RA, 5 percent when the applicable
emission standard is used to calculate RA, or within 5 ppmv when the RA is calculated as the absolute average difference between the RM and CEMSS plus the 2.5
percent confidence coefficient.
40 CFR 60 Performance Specification 6 For Continuous Emission Rate Monitoring Systems (CERMS)
13.2 CERMS Relative Accuracy. The RA of the CERMS shall be no greater than 20 percent of the mean value of the RM's test data in terms of the nits of the emission
standard, or 10 percent of the applicable standard, which err is greater.
Up dated January 17, 2006
13.2 Relative accuracy. The RA of the CEMSS must be no grater than 10 percent when the average of the RM value is used to calculate RA or 5 percent when the
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Ac
t
i
v
a
t
e

R
u
n
?
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification Compass Minerals Corporation
Point Source Boiler 2
Contact Phone No.Demise Hubbard
Stack Designation:Boiler 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024
Start Time 7:40 8:01 8:22 8:53 9:14 9:35 10:08 10:29 10:50 11:20 11:41 12:02
Stop Time 8:01 8:22 8:43 9:14 9:35 9:56 10:29 10:50 11:11 11:41 12:02 12:23
Run Time 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21 0:21
Stack I.D. (inches)39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25 39.25
As ft^2 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40 8.40
Cp (Pitot Tube Coefficient)0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84 0.84
Yd Meter Y Factor (unit less)0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870 0.9870
Pbar Barometric Pressure ("Hg)25.90 25.90 25.90 25.90 25.90 25.90 25.90 25.90 25.90 25.90 25.90 25.90
Pq (Static Pressure)0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70 0.70
Ps (Pressure of the Stack)25.95 25.95 25.95 25.95 25.95 25.95 25.95 25.95 25.95 25.95 25.95 25.95
Ts Stack Temp Avg. oF 322.60 322.50 322.50 322.10 322.60 322.70 322.10 322.00 322.50 322.00 322.60 322.10
Tm Meter Temperature oF 88.00 88.00 88.00 88.00 88.00 88.00 87.00 87.00 87.00 87.00 87.00 87.00
CO2 (carbon dioxide)8.59 8.50 8.58 8.80 8.84 8.85 8.69 8.67 8.64 8.70 8.65 8.62
O2 (oxygen)5.42 5.47 5.42 5.50 5.52 5.53 5.52 5.51 5.52 5.47 5.53 5.53
Md Molecular Weight Dry 29.59 29.58 29.59 29.63 29.63 29.64 29.61 29.61 29.60 29.61 29.61 29.60
Ms Molecular Weight Wet 27.60 27.59 27.60 27.65 27.65 27.66 27.64 27.64 27.63 28.14 28.14 28.13
N2 (nitrogen)86.00 86.03 86.00 85.70 85.64 85.62 85.79 85.82 85.84 85.84 85.82 85.85
Vm Sample Volume (cf)42.18 42.18 42.18 42.10 42.10 42.10 42.07 42.07 42.07 42.18 42.18 42.18
Vm std Standard Volume (dscf)34.71 34.71 34.71 34.64 34.64 34.64 34.68 34.68 34.68 34.77 34.77 34.77
Vlc Moisture (g)153.30 153.30 153.30 150.60 150.60 150.60 150.80 150.80 150.80 107.10 107.10 107.10
Vwstd Moisture Volume (scf)7.22 7.22 7.22 7.09 7.09 7.09 7.10 7.10 7.10 5.04 5.04 5.04
Bws Moisture Content (%100)17.21%17.21%17.21%16.99%16.99%16.99%16.99%16.99%16.99%12.66%12.66%12.66%
S Bws (saturation moisture)99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%99.90%
AvgSqrtDlp √∆P 0.958 0.958 0.957 0.961 0.956 0.959 0.960 0.956 0.955 0.953 0.957 0.960
Vs. Gas Velocity (ft./sec)71.95 71.91 71.80 72.02 71.67 71.89 71.97 71.69 71.66 70.81 71.13 71.33
Qa (stack actual flow rate) acfm 36,271 36,251 36,196 36,307 36,130 36,241 36,282 36,140 36,125 35,697 35,858 35,959
Qs (stack std. flow rate) dscfm 17,572 17,565 17,538 17,648 17,551 17,603 17,636 17,569 17,551 18,258 18,327 18,390
Qsd (stack std. flow rate) dscfh 1,054,339 1,053,887 1,052,275 1,058,903 1,053,083 1,056,181 1,058,131 1,054,149 1,053,035 1,095,492 1,099,599 1,103,396
Qw (stack flow rate) wscfm 1,273,537 1,272,991 1,271,044 1,275,591 1,268,581 1,272,312 1,274,705 1,269,908 1,268,566 1,254,320 1,259,022 1,263,370
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Test Overview
NSPS Relative Accuracy
Performance Specification Test -
CEMS Certification Compass Minerals Corporation
Point Source Boiler 2
Contact Phone No.Demise Hubbard
Stack Designation:Boiler 2
Project No.:0
Run Run # 1 Run # 2 Run # 3 Run # 4 Run # 5 Run # 6 Run # 7 Run # 8 Run # 9 Run # 10 Run # 11 Run # 12
Test Date 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024 10/17/2024
Heat Input - BTU/hr.
F factor - scf/MMBtu 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0 8710.0
Fuel Analysis - ft3/min 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0 1050.0
Fuel Flow - ft3/min 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
Heat Input - BTU/hr.0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
SO2 Concentrations
Uncorrected
Dry Corrected
Wet Corrected
NOx Concentrations
Uncorrected 5.82 5.81 5.80 5.78 5.79 5.78 5.79 5.81 5.80 5.81 5.76 5.78
Dry Corrected 5.81 5.80 5.79 5.87 5.99 5.98 5.88 5.80 5.79 5.80 5.75 5.77
Wet Corrected
CO Concentrations
Uncorrected
Dry Corrected
Wet Corrected
CO2 Concentrations
Uncorrected 8.57 8.52 8.60 8.82 8.85 8.86 8.70 8.67 8.64 8.70 8.65 8.62
Dry Corrected 8.59 8.50 8.58 8.80 8.84 8.85 8.69 8.67 8.64 8.70 8.65 8.62
Wet Corrected
O2 Concentrations
Uncorrected 5.41 5.47 5.42 5.50 5.53 5.54 5.52 5.51 5.52 5.46 5.52 5.52
Dry Corrected 5.42 5.47 5.42 5.50 5.52 5.53 5.52 5.51 5.52 5.47 5.53 5.53
Wet Corrected
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 2
Average Emission
Dry SO2 NOX CO
lbs./MMBtu 0.008 Average % concentration
lbs./hr.CO2 O2
ppm or % 5.84 8.68 5.49
Run 1 Enter O2 or CO2
Dry SO2 NOX CO CO2 O2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.16E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.944E-07
lbs./hr.0.73 8.59 5.42
ppm or %5.81 8.57 5.41
Run 2
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.18E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.932E-07
lbs./hr.0.73 8.50 5.47
ppm or %5.80 8.57 5.47 Raw Value
Run 3
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.14E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.920E-07
lbs./hr.0.73 8.58 5.42
ppm or %5.79 8.60 5.42 Raw Value
Run 4
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.29E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.016E-07
lbs./hr.0.74 8.80 5.50
ppm or %5.87 8.82 5.50 Raw Value
Run 5
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.47E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.154E-07
lbs./hr.0.7534 8.84 5.52
ppm or %5.99 8.85 5.53 Raw Value
Corrected For Cal. Drift
Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
O2
CO2
Clear
lbs./MMBTU
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Compass Minerals Corporation
Boiler 2
O2
CO2
Clear
lbs./MMBTU
Run 6
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.46E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.141E-07
lbs./hr.0.7542 8.85 5.53
ppm or %5.98 8.86 5.54 Raw Value
Run 7
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.32E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 7.028E-07
lbs./hr.0.74 8.69 5.52
ppm or %5.88 8.70 5.52 Raw Value
Run 8
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.20E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.932E-07
lbs./hr.0.73 8.67 5.51
ppm or %5.80 8.67 5.51 Raw Value
Run 9
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.19E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.920E-07
lbs./hr.0.73 8.64 5.52
ppm or %5.79 8.64 5.52 Raw Value
Run 10
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.18E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.932E-07
lbs./hr.0.76 8.70 5.47
ppm or %5.80 8.70 5.46 Raw Value
Run 11
Dry SO2 NOX CO CO2 O2
Atomic Weight 64 46 28
lbs./MMBtu (O2)8.14E-03 E=Cd x Fd x (20.9/(20.9-%O2d))
lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d)
lbs./cu.ft 6.873E-07
lbs./hr.0.76 8.65 5.53
ppm or %5.75 8.65 5.52 Raw Value
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Corrected For Cal. Drift
Compass Minerals Boiler #2 RATA RM 1, 2, 3A, 7E (tested 10-17-2024 )
Calibration Error Test
Test Date October 17, 2024 O2
CS - Cal. Span 22.04
Units %
Cylinder No. Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.00% Passed Cal.
Mid-level 11.06 11.05 0.01 0.05% Passed Cal.
High-level 22.04 22.05 0.01 0.05% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of CS - Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 50.18%
100% of Cal. Span High-level 100.00%
Test Date October 17, 2024 CO2
CS - Cal. Span 22.69
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 0.01 0.01 0.044% Passed Cal.
Mid-level 11.13 11.13 0.00 0.000% Passed Cal.
High-level 22.69 22.70 0.01 0.044% Passed Cal.
% of Span Sec. 8.2.1 Cal Gas Verification
0 to 20% of Cal. Span Low-Level 0.00%
40 to 60% of Cal. Span Mid-level 49.05%
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 October 17, 2024 NOx
CS - Cal. Span 18.26
Units ppm
Cylinder
No.
Expiration
Date Cal. Gas CV- Certified
Concentration
CDir or CS -
Measured
Concentration
Difference
ACE Eq. 7E-1
Analyzer Cal.
Error
Status
Low-level 0.00 0.00 0.00 0.000% Passed Cal.
Mid-level 8.89 8.90 0.01 0.055% Passed Cal.
High-level 18.26 18.30 0.04 0.219% 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 48.69%
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