DAQ-2024-011633

1

DAQC-1135-24
Site ID 10303 (B4)

MEMORANDUM

TO: STACK TEST FILE – ASH GROVE CEMENT COMPANY

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Robert Sirrine, Environmental Scientist

DATE: November 12, 2024

SUBJECT: Sources: Main Kiln, Coal Mill, and Clinker Cooler
Contact: Cody Watkins, 435-857-1283
Location: Leamington, UT
Tester: Mostardi Platt, Mike Lipinski – 630-993-2100
FRS ID #: UT0000004902300015
Permit #: Title V permit 2300015005, dated September 22, 2023, revised
May 13, 2024
Subject: Review of Stack Test Report dated August 6, 2024, and additional data
emailed November 6, 2024

On August 6, 2024, DAQ received a test report for the Ash Grove Cement Company Main Kiln (MK), Coal
Mill (CM), and Clinker Cooler (CC) stacks at the Leamington, UT plant. Additional data was received
November 6, 2024. Testing was performed on June 11-13, 2024, to demonstrate compliance with the emission
limits found in Conditions II.B.4.g, II.B.4.l, II.B.4.m, II.B.4.n, II.B.4.q, II.B.5.a, II.B.9.c, II.B.9.d, and II.B.9.e.
The DAQ-calculated test results are:

Source Test Date RM/Pollutant DAQ Result Test Result Limit

MK/Mill On 6/13/24 5/PM 0.013* 0.013* 0.07 *

MK/Mill Off 6/12/24 5/PM 0.007* 0.007* 0.07 *

CM/Mill On 6/13/24 5/PM 0.006* 0.006* 0.07*

CM/Mill Off 6/12/24 5/PM 0.005* 0.005* 0.07*

CC 6/13/24 5/PM 0.002* 0.002* 0.07*

CM Mill On 6/13/24 30B/Hg 0.30** 0.32** 55**

CM Mill On 6/13/24 25A/THC 14.2 ppmdv^ 14.2 ppmdv^ 24 ppmdv^

MK/Mill On 6/11/24 23/D/F 0.002 ng/dscm^ 0.002 ng/dscm^ <0.20 ng/dscm^

MK/Mill Off 6/12/24 23/D/F 0.12 ng/dscm^ 0.12 ng/dscm^ <0.20 ng/dscm^

NOTE: *lb/ton of clinker produced, ** lb/MM tons of clinker produced ^@ 7% O2

2

DEVIATIONS: None.

CONCLUSION: The stack testing report appears to be complete and found to be
acceptable with additional data emailed on November 6, 2024.

RECOMMENDATION: Ash Grove Cement Company appears to have been in compliance at
the time of testing with the above tested for emission limits on the
Main Kiln, Coal Mill, and Clinker Cooler stacks with the mill on and
off as stipulated. These tests established a new site-specific (SSOL)
30-day rolling average Operating Limit (OPL) for PM based on
backscatter %; as required by 40 CFR 63, Subpart LLL. The average
back scatter for the CC was 6.2% and for the MK/CM it was 11.1 %.
These values are measured during the CC and MK/CM PM testing
and then used in a specified equation to produce the new 30-day
rolling average PM CPMS action limit. The limits established during
the June 11-13, 2024, testing are MK/CM 46.7 and CC 33.3
milliamps or digital equivalent. These are continuous parametric
monitoring system values read from process monitors in milliamps
and totaled on a rolling 30-day average that would require action if
exceeded.

HPV: No

ATTACHMENTS: Stack test report Received August 6, 2024
Additional data received via email November 6, 2024
DAQ generated Excel review spreadsheets.
Compliance Emissions
Test Report
Ash Grove Cement Company
Leamington Plant
Clinker Cooler Stack, Coal Mill Stack, and
Main Kiln Stack
Leamington, Utah
Report No. M242413B
June 11 through 13, 2024
Crown Point, IN I Mendota Heights, MN I Denver, CO | Henderson, NV
Corporate Headquarters 888 Industrial Drive Elmhurst, Illinois 60126
630-993-2100
Compliance Emissions
Test Report

Ash Grove Cement Company Leamington Plant Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Leamington, Utah June 11 through 13, 2024

Report Submittal Date August 5, 2024

© Copyright 2024
All rights reserved in Mostardi Platt

Project No. M242413B
TABLE OF CONTENTS

1.0 EXECUTIVE SUMMARY ............................................................................................................................... 1
2.0 TEST METHODOLOGY ................................................................................................................................ 2 Method 1 Traverse Point Determination ................................................................................................... 2 Method 2 Volumetric Flowrate Determination .......................................................................................... 3 Method 3A Oxygen (O2)/Carbon Dioxide (CO2) Determination ................................................................ 3
Method 5 Filterable Particulate Matter (FPM) Determination ................................................................... 3 Method 23 Dioxin and Furan Determination ............................................................................................. 3 Method 25A THC Determination ............................................................................................................ 4 Method 30B Mercury Determination ......................................................................................................... 4
3.0 TEST RESULT SUMMARIES ....................................................................................................................... 5
4.0 CERTIFICATION.......................................................................................................................................... 13

APPENDIX Appendix A - Operating Data .................................................................................................................. 15 Appendix B - Test Section Diagram ....................................................................................................... 76 Appendix C - Sample Train Diagrams .................................................................................................... 82 Appendix D - Calculation Nomenclature and Formulas ......................................................................... 89
Appendix E - Laboratory Sample Analysis ........................................................................................... 108 Appendix F - Reference Method Test Data .......................................................................................... 152 Appendix G - Field Data Sheets ........................................................................................................... 216 Appendix H - Calibration Data .............................................................................................................. 257 Appendix I - Gas Cylinder Calibrations ................................................................................................. 299 Appendix J – Mercury QA/QC Data ...................................................................................................... 307
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
i ©Mostardi Platt

1.0 EXECUTIVE SUMMARY
Mostardi Platt conducted a compliance emissions test program for Ash Grove Cement Company on June 11 through 13, 2024 on the Clinker Cooler Stack, Main Kiln Stack, and Coal Mill Stack at the Leamington Cement Plant in Leamington, Utah. This report summarizes the results of the test
program and test methods used. The test locations, test dates, and test parameters are summarized below.

TEST OVERVIEW
Test Locations Test Dates Test Parameters
Clinker Cooler Stack June 13, 2024 Filterable Particulate Matter (FPM)
Main Kiln Stack June 11 through 13, 2024 FPM, polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofurans (D/F)
Coal Mill Stack June 12 and 13, 2024 CO2, FPM, total hydrocarbons (THC), and Mercury (Hg)
The purpose of the test program was to evaluate the emissions during the specified operating conditions to satisfy the regulatory requirements of Utah Department of Environmental Quality (UDEQ) Operating Permit No. 2300015004 and as required in 40CFR63, Subpart LLL. Selected
results of the test program are summarized below. A complete summary of emission test results follows the narrative portion of this report.
FILTERABLE PARTICULATE MATTER EMISSION SUMMARY
Test Location Source Condition Test Dates Emission Limit Average Emission Rate, lb/ton
Clinker Cooler Stack Normal 6/13/24
0.07 lb/ton
0.002 lb/ton
Main Kiln Mill On 6/13/24 0.013 lb/ton
Mill Off 6/12/24 0.007 lb/ton
Coal Mill Stack Mill On 6/13/24 0.006 lb/ton
Mill Off 6/12/24 0.005 lb/ton

MAIN KILN STACK D/F EMISSION SUMMARY
Test Location Source Condition Test Date Parameter Emission Limit Average Emission Rate
Main Kiln Mill On 6/11/24 D/F ≤0.20 ng/dscm (TEQ)1 0.002 ng/dscm
Mill Off 6/12/24 D/F ≤0.20 ng/dscm (TEQ)1 0.12 ng/dscm

1 If the average temperature at the inlet to the first PM control device (fabric filter or electrostatic precipitator) during the D/F performance test is 400 °F or less, this limit is changed to 0.40 ng/dscm (TEQ).
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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COAL MILL STACK Hg AND THC EMISSION SUMMARY
Test Location Source Condition Test Date Parameter Emission Limit Average Emission Rate
Coal Mill Stack Mill On 6/13/24
CO2 N/A 6.1%
Hg 55 lb/MM tons of clinker 0.32 lb/MM tons of clinker
THC 24 ppmvd@7%O2 14.2 ppmvd@7%O2
Operating data as provided by Ash Grove Cement Company is included in Appendix A. The identifications of the individuals associated with the test program are summarized below.

TEST PERSONNEL INFORMATION
Location Address Contact
Test Facility Ash Grove Cement Company UT-132 Leamington, UT 84638
Mr. Cody Watkins Environmental Manager [phone] [e-mail]
Testing Company
Representative
Mostardi Platt
7715 Commercial Way, Suite 155 Henderson, NV 89011
Mr. Mike Lipinski
Senior Project Manager [phone] [e-mail] www.mostardiplatt.com

The test crew consisted of A. Robles, R. Sollars, E. Rodriguez, R. Bogenegra and M. Lipinski of Mostardi Platt.
2.0 TEST METHODOLOGY
Emission testing was conducted following the methods specified in 40 CFR, Part 60, Appendix A. Schematics of the test section diagrams and sampling trains used are included in Appendix B and C, respectively. Calculation examples and nomenclature are included in Appendix D and
laboratory analysis data are found in Appendix E. Copies of analyzer print-outs and field data sheets for each test run are included in Appendix F and G, respectively. The following methodologies were used during the test program:
Method 1 Traverse Point Determination
Test measurement points were selected in accordance with Method 1. The characteristics of the measurement location are summarized below.

Location Diameter (Feet) Upstream Diameters Downstream Diameters Test Parameter Number of Sampling Points
Clinker Cooler Stack 8.75 2.5 3.4 FPM 24
Main Kiln 11.00 4.1 5.5 FPM, D/F 20
Coal Mill Stack 2.417 1.8 6.3
FPM 24
CO2, THC, Hg 3
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Method 2 Volumetric Flowrate Determination Gas velocity was measured following Method 2, for purposes of calculating stack gas volumetric flow rate. S-type pitot tubes, differential pressure gauges, thermocouples and temperature readouts were used to determine gas velocity at each sample point at each test location. All of the equipment used was calibrated in accordance with the specifications of the Method. Calibration data are presented in Appendix H. Method 3A Oxygen (O2)/Carbon Dioxide (CO2) Determination Stack gas molecular weight was determined in accordance with Method 3A. Servomex or ECOM analyzers were used to determine stack gas oxygen and carbon dioxide content and, by difference, nitrogen content at the Main Kiln Stack and Coal Mill Stack test locations. A Fyrite analyzer was used on the Main Kiln Stack during the Raw Mill Off condition. An ECOM analyzer was initially used at the Clinker Cooler Stack; however, all readings were ambient throughout run
1. Ambient O2 and CO2 values were verified by Fyrite during runs two and three at the Clinker Cooler. All of the equipment used was calibrated in accordance with the specifications of the Method and calibration data are included in Appendix H. Copies of the gas cylinder certifications
are included in Appendix I. Method 5 Filterable Particulate Matter (FPM) Determination
Stack gas particulate concentrations and emission rates were determined in accordance with
Method 5, 40 CFR, Part 60, Appendix A. An Environmental Supply Company, Inc. sampling train was used to sample stack gas at an isokinetic rate, as specified in the Method. Particulate matter in the sample probe was recovered using an acetone rinse. The probe wash and filter catch were
analyzed by Mostardi Platt personnel in accordance with the Method. For any runs where the filter weight was below the calculated reporting detection limit of 0.15 mg,
filter weight results were adjusted to a weight differential of 0.15 mg gain on the filter. Laboratory data are found in Appendix E. All of the equipment used was calibrated in accordance with the specifications of the Method. Calibration data are presented in Appendix H. Method 23 Dioxin and Furan Determination
Stack gas dioxin and furan concentrations and emission rates were determined in accordance with Method 23, 4CFR60, Appendix A. An Environmental Supply Company sampling train was used to sample for concentrations of dioxins and furans, in the manner specified in the Method. A total of twelve (12) test points will be sampled per run. Six (6) test points were sampled using
the two (2) ports that are 90 degrees apart at the stack test location. The alternative recovery procedure was used that removes the methylene chloride recovery solvent rinse for toluene, as specified in ALT-036 - Approval Method 23 Modification for Cement Kilns. After recovery, samples were analyzed by an accredited laboratory following the procedures specified in the Method. Laboratory data are found in Appendix E. All of the equipment used was calibrated in accordance with the specifications of the Method. Calibration data are presented in Appendix H.
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Method 25A THC Determination The Method 25A sampling and measurement system met the requirements for stack sampling of THC set forth by the United States Environmental Protection Agency (USEPA). In particular, it met the requirements of USEPA Reference Method 25A, “Determination of Total Gaseous Organic Concentration Using a Flame Ionization Analyzer,” 40CFR60, Appendix A. This method applies to the measurement of total gaseous organic concentration of hydrocarbons. With this method, gas samples were extracted from the sample locations through heated Teflon sample lines to the analyzers.
The flame ionization detectors (FIDs) used during this program were Thermo 51 Series Total Hydrocarbon Analyzers. They are highly sensitive FIDs that provide a direct reading of total organic vapor concentrations with linear ranges of 0-10, 100, 1000, and 10,000 ppm by volume.
The instruments were calibrated using ultra-zero air and propane in air EPA Protocol standards. The calibrations were performed before and after sampling with calibration checks performed between each test run. Final concentrations are reported in ppm volume, dry as propane.
Calculations were performed by computer or by hand. An explanation of the nomenclature and calculations are included in Appendix D of this report. Calibration data are presented in Appendix H. Method 30B Mercury Determination
Paired trains were utilized sampling three test points per test run at the Coal Mill Stack. Per Method 30B sampling, each sample was collected on the paired in-situ sorbent traps with the B side being spiked. Spike values were based off of historical data. A tube of silica was used to capture remaining moisture prior to the sample reaching the gas metering system. The sample train used for this test program was designed by APEX, Inc. and meets all requirements for Method 30B sampling. Samples were analyzed onsite utilizing an Ohio Lumex, Inc. analyzer for total gaseous mercury. Concurrent Method 5 testing flow rates were used in order to calculate Hg emission rates on a lb/MM tons of clinker basis. Sample analysis data and mercury
quality assurance and control data are found in Appendix E. All of the equipment used was calibrated in accordance with the specifications of the Method.
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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3.0 TEST RESULT SUMMARIES

Client:
Facility:
Test Location:
Test Method:
Normal Normal Normal
6/13/24 6/13/24 6/13/24
7:30 9:45 12:10
9:39 11:54 14:19
Run 1 Run 2 Run 3 Average
232.7 237.5 240.0 236.7
1.8% 1.5% 1.7% 1.7%
25.05 25.05 25.05 25.05
90.982 88.735 87.215 88.977
37.472 36.780 36.295 36.849
135,197 132,700 130,948 132,948
84,696 82,855 81,267 82,939
86,279 84,104 82,697 84,360
102.1 101.8 102.0 102.0
ton/hr 115.8 116.0 116.1 116.0
5.7 6.2 6.7 6.2
0.00079 0.00080 0.00452 0.00204
0.0001 0.0001 0.0005 0.0002
0.0001 0.0001 0.0008 0.0003
0.097 0.099 0.557 0.251
0.001 0.001 0.005 0.002
Stack Conditions
End Time
Isokinetic Variance
Flue Gas Moisture, percent by volume
grains/dscf
Gas Volumetric Flow Rate, scfm
grams collected
CPMS Response, % Back Scatter
lb/ton of clinker
Date
Start Time
Average Gas Temperature, °F
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Average Flue Pressure, in. Hg
Gas Sample Volume, dscf
Filterable Particulate Matter (Method 5)
lb/hr
grains/acf
Ash Grove Cement Company
Leamington Cement Plant
Clinker Cooler Stack
Average Gas Velocity, ft/sec
Source Condition
5
Clinker Production Rate,
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Client:
Facility:
Test Location:
Test Method:
Mill Off Mill Off Mill Off
6/12/24 6/12/24 6/12/24
5:55 8:20 10:55
8:03 10:29 13:04
Run 1 Run 2 Run 3 Average
346.2 380.3 380.7 369.1
10.6% 9.6% 10.4% 10.2%
24.99 24.99 24.99 24.99
99.318 95.761 96.603 97.227
53.671 54.312 54.427 54.137
306,032 309,687 310,340 308,686
149,651 146,964 145,929 147,515
167,422 162,542 162,820 164,261
13.7 13.6 13.9 13.7
10.2 10.4 10.9 10.5
98.4 96.6 98.2 97.7
ton/hr 109.8 109.9 109.8 109.8
10.0 11.8 11.6 11.1
0.00498 0.00438 0.00215 0.00384
0.0004 0.0003 0.0002 0.0003
0.0008 0.0007 0.0003 0.0006
0.992 0.889 0.430 0.770
0.009 0.008 0.004 0.007
Stack Conditions
End Time
Isokinetic Variance
Flue Gas Moisture, percent by volume
grains/dscf
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Average %CO2 by volume, dry basis
grams collected
CPMS Response, % Back Scatter
lb/ton of clinker
Date
Start Time
Average Gas Temperature, °F
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Average Flue Pressure, in. Hg
Gas Sample Volume, dscf
Filterable Particulate Matter (Method 5)
lb/hr
grains/acf
Ash Grove Cememnt Company
Leamington Cement Plant
Main Kiln Stack
Average Gas Velocity, ft/sec
Source Condition
5
Clinker Production Rate,
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Client:
Facility:
Test Location:
Test Method:
Mill On Mill On Mill On Spiked
6/13/24 6/13/24 6/13/24 6/13/24
7:30 9:45 12:10 14:30
9:39 11:54 14:19 16:39
Run 1 Run 2 Run 3 Run 4 Average
226.7 225.6 224.2 224.5 225.3
14.7% 14.6% 14.3% 14.0% 14.4%
25.03 25.03 25.03 25.03 25.03
69.48 70.346 73.162 72.835 71.456
50.449 50.952 52.881 52.643 51.731
287,657 290,530 301,525 300,170 294,971
157,765 159,911 166,865 166,584 162,781
185,016 187,170 194,656 193,687 190,132
15.5 16.1 15.7 15.7 15.8
11.6 11.4 11.6 11.4 11.5
101.6 101.4 101.1 100.8 101.2
ton/hr 107.8 108.8 108.8 108.8 108.6
10.3 10.2 10.8 23.5 13.7
0.00361 0.00334 0.00205 0.00988 0.00472
0.0004 0.0004 0.0002 0.0012 0.0006
0.0008 0.0007 0.0004 0.0021 0.0010
1.084 1.004 0.618 2.989 1.424
0.010 0.009 0.006 0.027 0.013
Stack Conditions
End Time
Isokinetic Variance
Flue Gas Moisture, percent by volume
grains/dscf
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Average %CO2 by volume, dry basis
grams collected
CPMS Response, mA
lb/ton of clinker
Date
Start Time
Average Gas Temperature, °F
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Average Flue Pressure, in. Hg
Gas Sample Volume, dscf
Filterable Particulate Matter (Method 5)
lb/hr
grains/acf
Ash Grove Cememnt Company
Leamington Cement Plant
Main Kiln Stack
Average Gas Velocity, ft/sec
Source Condition
5
Clinker Production Rate,
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Client:
Facility:
Test Location:
Test Method:
Mill Off Mill Off Mill Off
6/12/24 6/12/24 6/12/24
5:55 8:20 10:55
7:58 10:23 13:55
Run 1 Run 2 Run 3 Average
157.7 163.1 163.6 161.5
10.3% 10.3% 11.9% 10.8%
24.99 24.99 24.99 24.99
93.64 93.945 93.581 93.722
65.547 66.420 66.484 66.150
18,045 18,285 18,303 18,211
11,563 11,609 11,403 11,525
12,884 12,943 12,945 12,924
7.6 6.7 6.7 7.0
16.5 16.9 16.9 16.8
100.3 100.2 101.6 100.7
ton/hr 118.4 115.3 115.9 116.5
7.0 8.4 7.4 7.6
0.03786 0.03877 0.04060 0.03908
0.0040 0.0040 0.0042 0.0041
0.0062 0.0064 0.0067 0.0064
0.618 0.634 0.654 0.635
0.005 0.005 0.006 0.005
Stack Conditions
End Time
Isokinetic Variance
Flue Gas Moisture, percent by volume
grains/dscf
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Average %CO2 by volume, dry basis
grams collected
CPMS Response, mA
lb/ton of clinker
Date
Start Time
Average Gas Temperature, °F
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Average Flue Pressure, in. Hg
Gas Sample Volume, dscf
Filterable Particulate Matter (Method 5)
lb/hr
grains/acf
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
Average Gas Velocity, ft/sec
Source Condition
5
Clinker Production Rate,
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Client:
Facility:
Test Location:
Test Method:
MILL ON MILL ON MILL ON SPIKED
6/13/24 6/13/24 6/13/24 6/13/24
7:30 9:45 12:10 14:30
9:33 11:48 13:55 16:35
Run 1 Run 2 Run 3 Run 4 Average
163.3 163.0 164.0 164.1 163.6
9.1% 8.6% 8.5% 8.6% 8.7%
25.04 25.04 25.04 25.04 25.04
93.118 95.05 94.693 94.632 94.373
65.469 65.635 65.493 65.554 65.538
18,023 18,069 18,030 18,047 18,042
11,617 11,721 11,679 11,675 11,673
12,780 12,818 12,770 12,779 12,787
7.6 6.7 6.7 6.2 6.8
16.5 16.9 16.9 16.9 16.8
99.3 100.4 100.4 100.4 100.1
ton/hr 107.8 108.8 108.8 108.8 108.6
10.3 10.2 10.8 23.5 13.7
0.03895 0.03909 0.02638 0.05039 0.03870
0.0042 0.0041 0.0028 0.0053 0.0041
0.0065 0.0063 0.0043 0.0082 0.0063
0.643 0.638 0.430 0.822 0.633
0.006 0.006 0.004 0.008 0.006
Clinker Production Rate,
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
Average Gas Velocity, ft/sec
Source Condition
5
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Average Flue Pressure, in. Hg
Gas Sample Volume, dscf
Filterable Particulate Matter (Method 5)
lb/hr
grains/acf
Date
Start Time
Average Gas Temperature, °F
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Average %CO2 by volume, dry basis
grams collected
CPMS Response, mA
lb/ton of clinker
grains/dscf
Stack Conditions
End Time
Isokinetic Variance
Flue Gas Moisture, percent by volume
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Client:
Facility:
Test Location:
Test Method:
Mill On Mill On Mill On
6/11/24 6/11/24 6/11/24
8:10 11:35 15:00
11:19 14:44 18:09
Run 1 Run 2 Run 3 Average
231.3 233.5 234.8 233.2
14.0% 14.0% 14.1% 14.0%
25.05 25.05 25.05 25.05
134.034 133.850 133.512 133.799
53.703 53.607 53.562 53.624
306,214 305,666 305,411 305,764
168,324 167,496 166,976 167,599
195,769 194,808 194,296 194,958
14.6 16.1 16.3 15.7
12.0 11.7 11.6 11.8
101.2 101.6 101.7 101.5
227.0 227.5 227.4 227.3
≤0.03 ≤0.04 ≤0.03 ≤0.03
≤1.20E-03 ≤1.90E-03 ≤1.60E-03 ≤1.57E-03
ng/dscm TEQ @ 7% O2 Dry ≤1.87E-03 ≤2.87E-03 ≤2.39E-03 ≤2.38E-03
PCDD/PCDF Emissions
ng/dscm
Gas Sample Volume, dscf
Average Gas Velocity, ft/sec
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Baghouse Inlet Temperature, °F
ng/dscm TEQ
Average Flue Pressure, in. Hg
Isokinetic Variance
End Time
Stack Conditions
Average %CO2 by volume, dry basis
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Flue Gas Moisture, percent by volume
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
23
Source Condition
Date
Start Time
Average Gas Temperature, °F
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Client:
Facility:
Test Location:
Test Method:
Mill Off Mill Off Mill Off
6/12/24 6/12/24 6/12/24
5:55 9:20 12:45
9:04 12:29 15:54
Run 1 Run 2 Run 3 Average
344.1 382.8 385.4 370.8
14.6% 14.6% 14.5% 14.6%
24.98 24.79 24.79 24.85
114.060 103.668 104.610 107.446
53.357 51.664 52.231 52.417
304,240 294,586 297,821 298,882
142,496 130,650 131,811 134,986
166,775 152,910 154,101 157,929
13.7 13.6 13.9 13.7
10.2 10.4 10.9 10.5
102.5 101.6 101.6 101.9
388.9 390.6 390.2 389.9
≤24.91 ≤29.51 ≤32.60 ≤29.01
≤6.98E-02 ≤9.42E-02 ≤1.01E-01 ≤8.82E-02
ng/dscm TEQ @ 7% O2 Dry ≤9.07E-02 ≤1.25E-01 ≤1.40E-01 ≤1.18E-01
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
23
Source Condition
Date
Start Time
Average Gas Temperature, °F
Average Flue Pressure, in. Hg
Isokinetic Variance
End Time
Stack Conditions
Average %CO2 by volume, dry basis
Average %O2 by volume, dry basis
Gas Volumetric Flow Rate, scfm
Flue Gas Moisture, percent by volume
PCDD/PCDF Emissions
ng/dscm
Gas Sample Volume, dscf
Average Gas Velocity, ft/sec
Gas Volumetric Flow Rate, acfm
Gas Volumetric Flow Rate, dscfm
Baghouse Inlet Temperature, °F
ng/dscm TEQ
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Test
No. Date
Start
Time
End
Time
CO2 %
(dry)
O2 %
(dry)
Moisture,
%
THC ppm
as C3H8
(wet)
THC
ppmvd @
7% O2
1 06/13/24 7:30 8:29 5.9 17.0 9.1 3.3 12.9
2 06/13/24 9:45 10:44 6.1 16.9 8.6 3.7 14.1
3 06/13/24 12:10 13:09 6.2 16.9 8.5 4.1 15.6
6.1 16.9 8.7 3.7 14.2
Ash Grove Cement Company
Leamington Plant
Coal Mill
THC Summary
Average
Test No. Date Start Time End Time
Vm (standard L)ng detected ppb ug/dscm ug/wscm
lb/MM tons
of clinker
1A 48.921 43.9 0.108 0.897 0.816 0.331
1B 47.310 38.4 0.097 0.812 0.738 0.300
41.2 0.102 0.855 0.777 0.316
2A 48.647 43.0 0.106 0.884 0.808 0.337
2B 49.850 33.3 0.080 0.668 0.611 0.255
38.2 0.093 0.776 0.709 0.296
3A 48.349 48.3 0.120 0.999 0.914 0.378
3B 46.726 39.4 0.101 0.843 0.772 0.319
43.9 0.110 0.921 0.843 0.348
41.05 0.10 0.85 0.78 0.320
Method 30B (Sorbent Trap) Mercury Test Results Summary
Ash Grove Cement Company
Leamington Plant
6/12/2024 7:30 8:30
Coal Mill Stack
Average
6/12/2024 9:45 10:45
Average
6/12/2024 12:10 13:10
Average
Overall Average
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 12 of 315 ©Mostardi Platt

4.0 CERTIFICATION
Mostardi Platt is pleased to have been of service to Ash Grove Cement Company. If you have any questions regarding this test report, please do not hesitate to contact us at 630-993-2100.
As project 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, and the test program was performed in accordance with the methods specified in this test report.
MOSTARDI PLATT
_________________________________ Program Manager Michal Lipinski _________________________________ Quality Assurance Richard J. Sollars II
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 13 of 315 ©Mostardi Platt

APPENDICES

Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 14 of 315 ©Mostardi Platt
Appendix A - Operating Data
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 15 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 05:55 386.0
06/12/2024 05:56 385.2
06/12/2024 05:57 384.8
06/12/2024 05:58 384.0
06/12/2024 05:59 383.2
06/12/2024 06:00 381.8
06/12/2024 06:01 380.8
06/12/2024 06:02 380.0
06/12/2024 06:03 379.7
06/12/2024 06:04 379.0
06/12/2024 06:05 379.0
06/12/2024 06:06 379.0
06/12/2024 06:07 379.0
06/12/2024 06:08 379.0
06/12/2024 06:09 379.0
06/12/2024 06:10 379.0
06/12/2024 06:11 380.0
06/12/2024 06:12 380.0
06/12/2024 06:13 380.0
06/12/2024 06:14 380.0
06/12/2024 06:15 379.2
06/12/2024 06:16 379.0
06/12/2024 06:17 379.8
06/12/2024 06:18 380.0
06/12/2024 06:19 380.0
06/12/2024 06:20 380.0
06/12/2024 06:21 380.8
06/12/2024 06:22 381.0
06/12/2024 06:23 381.3
06/12/2024 06:24 382.0
06/12/2024 06:25 382.7
06/12/2024 06:26 383.0
06/12/2024 06:27 383.0
06/12/2024 06:28 383.5
06/12/2024 06:29 384.0
06/12/2024 06:30 383.5
06/12/2024 06:31 383.0
06/12/2024 06:32 382.0
06/12/2024 06:33 381.7
06/12/2024 06:34 381.0
06/12/2024 06:35 380.5
06/12/2024 06:36 380.0
06/12/2024 06:37 380.0
06/12/2024 06:38 380.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 16 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 06:39 380.0
06/12/2024 06:40 380.0
06/12/2024 06:41 380.3
06/12/2024 06:42 381.2
06/12/2024 06:43 382.2
06/12/2024 06:44 383.3
06/12/2024 06:45 384.5
06/12/2024 06:46 385.5
06/12/2024 06:47 386.7
06/12/2024 06:48 388.3
06/12/2024 06:49 389.5
06/12/2024 06:50 390.0
06/12/2024 06:51 390.8
06/12/2024 06:52 391.5
06/12/2024 06:53 392.0
06/12/2024 06:54 392.0
06/12/2024 06:55 392.0
06/12/2024 06:56 392.0
06/12/2024 06:57 392.2
06/12/2024 06:58 393.0
06/12/2024 06:59 393.0
06/12/2024 07:00 393.0
06/12/2024 07:01 393.0
06/12/2024 07:02 393.0
06/12/2024 07:03 393.0
06/12/2024 07:04 393.0
06/12/2024 07:05 393.0
06/12/2024 07:06 393.0
06/12/2024 07:07 393.0
06/12/2024 07:08 393.0
06/12/2024 07:09 393.0
06/12/2024 07:10 393.0
06/12/2024 07:11 393.0
06/12/2024 07:12 392.8
06/12/2024 07:13 392.0
06/12/2024 07:14 392.0
06/12/2024 07:15 392.0
06/12/2024 07:16 392.0
06/12/2024 07:17 392.0
06/12/2024 07:18 392.0
06/12/2024 07:19 392.0
06/12/2024 07:20 392.7
06/12/2024 07:21 393.0
06/12/2024 07:22 393.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 17 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 07:23 393.7
06/12/2024 07:24 394.0
06/12/2024 07:25 394.0
06/12/2024 07:26 394.0
06/12/2024 07:27 394.0
06/12/2024 07:28 393.2
06/12/2024 07:29 393.0
06/12/2024 07:30 394.0
06/12/2024 07:31 394.0
06/12/2024 07:32 394.7
06/12/2024 07:33 395.0
06/12/2024 07:34 395.0
06/12/2024 07:35 394.3
06/12/2024 07:36 394.3
06/12/2024 07:37 395.0
06/12/2024 07:38 395.0
06/12/2024 07:39 395.0
06/12/2024 07:40 395.0
06/12/2024 07:41 395.0
06/12/2024 07:42 395.0
06/12/2024 07:43 395.0
06/12/2024 07:44 395.0
06/12/2024 07:45 395.0
06/12/2024 07:46 395.0
06/12/2024 07:47 395.0
06/12/2024 07:48 396.0
06/12/2024 07:49 396.0
06/12/2024 07:50 396.0
06/12/2024 07:51 396.0
06/12/2024 07:52 395.5
06/12/2024 07:53 395.0
06/12/2024 07:54 393.8
06/12/2024 07:55 392.7
06/12/2024 07:56 391.5
06/12/2024 07:57 390.3
06/12/2024 07:58 389.5
06/12/2024 07:59 389.0
06/12/2024 08:00 388.3
06/12/2024 08:01 388.0
06/12/2024 08:02 388.0
06/12/2024 08:03 388.0
06/12/2024 08:04 388.0
06/12/2024 08:05 388.0
06/12/2024 08:06 388.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 18 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 08:07 388.0
06/12/2024 08:08 388.0
06/12/2024 08:09 388.0
06/12/2024 08:10 388.0
06/12/2024 08:11 388.0
06/12/2024 08:12 388.0
06/12/2024 08:13 388.0
06/12/2024 08:14 388.0
06/12/2024 08:15 388.7
06/12/2024 08:16 389.0
06/12/2024 08:17 389.0
06/12/2024 08:18 389.0
06/12/2024 08:19 390.0
06/12/2024 08:20 390.0
06/12/2024 08:21 390.8
06/12/2024 08:22 390.2
06/12/2024 08:23 390.8
06/12/2024 08:24 391.0
06/12/2024 08:25 391.0
06/12/2024 08:26 391.0
06/12/2024 08:27 391.0
06/12/2024 08:28 391.0
06/12/2024 08:29 391.7
06/12/2024 08:30 392.0
06/12/2024 08:31 392.0
06/12/2024 08:32 391.3
06/12/2024 08:33 391.0
06/12/2024 08:34 391.0
06/12/2024 08:35 391.0
06/12/2024 08:36 391.0
06/12/2024 08:37 391.0
06/12/2024 08:38 391.0
06/12/2024 08:39 391.0
06/12/2024 08:40 391.0
06/12/2024 08:41 391.0
06/12/2024 08:42 391.0
06/12/2024 08:43 391.0
06/12/2024 08:44 391.0
06/12/2024 08:45 391.0
06/12/2024 08:46 390.5
06/12/2024 08:47 390.0
06/12/2024 08:48 390.0
06/12/2024 08:49 390.0
06/12/2024 08:50 390.5
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 19 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 08:51 391.0
06/12/2024 08:52 391.0
06/12/2024 08:53 391.0
06/12/2024 08:54 391.0
06/12/2024 08:55 391.0
06/12/2024 08:56 391.0
06/12/2024 08:57 391.0
06/12/2024 08:58 391.0
06/12/2024 08:59 391.0
06/12/2024 09:00 391.2
06/12/2024 09:01 391.0
06/12/2024 09:02 391.0
06/12/2024 09:03 391.0
06/12/2024 09:04 391.0
Average
Max
Min
Count
388.9
396.0
379.0
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 20 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 09:20 391.0
06/12/2024 09:21 391.2
06/12/2024 09:22 392.0
06/12/2024 09:23 392.0
06/12/2024 09:24 392.0
06/12/2024 09:25 392.0
06/12/2024 09:26 392.2
06/12/2024 09:27 392.0
06/12/2024 09:28 392.0
06/12/2024 09:29 392.0
06/12/2024 09:30 392.0
06/12/2024 09:31 392.0
06/12/2024 09:32 392.0
06/12/2024 09:33 392.0
06/12/2024 09:34 392.0
06/12/2024 09:35 392.0
06/12/2024 09:36 392.0
06/12/2024 09:37 392.0
06/12/2024 09:38 392.0
06/12/2024 09:39 392.0
06/12/2024 09:40 392.0
06/12/2024 09:41 392.0
06/12/2024 09:42 391.7
06/12/2024 09:43 392.0
06/12/2024 09:44 392.0
06/12/2024 09:45 392.0
06/12/2024 09:46 392.0
06/12/2024 09:47 392.0
06/12/2024 09:48 392.0
06/12/2024 09:49 392.0
06/12/2024 09:50 392.0
06/12/2024 09:51 392.0
06/12/2024 09:52 392.0
06/12/2024 09:53 392.0
06/12/2024 09:54 392.5
06/12/2024 09:55 393.0
06/12/2024 09:56 393.0
06/12/2024 09:57 393.0
06/12/2024 09:58 393.0
06/12/2024 09:59 393.0
06/12/2024 10:00 393.0
06/12/2024 10:01 392.8
06/12/2024 10:02 392.0
06/12/2024 10:03 392.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 21 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 10:04 391.0
06/12/2024 10:05 391.0
06/12/2024 10:06 390.3
06/12/2024 10:07 390.0
06/12/2024 10:08 390.0
06/12/2024 10:09 390.0
06/12/2024 10:10 390.0
06/12/2024 10:11 390.0
06/12/2024 10:12 389.5
06/12/2024 10:13 389.0
06/12/2024 10:14 389.0
06/12/2024 10:15 389.0
06/12/2024 10:16 389.0
06/12/2024 10:17 389.0
06/12/2024 10:18 389.0
06/12/2024 10:19 388.5
06/12/2024 10:20 388.0
06/12/2024 10:21 388.0
06/12/2024 10:22 388.0
06/12/2024 10:23 388.0
06/12/2024 10:24 388.0
06/12/2024 10:25 388.0
06/12/2024 10:26 388.0
06/12/2024 10:27 388.8
06/12/2024 10:28 389.0
06/12/2024 10:29 389.0
06/12/2024 10:30 389.2
06/12/2024 10:31 390.0
06/12/2024 10:32 390.7
06/12/2024 10:33 391.5
06/12/2024 10:34 392.2
06/12/2024 10:35 393.0
06/12/2024 10:36 393.0
06/12/2024 10:37 394.0
06/12/2024 10:38 394.0
06/12/2024 10:39 394.0
06/12/2024 10:40 394.0
06/12/2024 10:41 394.0
06/12/2024 10:42 394.0
06/12/2024 10:43 394.0
06/12/2024 10:44 393.2
06/12/2024 10:45 393.0
06/12/2024 10:46 392.2
06/12/2024 10:47 391.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 22 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 10:48 390.2
06/12/2024 10:49 389.2
06/12/2024 10:50 389.0
06/12/2024 10:51 389.0
06/12/2024 10:52 388.5
06/12/2024 10:53 388.0
06/12/2024 10:54 388.0
06/12/2024 10:55 388.0
06/12/2024 10:56 388.0
06/12/2024 10:57 388.0
06/12/2024 10:58 388.0
06/12/2024 10:59 388.0
06/12/2024 11:00 388.0
06/12/2024 11:01 388.0
06/12/2024 11:02 387.5
06/12/2024 11:03 387.3
06/12/2024 11:04 388.0
06/12/2024 11:05 388.3
06/12/2024 11:06 389.0
06/12/2024 11:07 389.0
06/12/2024 11:08 389.0
06/12/2024 11:09 389.0
06/12/2024 11:10 388.7
06/12/2024 11:11 388.0
06/12/2024 11:12 387.8
06/12/2024 11:13 387.3
06/12/2024 11:14 388.0
06/12/2024 11:15 388.0
06/12/2024 11:16 388.0
06/12/2024 11:17 388.0
06/12/2024 11:18 388.2
06/12/2024 11:19 389.0
06/12/2024 11:20 389.0
06/12/2024 11:21 389.0
06/12/2024 11:22 389.8
06/12/2024 11:23 390.0
06/12/2024 11:24 390.8
06/12/2024 11:25 391.0
06/12/2024 11:26 391.3
06/12/2024 11:27 392.0
06/12/2024 11:28 392.0
06/12/2024 11:29 392.0
06/12/2024 11:30 392.3
06/12/2024 11:31 393.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 23 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 11:32 393.0
06/12/2024 11:33 393.0
06/12/2024 11:34 393.0
06/12/2024 11:35 394.0
06/12/2024 11:36 394.0
06/12/2024 11:37 394.0
06/12/2024 11:38 393.7
06/12/2024 11:39 393.0
06/12/2024 11:40 393.0
06/12/2024 11:41 392.7
06/12/2024 11:42 392.0
06/12/2024 11:43 392.0
06/12/2024 11:44 391.3
06/12/2024 11:45 391.0
06/12/2024 11:46 391.0
06/12/2024 11:47 390.8
06/12/2024 11:48 390.0
06/12/2024 11:49 390.0
06/12/2024 11:50 390.2
06/12/2024 11:51 390.5
06/12/2024 11:52 390.0
06/12/2024 11:53 390.0
06/12/2024 11:54 390.3
06/12/2024 11:55 391.0
06/12/2024 11:56 391.0
06/12/2024 11:57 391.0
06/12/2024 11:58 391.0
06/12/2024 11:59 391.0
06/12/2024 12:00 391.0
06/12/2024 12:01 391.0
06/12/2024 12:02 391.0
06/12/2024 12:03 391.0
06/12/2024 12:04 390.3
06/12/2024 12:05 390.0
06/12/2024 12:06 390.0
06/12/2024 12:07 390.0
06/12/2024 12:08 390.0
06/12/2024 12:09 390.0
06/12/2024 12:10 390.0
06/12/2024 12:11 390.0
06/12/2024 12:12 389.7
06/12/2024 12:13 390.0
06/12/2024 12:14 390.0
06/12/2024 12:15 390.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 24 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 12:16 389.8
06/12/2024 12:17 389.0
06/12/2024 12:18 389.0
06/12/2024 12:19 389.0
06/12/2024 12:20 389.0
06/12/2024 12:21 388.5
06/12/2024 12:22 388.0
06/12/2024 12:23 388.0
06/12/2024 12:24 388.0
06/12/2024 12:25 388.0
06/12/2024 12:26 388.0
06/12/2024 12:27 388.0
06/12/2024 12:28 388.0
06/12/2024 12:29 388.0
Average
Max
Min
Count
390.6
394.0
387.3
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 25 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 12:45 390.0
06/12/2024 12:46 390.0
06/12/2024 12:47 390.5
06/12/2024 12:48 391.0
06/12/2024 12:49 391.0
06/12/2024 12:50 391.0
06/12/2024 12:51 390.3
06/12/2024 12:52 390.0
06/12/2024 12:53 390.0
06/12/2024 12:54 390.0
06/12/2024 12:55 390.0
06/12/2024 12:56 390.0
06/12/2024 12:57 390.0
06/12/2024 12:58 390.0
06/12/2024 12:59 390.0
06/12/2024 13:00 390.0
06/12/2024 13:01 390.0
06/12/2024 13:02 390.0
06/12/2024 13:03 390.0
06/12/2024 13:04 390.0
06/12/2024 13:05 390.0
06/12/2024 13:06 390.0
06/12/2024 13:07 390.0
06/12/2024 13:08 390.0
06/12/2024 13:09 390.0
06/12/2024 13:10 390.0
06/12/2024 13:11 390.0
06/12/2024 13:12 390.0
06/12/2024 13:13 390.2
06/12/2024 13:14 391.0
06/12/2024 13:15 391.0
06/12/2024 13:16 391.0
06/12/2024 13:17 391.0
06/12/2024 13:18 390.0
06/12/2024 13:19 390.0
06/12/2024 13:20 389.2
06/12/2024 13:21 389.0
06/12/2024 13:22 389.0
06/12/2024 13:23 389.0
06/12/2024 13:24 389.7
06/12/2024 13:25 390.0
06/12/2024 13:26 390.0
06/12/2024 13:27 390.0
06/12/2024 13:28 389.3
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 26 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 13:29 389.0
06/12/2024 13:30 389.0
06/12/2024 13:31 389.0
06/12/2024 13:32 388.8
06/12/2024 13:33 388.0
06/12/2024 13:34 388.0
06/12/2024 13:35 388.5
06/12/2024 13:36 389.0
06/12/2024 13:37 389.0
06/12/2024 13:38 389.5
06/12/2024 13:39 390.0
06/12/2024 13:40 390.0
06/12/2024 13:41 390.0
06/12/2024 13:42 390.0
06/12/2024 13:43 390.0
06/12/2024 13:44 390.0
06/12/2024 13:45 390.0
06/12/2024 13:46 390.0
06/12/2024 13:47 390.0
06/12/2024 13:48 390.0
06/12/2024 13:49 390.0
06/12/2024 13:50 389.0
06/12/2024 13:51 389.8
06/12/2024 13:52 390.0
06/12/2024 13:53 390.2
06/12/2024 13:54 391.0
06/12/2024 13:55 391.0
06/12/2024 13:56 390.2
06/12/2024 13:57 390.0
06/12/2024 13:58 390.0
06/12/2024 13:59 390.7
06/12/2024 14:00 391.0
06/12/2024 14:01 391.0
06/12/2024 14:02 391.0
06/12/2024 14:03 391.0
06/12/2024 14:04 391.0
06/12/2024 14:05 391.0
06/12/2024 14:06 391.0
06/12/2024 14:07 391.0
06/12/2024 14:08 391.0
06/12/2024 14:09 391.0
06/12/2024 14:10 390.7
06/12/2024 14:11 390.0
06/12/2024 14:12 390.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 27 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 14:13 390.0
06/12/2024 14:14 390.0
06/12/2024 14:15 390.0
06/12/2024 14:16 390.0
06/12/2024 14:17 390.0
06/12/2024 14:18 389.3
06/12/2024 14:19 389.0
06/12/2024 14:20 389.0
06/12/2024 14:21 389.0
06/12/2024 14:22 389.0
06/12/2024 14:23 389.3
06/12/2024 14:24 390.0
06/12/2024 14:25 390.5
06/12/2024 14:26 391.0
06/12/2024 14:27 391.0
06/12/2024 14:28 392.0
06/12/2024 14:29 392.0
06/12/2024 14:30 392.3
06/12/2024 14:31 393.0
06/12/2024 14:32 393.0
06/12/2024 14:33 393.0
06/12/2024 14:34 393.0
06/12/2024 14:35 393.0
06/12/2024 14:36 393.0
06/12/2024 14:37 393.0
06/12/2024 14:38 393.0
06/12/2024 14:39 392.7
06/12/2024 14:40 392.2
06/12/2024 14:41 392.2
06/12/2024 14:42 392.0
06/12/2024 14:43 391.0
06/12/2024 14:44 390.7
06/12/2024 14:45 390.0
06/12/2024 14:46 390.0
06/12/2024 14:47 390.0
06/12/2024 14:48 389.2
06/12/2024 14:49 389.0
06/12/2024 14:50 389.0
06/12/2024 14:51 389.0
06/12/2024 14:52 389.0
06/12/2024 14:53 388.2
06/12/2024 14:54 388.0
06/12/2024 14:55 388.0
06/12/2024 14:56 388.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 28 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 14:57 388.0
06/12/2024 14:58 388.0
06/12/2024 14:59 388.0
06/12/2024 15:00 388.0
06/12/2024 15:01 388.8
06/12/2024 15:02 389.0
06/12/2024 15:03 389.0
06/12/2024 15:04 390.0
06/12/2024 15:05 390.0
06/12/2024 15:06 390.0
06/12/2024 15:07 390.0
06/12/2024 15:08 390.0
06/12/2024 15:09 390.0
06/12/2024 15:10 390.2
06/12/2024 15:11 391.0
06/12/2024 15:12 391.0
06/12/2024 15:13 391.0
06/12/2024 15:14 392.0
06/12/2024 15:15 392.0
06/12/2024 15:16 392.0
06/12/2024 15:17 391.3
06/12/2024 15:18 391.0
06/12/2024 15:19 391.0
06/12/2024 15:20 391.2
06/12/2024 15:21 392.0
06/12/2024 15:22 391.7
06/12/2024 15:23 391.0
06/12/2024 15:24 391.0
06/12/2024 15:25 391.0
06/12/2024 15:26 391.0
06/12/2024 15:27 391.0
06/12/2024 15:28 390.0
06/12/2024 15:29 390.0
06/12/2024 15:30 389.5
06/12/2024 15:31 389.0
06/12/2024 15:32 389.0
06/12/2024 15:33 389.0
06/12/2024 15:34 389.7
06/12/2024 15:35 390.0
06/12/2024 15:36 390.0
06/12/2024 15:37 390.0
06/12/2024 15:38 390.0
06/12/2024 15:39 390.0
06/12/2024 15:40 390.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 29 of 315 ©Mostardi Platt
Date/Time
KILN:
IN_TMP_BA
G_MILL_OFF
(DEGF)
Raw
Value
06/12/2024 15:41 390.2
06/12/2024 15:42 390.0
06/12/2024 15:43 390.0
06/12/2024 15:44 390.0
06/12/2024 15:45 390.0
06/12/2024 15:46 390.0
06/12/2024 15:47 390.0
06/12/2024 15:48 390.0
06/12/2024 15:49 390.3
06/12/2024 15:50 391.0
06/12/2024 15:51 391.0
06/12/2024 15:52 391.0
06/12/2024 15:53 391.0
06/12/2024 15:54 391.0
Average
Max
Min
Count
390.2
393.0
388.0
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 30 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 08:10 227.2
06/11/2024 08:11 226.3
06/11/2024 08:12 225.2
06/11/2024 08:13 225.0
06/11/2024 08:14 225.0
06/11/2024 08:15 224.0
06/11/2024 08:16 224.0
06/11/2024 08:17 224.7
06/11/2024 08:18 225.0
06/11/2024 08:19 224.7
06/11/2024 08:20 225.2
06/11/2024 08:21 226.0
06/11/2024 08:22 226.8
06/11/2024 08:23 227.2
06/11/2024 08:24 228.0
06/11/2024 08:25 228.0
06/11/2024 08:26 228.0
06/11/2024 08:27 228.0
06/11/2024 08:28 228.0
06/11/2024 08:29 227.7
06/11/2024 08:30 227.0
06/11/2024 08:31 227.0
06/11/2024 08:32 227.0
06/11/2024 08:33 227.0
06/11/2024 08:34 227.0
06/11/2024 08:35 227.0
06/11/2024 08:36 227.0
06/11/2024 08:37 226.0
06/11/2024 08:38 225.7
06/11/2024 08:39 226.0
06/11/2024 08:40 226.0
06/11/2024 08:41 226.0
06/11/2024 08:42 226.0
06/11/2024 08:43 226.0
06/11/2024 08:44 226.0
06/11/2024 08:45 226.0
06/11/2024 08:46 226.0
06/11/2024 08:47 226.0
06/11/2024 08:48 226.0
06/11/2024 08:49 225.8
06/11/2024 08:50 225.0
06/11/2024 08:51 225.0
06/11/2024 08:52 225.0
06/11/2024 08:53 224.7
06/11/2024 08:54 224.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 31 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 08:55 224.0
06/11/2024 08:56 224.0
06/11/2024 08:57 224.3
06/11/2024 08:58 225.0
06/11/2024 08:59 225.0
06/11/2024 09:00 225.7
06/11/2024 09:01 225.0
06/11/2024 09:02 225.0
06/11/2024 09:03 225.0
06/11/2024 09:04 225.7
06/11/2024 09:05 226.0
06/11/2024 09:06 226.0
06/11/2024 09:07 226.0
06/11/2024 09:08 226.0
06/11/2024 09:09 226.0
06/11/2024 09:10 225.7
06/11/2024 09:11 225.0
06/11/2024 09:12 225.0
06/11/2024 09:13 225.0
06/11/2024 09:14 225.0
06/11/2024 09:15 225.0
06/11/2024 09:16 225.0
06/11/2024 09:17 225.0
06/11/2024 09:18 225.0
06/11/2024 09:19 225.0
06/11/2024 09:20 225.0
06/11/2024 09:21 225.0
06/11/2024 09:22 225.0
06/11/2024 09:23 226.0
06/11/2024 09:24 226.8
06/11/2024 09:25 227.0
06/11/2024 09:26 227.0
06/11/2024 09:27 227.0
06/11/2024 09:28 228.0
06/11/2024 09:29 227.8
06/11/2024 09:30 227.0
06/11/2024 09:31 227.0
06/11/2024 09:32 226.2
06/11/2024 09:33 226.0
06/11/2024 09:34 226.0
06/11/2024 09:35 225.5
06/11/2024 09:36 225.0
06/11/2024 09:37 225.0
06/11/2024 09:38 225.7
06/11/2024 09:39 226.3
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 32 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 09:40 227.2
06/11/2024 09:41 228.0
06/11/2024 09:42 228.2
06/11/2024 09:43 229.0
06/11/2024 09:44 229.0
06/11/2024 09:45 229.0
06/11/2024 09:46 229.0
06/11/2024 09:47 229.0
06/11/2024 09:48 229.0
06/11/2024 09:49 229.0
06/11/2024 09:50 229.7
06/11/2024 09:51 230.0
06/11/2024 09:52 229.2
06/11/2024 09:53 229.0
06/11/2024 09:54 228.2
06/11/2024 09:55 228.0
06/11/2024 09:56 228.0
06/11/2024 09:57 227.3
06/11/2024 09:58 227.0
06/11/2024 09:59 228.0
06/11/2024 10:00 228.0
06/11/2024 10:01 228.0
06/11/2024 10:02 228.0
06/11/2024 10:03 228.0
06/11/2024 10:04 227.3
06/11/2024 10:05 227.0
06/11/2024 10:06 227.0
06/11/2024 10:07 227.3
06/11/2024 10:08 228.0
06/11/2024 10:09 228.2
06/11/2024 10:10 229.0
06/11/2024 10:11 229.0
06/11/2024 10:12 229.0
06/11/2024 10:13 229.0
06/11/2024 10:14 229.0
06/11/2024 10:15 229.0
06/11/2024 10:16 229.0
06/11/2024 10:17 229.0
06/11/2024 10:18 229.0
06/11/2024 10:19 229.0
06/11/2024 10:20 229.0
06/11/2024 10:21 229.0
06/11/2024 10:22 229.0
06/11/2024 10:23 229.0
06/11/2024 10:24 229.3
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 33 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 10:25 230.0
06/11/2024 10:26 230.0
06/11/2024 10:27 230.0
06/11/2024 10:28 230.0
06/11/2024 10:29 230.0
06/11/2024 10:30 230.0
06/11/2024 10:31 230.0
06/11/2024 10:32 230.0
06/11/2024 10:33 230.0
06/11/2024 10:34 230.0
06/11/2024 10:35 229.5
06/11/2024 10:36 229.0
06/11/2024 10:37 228.2
06/11/2024 10:38 228.0
06/11/2024 10:39 227.3
06/11/2024 10:40 227.0
06/11/2024 10:41 226.2
06/11/2024 10:42 226.8
06/11/2024 10:43 227.0
06/11/2024 10:44 227.0
06/11/2024 10:45 227.0
06/11/2024 10:46 227.0
06/11/2024 10:47 227.0
06/11/2024 10:48 227.0
06/11/2024 10:49 227.0
06/11/2024 10:50 227.0
06/11/2024 10:51 227.0
06/11/2024 10:52 227.0
06/11/2024 10:53 226.0
06/11/2024 10:54 226.0
06/11/2024 10:55 226.0
06/11/2024 10:56 226.0
06/11/2024 10:57 226.2
06/11/2024 10:58 227.0
06/11/2024 10:59 227.0
06/11/2024 11:00 227.0
06/11/2024 11:01 227.0
06/11/2024 11:02 227.0
06/11/2024 11:03 227.8
06/11/2024 11:04 228.0
06/11/2024 11:05 228.0
06/11/2024 11:06 228.0
06/11/2024 11:07 227.0
06/11/2024 11:08 227.0
06/11/2024 11:09 227.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 34 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 11:10 226.0
06/11/2024 11:11 226.0
06/11/2024 11:12 226.0
06/11/2024 11:13 226.0
06/11/2024 11:14 226.0
06/11/2024 11:15 226.0
06/11/2024 11:16 226.0
06/11/2024 11:17 226.0
06/11/2024 11:18 226.8
06/11/2024 11:19 227.0
Average
Max
Min
Count
227.0
230.0
224.0
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 35 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 11:35 228.0
06/11/2024 11:36 228.7
06/11/2024 11:37 229.0
06/11/2024 11:38 228.3
06/11/2024 11:39 228.0
06/11/2024 11:40 228.0
06/11/2024 11:41 228.0
06/11/2024 11:42 228.0
06/11/2024 11:43 228.0
06/11/2024 11:44 228.0
06/11/2024 11:45 228.5
06/11/2024 11:46 229.0
06/11/2024 11:47 229.0
06/11/2024 11:48 228.8
06/11/2024 11:49 228.0
06/11/2024 11:50 228.0
06/11/2024 11:51 228.0
06/11/2024 11:52 228.0
06/11/2024 11:53 228.0
06/11/2024 11:54 228.0
06/11/2024 11:55 228.0
06/11/2024 11:56 228.0
06/11/2024 11:57 228.0
06/11/2024 11:58 228.0
06/11/2024 11:59 228.0
06/11/2024 12:00 228.0
06/11/2024 12:01 228.0
06/11/2024 12:02 228.0
06/11/2024 12:03 228.0
06/11/2024 12:04 228.0
06/11/2024 12:05 228.0
06/11/2024 12:06 228.0
06/11/2024 12:07 228.0
06/11/2024 12:08 228.0
06/11/2024 12:09 227.7
06/11/2024 12:10 227.0
06/11/2024 12:11 227.0
06/11/2024 12:12 227.0
06/11/2024 12:13 227.0
06/11/2024 12:14 227.0
06/11/2024 12:15 226.8
06/11/2024 12:16 226.0
06/11/2024 12:17 225.0
06/11/2024 12:18 225.8
06/11/2024 12:19 226.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 36 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 12:20 226.0
06/11/2024 12:21 227.0
06/11/2024 12:22 227.0
06/11/2024 12:23 227.0
06/11/2024 12:24 228.0
06/11/2024 12:25 228.0
06/11/2024 12:26 228.0
06/11/2024 12:27 228.0
06/11/2024 12:28 228.0
06/11/2024 12:29 227.5
06/11/2024 12:30 227.0
06/11/2024 12:31 226.0
06/11/2024 12:32 226.0
06/11/2024 12:33 226.0
06/11/2024 12:34 226.0
06/11/2024 12:35 226.0
06/11/2024 12:36 226.0
06/11/2024 12:37 226.0
06/11/2024 12:38 226.0
06/11/2024 12:39 226.0
06/11/2024 12:40 226.0
06/11/2024 12:41 226.0
06/11/2024 12:42 226.0
06/11/2024 12:43 225.5
06/11/2024 12:44 225.3
06/11/2024 12:45 226.0
06/11/2024 12:46 225.7
06/11/2024 12:47 226.0
06/11/2024 12:48 226.0
06/11/2024 12:49 226.0
06/11/2024 12:50 226.8
06/11/2024 12:51 227.0
06/11/2024 12:52 227.0
06/11/2024 12:53 227.0
06/11/2024 12:54 227.0
06/11/2024 12:55 227.0
06/11/2024 12:56 227.0
06/11/2024 12:57 227.8
06/11/2024 12:58 228.0
06/11/2024 12:59 229.0
06/11/2024 13:00 229.0
06/11/2024 13:01 229.0
06/11/2024 13:02 229.0
06/11/2024 13:03 229.0
06/11/2024 13:04 229.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 37 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 13:05 229.0
06/11/2024 13:06 229.0
06/11/2024 13:07 229.0
06/11/2024 13:08 229.0
06/11/2024 13:09 229.0
06/11/2024 13:10 229.0
06/11/2024 13:11 229.0
06/11/2024 13:12 229.0
06/11/2024 13:13 229.0
06/11/2024 13:14 229.0
06/11/2024 13:15 229.0
06/11/2024 13:16 229.0
06/11/2024 13:17 228.3
06/11/2024 13:18 228.0
06/11/2024 13:19 228.0
06/11/2024 13:20 228.0
06/11/2024 13:21 227.0
06/11/2024 13:22 227.0
06/11/2024 13:23 226.5
06/11/2024 13:24 226.0
06/11/2024 13:25 226.0
06/11/2024 13:26 226.0
06/11/2024 13:27 226.0
06/11/2024 13:28 226.0
06/11/2024 13:29 226.0
06/11/2024 13:30 226.0
06/11/2024 13:31 226.0
06/11/2024 13:32 226.0
06/11/2024 13:33 226.0
06/11/2024 13:34 226.0
06/11/2024 13:35 226.0
06/11/2024 13:36 226.0
06/11/2024 13:37 226.0
06/11/2024 13:38 226.5
06/11/2024 13:39 227.0
06/11/2024 13:40 227.0
06/11/2024 13:41 227.0
06/11/2024 13:42 227.0
06/11/2024 13:43 227.0
06/11/2024 13:44 227.0
06/11/2024 13:45 226.0
06/11/2024 13:46 225.7
06/11/2024 13:47 225.0
06/11/2024 13:48 225.0
06/11/2024 13:49 225.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 38 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 13:50 225.5
06/11/2024 13:51 226.0
06/11/2024 13:52 226.8
06/11/2024 13:53 227.8
06/11/2024 13:54 229.0
06/11/2024 13:55 230.0
06/11/2024 13:56 230.0
06/11/2024 13:57 230.0
06/11/2024 13:58 230.0
06/11/2024 13:59 230.3
06/11/2024 14:00 230.5
06/11/2024 14:01 230.0
06/11/2024 14:02 230.0
06/11/2024 14:03 230.0
06/11/2024 14:04 230.0
06/11/2024 14:05 230.0
06/11/2024 14:06 230.0
06/11/2024 14:07 230.0
06/11/2024 14:08 230.0
06/11/2024 14:09 229.8
06/11/2024 14:10 229.0
06/11/2024 14:11 228.2
06/11/2024 14:12 228.0
06/11/2024 14:13 228.5
06/11/2024 14:14 228.2
06/11/2024 14:15 228.0
06/11/2024 14:16 227.7
06/11/2024 14:17 227.0
06/11/2024 14:18 227.0
06/11/2024 14:19 227.0
06/11/2024 14:20 227.0
06/11/2024 14:21 227.0
06/11/2024 14:22 227.0
06/11/2024 14:23 227.0
06/11/2024 14:24 227.0
06/11/2024 14:25 227.0
06/11/2024 14:26 227.2
06/11/2024 14:27 227.5
06/11/2024 14:28 227.3
06/11/2024 14:29 228.0
06/11/2024 14:30 228.0
06/11/2024 14:31 228.0
06/11/2024 14:32 228.0
06/11/2024 14:33 228.0
06/11/2024 14:34 228.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 39 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 14:35 227.2
06/11/2024 14:36 226.8
06/11/2024 14:37 226.0
06/11/2024 14:38 226.0
06/11/2024 14:39 226.7
06/11/2024 14:40 226.0
06/11/2024 14:41 226.0
06/11/2024 14:42 226.0
06/11/2024 14:43 226.0
06/11/2024 14:44 226.0
Average
Max
Min
Count
227.5
230.5
225.0
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 40 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 15:00 228.8
06/11/2024 15:01 229.0
06/11/2024 15:02 229.0
06/11/2024 15:03 229.0
06/11/2024 15:04 229.0
06/11/2024 15:05 229.0
06/11/2024 15:06 229.0
06/11/2024 15:07 229.0
06/11/2024 15:08 229.0
06/11/2024 15:09 228.5
06/11/2024 15:10 228.8
06/11/2024 15:11 229.0
06/11/2024 15:12 229.0
06/11/2024 15:13 229.0
06/11/2024 15:14 229.0
06/11/2024 15:15 229.0
06/11/2024 15:16 229.0
06/11/2024 15:17 228.5
06/11/2024 15:18 228.0
06/11/2024 15:19 228.0
06/11/2024 15:20 227.2
06/11/2024 15:21 227.0
06/11/2024 15:22 227.0
06/11/2024 15:23 227.0
06/11/2024 15:24 227.0
06/11/2024 15:25 227.0
06/11/2024 15:26 226.8
06/11/2024 15:27 226.0
06/11/2024 15:28 226.0
06/11/2024 15:29 226.0
06/11/2024 15:30 226.0
06/11/2024 15:31 226.0
06/11/2024 15:32 225.8
06/11/2024 15:33 225.0
06/11/2024 15:34 225.0
06/11/2024 15:35 225.0
06/11/2024 15:36 225.3
06/11/2024 15:37 226.2
06/11/2024 15:38 227.0
06/11/2024 15:39 227.0
06/11/2024 15:40 226.7
06/11/2024 15:41 226.0
06/11/2024 15:42 226.0
06/11/2024 15:43 226.0
06/11/2024 15:44 226.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 41 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 15:45 226.0
06/11/2024 15:46 226.0
06/11/2024 15:47 226.2
06/11/2024 15:48 227.0
06/11/2024 15:49 227.0
06/11/2024 15:50 227.0
06/11/2024 15:51 226.8
06/11/2024 15:52 226.0
06/11/2024 15:53 226.0
06/11/2024 15:54 226.0
06/11/2024 15:55 225.2
06/11/2024 15:56 225.0
06/11/2024 15:57 225.0
06/11/2024 15:58 225.5
06/11/2024 15:59 226.5
06/11/2024 16:00 227.5
06/11/2024 16:01 228.7
06/11/2024 16:02 229.0
06/11/2024 16:03 229.8
06/11/2024 16:04 230.0
06/11/2024 16:05 230.0
06/11/2024 16:06 230.0
06/11/2024 16:07 230.0
06/11/2024 16:08 230.0
06/11/2024 16:09 230.0
06/11/2024 16:10 230.0
06/11/2024 16:11 230.0
06/11/2024 16:12 229.0
06/11/2024 16:13 229.0
06/11/2024 16:14 229.0
06/11/2024 16:15 228.5
06/11/2024 16:16 228.0
06/11/2024 16:17 228.0
06/11/2024 16:18 228.0
06/11/2024 16:19 227.8
06/11/2024 16:20 227.0
06/11/2024 16:21 227.0
06/11/2024 16:22 227.0
06/11/2024 16:23 227.0
06/11/2024 16:24 227.0
06/11/2024 16:25 227.0
06/11/2024 16:26 227.0
06/11/2024 16:27 227.0
06/11/2024 16:28 227.0
06/11/2024 16:29 227.2
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 42 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 16:30 228.0
06/11/2024 16:31 228.0
06/11/2024 16:32 228.0
06/11/2024 16:33 228.0
06/11/2024 16:34 228.0
06/11/2024 16:35 228.0
06/11/2024 16:36 228.0
06/11/2024 16:37 228.0
06/11/2024 16:38 228.3
06/11/2024 16:39 229.0
06/11/2024 16:40 229.0
06/11/2024 16:41 229.0
06/11/2024 16:42 229.0
06/11/2024 16:43 228.8
06/11/2024 16:44 228.0
06/11/2024 16:45 228.0
06/11/2024 16:46 228.0
06/11/2024 16:47 227.5
06/11/2024 16:48 227.0
06/11/2024 16:49 227.0
06/11/2024 16:50 227.8
06/11/2024 16:51 228.0
06/11/2024 16:52 228.0
06/11/2024 16:53 228.0
06/11/2024 16:54 228.8
06/11/2024 16:55 229.0
06/11/2024 16:56 229.0
06/11/2024 16:57 229.0
06/11/2024 16:58 229.0
06/11/2024 16:59 229.0
06/11/2024 17:00 229.0
06/11/2024 17:01 229.0
06/11/2024 17:02 229.0
06/11/2024 17:03 229.0
06/11/2024 17:04 229.0
06/11/2024 17:05 228.5
06/11/2024 17:06 228.0
06/11/2024 17:07 228.0
06/11/2024 17:08 228.0
06/11/2024 17:09 228.0
06/11/2024 17:10 228.2
06/11/2024 17:11 229.0
06/11/2024 17:12 229.3
06/11/2024 17:13 230.0
06/11/2024 17:14 229.5
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 43 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 17:15 228.7
06/11/2024 17:16 228.0
06/11/2024 17:17 227.0
06/11/2024 17:18 227.0
06/11/2024 17:19 227.0
06/11/2024 17:20 226.8
06/11/2024 17:21 226.0
06/11/2024 17:22 226.0
06/11/2024 17:23 225.2
06/11/2024 17:24 226.0
06/11/2024 17:25 226.0
06/11/2024 17:26 225.5
06/11/2024 17:27 225.3
06/11/2024 17:28 225.5
06/11/2024 17:29 226.0
06/11/2024 17:30 225.2
06/11/2024 17:31 225.0
06/11/2024 17:32 225.0
06/11/2024 17:33 225.2
06/11/2024 17:34 226.0
06/11/2024 17:35 226.3
06/11/2024 17:36 227.0
06/11/2024 17:37 227.0
06/11/2024 17:38 227.0
06/11/2024 17:39 227.0
06/11/2024 17:40 226.2
06/11/2024 17:41 226.0
06/11/2024 17:42 226.0
06/11/2024 17:43 226.0
06/11/2024 17:44 226.2
06/11/2024 17:45 226.5
06/11/2024 17:46 226.0
06/11/2024 17:47 226.0
06/11/2024 17:48 226.0
06/11/2024 17:49 226.0
06/11/2024 17:50 225.7
06/11/2024 17:51 225.0
06/11/2024 17:52 225.3
06/11/2024 17:53 226.0
06/11/2024 17:54 226.0
06/11/2024 17:55 226.0
06/11/2024 17:56 226.0
06/11/2024 17:57 226.0
06/11/2024 17:58 226.0
06/11/2024 17:59 226.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 44 of 315 ©Mostardi Platt
Date/Time
IN_TMP_BA
G_MILL_ON
(DEGF)
Raw
Value
06/11/2024 18:00 227.0
06/11/2024 18:01 227.0
06/11/2024 18:02 227.0
06/11/2024 18:03 227.0
06/11/2024 18:04 227.0
06/11/2024 18:05 227.0
06/11/2024 18:06 227.0
06/11/2024 18:07 226.3
06/11/2024 18:08 226.0
06/11/2024 18:09 225.3
Average
Max
Min
Count
227.4
230.0
225.0
190
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 45 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 05:55 101.0 8.3 1.0 0.0
06/12/2024 05:56 100.4 8.8 1.0 0.0
06/12/2024 05:57 101.9 8.5 1.0 0.0
06/12/2024 05:58 101.1 8.4 1.0 0.0
06/12/2024 05:59 101.6 8.2 1.0 0.0
06/12/2024 06:00 101.5 8.1 1.0 0.0
06/12/2024 06:01 99.9 8.1 1.0 0.0
06/12/2024 06:02 104.0 8.1 1.0 0.0
06/12/2024 06:03 99.3 8.2 1.0 0.0
06/12/2024 06:04 104.1 7.9 1.0 0.0
06/12/2024 06:05 103.7 8.1 1.0 0.0
06/12/2024 06:06 101.1 8.0 1.0 0.0
06/12/2024 06:07 101.2 7.8 1.0 0.0
06/12/2024 06:08 101.1 8.1 1.0 0.0
06/12/2024 06:09 98.9 8.0 1.0 0.0
06/12/2024 06:10 101.6 7.9 1.0 0.0
06/12/2024 06:11 98.7 7.8 1.0 0.0
06/12/2024 06:12 101.2 7.7 1.0 0.0
06/12/2024 06:13 101.3 8.6 1.0 0.0
06/12/2024 06:14 102.4 8.3 1.0 0.0
06/12/2024 06:15 101.6 8.0 1.0 0.0
06/12/2024 06:16 100.7 8.3 1.0 0.0
06/12/2024 06:17 101.2 8.1 1.0 0.0
06/12/2024 06:18 101.2 7.9 1.0 0.0
06/12/2024 06:19 98.0 8.2 1.0 0.0
06/12/2024 06:20 101.9 8.4 1.0 0.0
06/12/2024 06:21 100.6 8.6 1.0 0.0
06/12/2024 06:22 102.7 8.2 1.0 0.0
06/12/2024 06:23 101.2 8.3 1.0 0.0
06/12/2024 06:24 103.4 8.3 1.0 0.0
06/12/2024 06:25 100.3 8.3 1.0 0.0
06/12/2024 06:26 100.2 8.4 1.0 0.0
06/12/2024 06:27 100.9 8.4 1.0 0.0
06/12/2024 06:28 101.1 8.8 1.0 0.0
06/12/2024 06:29 101.8 8.6 1.0 0.0
06/12/2024 06:30 101.0 8.4 1.0 0.0
06/12/2024 06:31 101.3 8.3 1.0 0.0
06/12/2024 06:32 101.5 8.6 1.0 0.0
06/12/2024 06:33 101.3 8.5 1.0 0.0
06/12/2024 06:34 100.7 8.3 1.0 0.0
06/12/2024 06:35 101.2 8.4 1.0 0.0
06/12/2024 06:36 101.2 8.1 1.0 0.0
06/12/2024 06:37 101.1 8.3 1.0 0.0
06/12/2024 06:38 100.7 8.0 1.0 0.0
06/12/2024 06:39 101.6 8.2 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 46 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 06:40 101.0 8.7 1.0 0.0
06/12/2024 06:41 100.7 8.1 1.0 0.0
06/12/2024 06:42 101.8 8.4 1.0 0.0
06/12/2024 06:43 100.0 8.4 1.0 0.0
06/12/2024 06:44 102.4 8.0 1.0 0.0
06/12/2024 06:45 103.4 7.8 1.0 0.0
06/12/2024 06:46 100.3 8.0 1.0 0.0
06/12/2024 06:47 101.7 7.9 1.0 0.0
06/12/2024 06:48 101.8 7.8 1.0 0.0
06/12/2024 06:49 102.3 8.3 1.0 0.0
06/12/2024 06:50 101.1 8.2 1.0 0.0
06/12/2024 06:51 99.7 8.5 1.0 0.0
06/12/2024 06:52 100.7 8.3 1.0 0.0
06/12/2024 06:53 99.7 8.5 1.0 0.0
06/12/2024 06:54 102.1 8.1 1.0 0.0
06/12/2024 06:55 101.3 8.4 1.0 0.0
06/12/2024 06:56 100.1 8.5 1.0 0.0
06/12/2024 06:57 101.4 8.2 1.0 0.0
06/12/2024 06:58 101.2 8.4 1.0 0.0
06/12/2024 06:59 101.0 8.3 1.0 0.0
06/12/2024 07:00 100.8 8.4 1.0 0.0
06/12/2024 07:01 101.7 2.5 1.0 0.0
06/12/2024 07:02 100.4 -0.1 1.0 0.0
06/12/2024 07:03 99.7 -0.1 1.0 0.0
06/12/2024 07:04 100.2 -0.1 1.0 0.0
06/12/2024 07:05 100.4 64.5 1.0 0.0
06/12/2024 07:06 100.1 65.7 1.0 0.0
06/12/2024 07:07 99.7 65.6 1.0 0.0
06/12/2024 07:08 100.9 43.2 1.0 0.0
06/12/2024 07:09 100.6 1.3 1.0 0.0
06/12/2024 07:10 100.5 7.9 1.0 0.0
06/12/2024 07:11 100.3 7.7 1.0 0.0
06/12/2024 07:12 99.7 7.9 1.0 0.0
06/12/2024 07:13 99.1 7.8 1.0 0.0
06/12/2024 07:14 99.7 7.9 1.0 0.0
06/12/2024 07:15 99.3 7.9 1.0 0.0
06/12/2024 07:16 100.5 8.0 1.0 0.0
06/12/2024 07:17 100.2 8.0 1.0 0.0
06/12/2024 07:18 99.8 8.0 1.0 0.0
06/12/2024 07:19 101.1 8.2 1.0 0.0
06/12/2024 07:20 99.4 7.9 1.0 0.0
06/12/2024 07:21 99.3 8.9 1.0 0.0
06/12/2024 07:22 100.9 8.4 1.0 0.0
06/12/2024 07:23 99.3 7.6 1.0 0.0
06/12/2024 07:24 102.9 8.0 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 47 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 07:25 99.6 8.0 1.0 0.0
06/12/2024 07:26 99.6 7.8 1.0 0.0
06/12/2024 07:27 102.3 7.9 1.0 0.0
06/12/2024 07:28 102.9 7.9 1.0 0.0
06/12/2024 07:29 99.9 8.1 1.0 0.0
06/12/2024 07:30 107.1 7.8 1.0 0.0
06/12/2024 07:31 101.6 8.8 1.0 0.0
06/12/2024 07:32 103.3 8.0 1.0 0.0
06/12/2024 07:33 100.6 8.1 1.0 0.0
06/12/2024 07:34 101.5 7.7 1.0 0.0
06/12/2024 07:35 101.6 8.1 1.0 0.0
06/12/2024 07:36 101.5 8.0 1.0 0.0
06/12/2024 07:37 100.5 8.5 1.0 0.0
06/12/2024 07:38 100.3 8.0 1.0 0.0
06/12/2024 07:39 101.5 8.5 1.0 0.0
06/12/2024 07:40 100.5 8.7 1.0 0.0
06/12/2024 07:41 101.4 8.3 1.0 0.0
06/12/2024 07:42 101.8 8.6 1.0 0.0
06/12/2024 07:43 101.0 8.6 1.0 0.0
06/12/2024 07:44 101.7 8.5 1.0 0.0
06/12/2024 07:45 101.1 8.2 1.0 0.0
06/12/2024 07:46 101.2 8.4 1.0 0.0
06/12/2024 07:47 101.6 8.1 1.0 0.0
06/12/2024 07:48 100.1 8.0 1.0 0.0
06/12/2024 07:49 101.2 8.0 1.0 0.0
06/12/2024 07:50 101.8 7.9 1.0 0.0
06/12/2024 07:51 102.2 8.0 1.0 0.0
06/12/2024 07:52 99.9 7.9 1.0 0.0
06/12/2024 07:53 100.3 8.1 1.0 0.0
06/12/2024 07:54 101.9 8.2 1.0 0.0
06/12/2024 07:55 99.3 8.0 1.0 0.0
06/12/2024 07:56 103.3 8.0 1.0 0.0
06/12/2024 07:57 101.5 8.0 1.0 0.0
06/12/2024 07:58 102.0 7.8 1.0 0.0
06/12/2024 07:59 101.0 7.8 1.0 0.0
06/12/2024 08:00 100.6 7.6 1.0 0.0
06/12/2024 08:01 100.9 7.6 1.0 0.0
06/12/2024 08:02 102.1 7.8 1.0 0.0
06/12/2024 08:03 101.0 7.6 1.0 0.0
Average
Max
Min
Count
101.1
107.1
98.0
129
8.2
8.9
7.6
119
1
1
1
129
0
0
0
129
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 48 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 08:20 102.1 7.9 1.0 0.0
06/12/2024 08:21 102.3 7.8 1.0 0.0
06/12/2024 08:22 100.7 7.6 1.0 0.0
06/12/2024 08:23 101.1 8.0 1.0 0.0
06/12/2024 08:24 100.8 7.8 1.0 0.0
06/12/2024 08:25 102.7 7.4 1.0 0.0
06/12/2024 08:26 102.7 8.0 1.0 0.0
06/12/2024 08:27 102.2 7.5 1.0 0.0
06/12/2024 08:28 105.4 8.4 1.0 0.0
06/12/2024 08:29 103.7 8.2 1.0 0.0
06/12/2024 08:30 100.8 7.8 1.0 0.0
06/12/2024 08:31 102.2 7.6 1.0 0.0
06/12/2024 08:32 100.6 8.1 1.0 0.0
06/12/2024 08:33 101.8 7.9 1.0 0.0
06/12/2024 08:34 100.4 8.0 1.0 0.0
06/12/2024 08:35 100.7 7.8 1.0 0.0
06/12/2024 08:36 100.7 8.1 1.0 0.0
06/12/2024 08:37 101.1 8.6 1.0 0.0
06/12/2024 08:38 101.5 8.2 1.0 0.0
06/12/2024 08:39 101.5 8.3 1.0 0.0
06/12/2024 08:40 101.5 8.5 1.0 0.0
06/12/2024 08:41 101.1 7.9 1.0 0.0
06/12/2024 08:42 103.8 7.8 1.0 0.0
06/12/2024 08:43 101.2 8.2 1.0 0.0
06/12/2024 08:44 101.6 8.4 1.0 0.0
06/12/2024 08:45 101.0 7.8 1.0 0.0
06/12/2024 08:46 102.0 7.8 1.0 0.0
06/12/2024 08:47 100.9 8.0 1.0 0.0
06/12/2024 08:48 100.7 8.2 1.0 0.0
06/12/2024 08:49 100.3 8.0 1.0 0.0
06/12/2024 08:50 100.5 7.7 1.0 0.0
06/12/2024 08:51 100.3 7.5 1.0 0.0
06/12/2024 08:52 100.9 7.6 1.0 0.0
06/12/2024 08:53 100.0 7.8 1.0 0.0
06/12/2024 08:54 100.7 7.6 1.0 0.0
06/12/2024 08:55 103.5 8.0 1.0 0.0
06/12/2024 08:56 100.6 8.0 1.0 0.0
06/12/2024 08:57 100.8 7.6 1.0 0.0
06/12/2024 08:58 100.9 7.7 1.0 0.0
06/12/2024 08:59 102.3 7.9 1.0 0.0
06/12/2024 09:00 101.7 7.8 1.0 0.0
06/12/2024 09:01 101.7 8.2 1.0 0.0
06/12/2024 09:02 101.0 7.9 1.0 0.0
06/12/2024 09:03 100.8 7.5 1.0 0.0
06/12/2024 09:04 101.3 7.8 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 49 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 09:05 100.9 7.4 1.0 0.0
06/12/2024 09:06 100.9 7.6 1.0 0.0
06/12/2024 09:07 102.2 7.9 1.0 0.0
06/12/2024 09:08 101.1 7.9 1.0 0.0
06/12/2024 09:09 100.9 8.0 1.0 0.0
06/12/2024 09:10 101.4 7.7 1.0 0.0
06/12/2024 09:11 101.2 7.7 1.0 0.0
06/12/2024 09:12 101.3 7.8 1.0 0.0
06/12/2024 09:13 100.3 8.0 1.0 0.0
06/12/2024 09:14 100.7 7.9 1.0 0.0
06/12/2024 09:15 101.3 7.8 1.0 0.0
06/12/2024 09:16 102.2 7.6 1.0 0.0
06/12/2024 09:17 101.4 7.6 1.0 0.0
06/12/2024 09:18 102.1 7.7 1.0 0.0
06/12/2024 09:19 100.7 8.0 1.0 0.0
06/12/2024 09:20 101.0 7.5 1.0 0.0
06/12/2024 09:21 100.9 7.7 1.0 0.0
06/12/2024 09:22 102.7 7.6 1.0 0.0
06/12/2024 09:23 102.1 7.8 1.0 0.0
06/12/2024 09:24 100.9 7.7 1.0 0.0
06/12/2024 09:25 100.8 7.7 1.0 0.0
06/12/2024 09:26 101.2 7.4 1.0 0.0
06/12/2024 09:27 101.2 7.7 1.0 0.0
06/12/2024 09:28 101.3 7.6 1.0 0.0
06/12/2024 09:29 100.3 7.7 1.0 0.0
06/12/2024 09:30 101.0 7.7 1.0 0.0
06/12/2024 09:31 101.0 7.5 1.0 0.0
06/12/2024 09:32 99.8 7.4 1.0 0.0
06/12/2024 09:33 101.9 8.1 1.0 0.0
06/12/2024 09:34 106.2 7.7 1.0 0.0
06/12/2024 09:35 98.1 8.4 1.0 0.0
06/12/2024 09:36 105.0 8.4 1.0 0.0
06/12/2024 09:37 100.0 7.6 1.0 0.0
06/12/2024 09:38 97.9 7.8 1.0 0.0
06/12/2024 09:39 100.2 8.0 1.0 0.0
06/12/2024 09:40 103.1 8.1 1.0 0.0
06/12/2024 09:41 103.8 7.7 1.0 0.0
06/12/2024 09:42 102.3 7.6 1.0 0.0
06/12/2024 09:43 100.6 8.2 1.0 0.0
06/12/2024 09:44 100.9 8.5 1.0 0.0
06/12/2024 09:45 101.3 7.6 1.0 0.0
06/12/2024 09:46 100.6 8.1 1.0 0.0
06/12/2024 09:47 100.8 7.8 1.0 0.0
06/12/2024 09:48 101.2 8.0 1.0 0.0
06/12/2024 09:49 101.9 7.7 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 50 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 09:50 101.2 8.0 1.0 0.0
06/12/2024 09:51 101.3 7.9 1.0 0.0
06/12/2024 09:52 100.3 8.2 1.0 0.0
06/12/2024 09:53 100.9 7.7 1.0 0.0
06/12/2024 09:54 100.6 7.7 1.0 0.0
06/12/2024 09:55 101.3 7.7 1.0 0.0
06/12/2024 09:56 101.2 7.7 1.0 0.0
06/12/2024 09:57 101.0 7.3 1.0 0.0
06/12/2024 09:58 103.8 7.9 1.0 0.0
06/12/2024 09:59 99.8 7.8 1.0 0.0
06/12/2024 10:00 101.6 7.7 1.0 0.0
06/12/2024 10:01 99.9 7.8 1.0 0.0
06/12/2024 10:02 100.4 7.6 1.0 0.0
06/12/2024 10:03 100.8 7.7 1.0 0.0
06/12/2024 10:04 101.1 8.0 1.0 0.0
06/12/2024 10:05 100.6 8.2 1.0 0.0
06/12/2024 10:06 101.3 8.0 1.0 0.0
06/12/2024 10:07 101.9 7.9 1.0 0.0
06/12/2024 10:08 100.9 7.9 1.0 0.0
06/12/2024 10:09 101.3 7.6 1.0 0.0
06/12/2024 10:10 101.5 7.7 1.0 0.0
06/12/2024 10:11 102.0 7.6 1.0 0.0
06/12/2024 10:12 101.2 7.7 1.0 0.0
06/12/2024 10:13 100.5 7.9 1.0 0.0
06/12/2024 10:14 103.4 7.5 1.0 0.0
06/12/2024 10:15 100.9 7.9 1.0 0.0
06/12/2024 10:16 102.9 8.0 1.0 0.0
06/12/2024 10:17 101.0 8.0 1.0 0.0
06/12/2024 10:18 98.4 8.0 1.0 0.0
06/12/2024 10:19 99.6 7.9 1.0 0.0
06/12/2024 10:20 101.2 7.9 1.0 0.0
06/12/2024 10:21 101.1 7.7 1.0 0.0
06/12/2024 10:22 101.0 7.8 1.0 0.0
06/12/2024 10:23 101.3 7.9 1.0 0.0
Average
Max
Min
Count
101.3
106.2
97.9
124
7.8
8.6
7.3
124
1
1
1
124
0
0
0
124
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 51 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 10:55 101.1 8.0 1.0 0.0
06/12/2024 10:56 99.1 8.0 1.0 0.0
06/12/2024 10:57 100.7 8.2 1.0 0.0
06/12/2024 10:58 104.3 8.0 1.0 0.0
06/12/2024 10:59 101.0 7.8 1.0 0.0
06/12/2024 11:00 98.2 7.6 1.0 0.0
06/12/2024 11:01 103.2 8.2 1.0 0.0
06/12/2024 11:02 101.3 8.1 1.0 0.0
06/12/2024 11:03 99.0 8.0 1.0 0.0
06/12/2024 11:04 101.0 8.2 1.0 0.0
06/12/2024 11:05 101.0 7.8 1.0 0.0
06/12/2024 11:06 101.4 7.9 1.0 0.0
06/12/2024 11:07 101.1 8.0 1.0 0.0
06/12/2024 11:08 100.2 7.8 1.0 0.0
06/12/2024 11:09 102.1 8.0 1.0 0.0
06/12/2024 11:10 100.9 7.9 1.0 0.0
06/12/2024 11:11 101.2 8.1 1.0 0.0
06/12/2024 11:12 101.7 8.1 1.0 0.0
06/12/2024 11:13 99.6 8.0 1.0 0.0
06/12/2024 11:14 101.1 7.9 1.0 0.0
06/12/2024 11:15 100.5 8.3 1.0 0.0
06/12/2024 11:16 100.8 8.2 1.0 0.0
06/12/2024 11:17 99.5 8.0 1.0 0.0
06/12/2024 11:18 103.3 8.1 1.0 0.0
06/12/2024 11:19 101.6 8.0 1.0 0.0
06/12/2024 11:20 101.0 7.8 1.0 0.0
06/12/2024 11:21 102.1 8.1 1.0 0.0
06/12/2024 11:22 99.9 8.2 1.0 0.0
06/12/2024 11:23 101.2 8.4 1.0 0.0
06/12/2024 11:24 101.9 8.0 1.0 0.0
06/12/2024 11:25 101.1 8.2 1.0 0.0
06/12/2024 11:26 101.3 8.4 1.0 0.0
06/12/2024 11:27 101.5 7.9 1.0 0.0
06/12/2024 11:28 101.5 8.0 1.0 0.0
06/12/2024 11:29 100.9 7.7 1.0 0.0
06/12/2024 11:30 100.6 8.0 1.0 0.0
06/12/2024 11:31 100.6 8.1 1.0 0.0
06/12/2024 11:32 101.3 8.0 1.0 0.0
06/12/2024 11:33 100.3 8.1 1.0 0.0
06/12/2024 11:34 101.2 7.6 1.0 0.0
06/12/2024 11:35 100.5 8.1 1.0 0.0
06/12/2024 11:36 100.5 8.0 1.0 0.0
06/12/2024 11:37 101.1 7.8 1.0 0.0
06/12/2024 11:38 100.9 8.0 1.0 0.0
06/12/2024 11:39 101.2 8.0 1.0 0.0
06/12/2024 11:40 101.8 7.8 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 52 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 11:41 100.7 7.9 1.0 0.0
06/12/2024 11:42 101.5 8.0 1.0 0.0
06/12/2024 11:43 100.5 8.2 1.0 0.0
06/12/2024 11:44 101.5 8.3 1.0 0.0
06/12/2024 11:45 100.7 7.9 1.0 0.0
06/12/2024 11:46 101.5 7.9 1.0 0.0
06/12/2024 11:47 100.6 8.0 1.0 0.0
06/12/2024 11:48 100.6 7.9 1.0 0.0
06/12/2024 11:49 100.8 8.4 1.0 0.0
06/12/2024 11:50 101.8 8.0 1.0 0.0
06/12/2024 11:51 101.8 8.0 1.0 0.0
06/12/2024 11:52 101.2 8.0 1.0 0.0
06/12/2024 11:53 100.9 7.8 1.0 0.0
06/12/2024 11:54 100.7 7.9 1.0 0.0
06/12/2024 11:55 101.5 7.8 1.0 0.0
06/12/2024 11:56 99.8 7.7 1.0 0.0
06/12/2024 11:57 101.5 7.7 1.0 0.0
06/12/2024 11:58 101.7 7.9 1.0 0.0
06/12/2024 11:59 100.4 8.8 1.0 0.0
06/12/2024 12:00 101.6 7.7 1.0 0.0
06/12/2024 12:01 98.8 8.1 1.0 0.0
06/12/2024 12:02 99.2 8.4 1.0 0.0
06/12/2024 12:03 102.3 8.0 1.0 0.0
06/12/2024 12:04 104.0 8.3 1.0 0.0
06/12/2024 12:05 101.3 8.5 1.0 0.0
06/12/2024 12:06 100.7 8.3 1.0 0.0
06/12/2024 12:07 103.7 8.3 1.0 0.0
06/12/2024 12:08 102.2 8.6 1.0 0.0
06/12/2024 12:09 102.3 8.3 1.0 0.0
06/12/2024 12:10 102.2 8.2 1.0 0.0
06/12/2024 12:11 102.3 8.2 1.0 0.0
06/12/2024 12:12 99.3 8.5 1.0 0.0
06/12/2024 12:13 100.9 8.3 1.0 0.0
06/12/2024 12:14 105.1 8.1 1.0 0.0
06/12/2024 12:15 101.5 8.4 1.0 0.0
06/12/2024 12:16 101.7 8.1 1.0 0.0
06/12/2024 12:17 102.5 8.0 1.0 0.0
06/12/2024 12:18 102.1 7.8 1.0 0.0
06/12/2024 12:19 102.0 8.0 1.0 0.0
06/12/2024 12:20 101.6 8.0 1.0 0.0
06/12/2024 12:21 105.1 8.0 1.0 0.0
06/12/2024 12:22 102.8 8.3 1.0 0.0
06/12/2024 12:23 103.0 8.3 1.0 0.0
06/12/2024 12:24 102.3 8.1 1.0 0.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 53 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/12/2024 12:25 100.7 8.3 1.0 0.0
06/12/2024 12:26 104.6 7.7 1.0 0.0
06/12/2024 12:27 101.2 8.0 1.0 0.0
06/12/2024 12:28 104.4 7.9 1.0 0.0
06/12/2024 12:29 98.6 8.0 1.0 0.0
06/12/2024 12:30 103.7 8.1 1.0 0.0
06/12/2024 12:31 105.2 7.9 1.0 0.0
06/12/2024 12:32 101.6 8.0 1.0 0.0
06/12/2024 12:33 100.5 7.7 1.0 0.0
06/12/2024 12:34 101.6 7.6 1.0 0.0
06/12/2024 12:35 102.6 7.9 1.0 0.0
06/12/2024 12:36 98.6 7.7 1.0 0.0
06/12/2024 12:37 107.4 7.8 1.0 0.0
06/12/2024 12:38 102.8 8.0 1.0 0.0
06/12/2024 12:39 102.5 8.3 1.0 0.0
06/12/2024 12:40 104.1 7.9 1.0 0.0
06/12/2024 12:41 103.6 7.6 1.0 0.0
06/12/2024 12:42 102.3 7.8 1.0 0.0
06/12/2024 12:43 101.6 7.5 1.0 0.0
06/12/2024 12:44 105.6 7.6 1.0 0.0
06/12/2024 12:45 102.5 7.7 1.0 0.0
06/12/2024 12:46 102.5 7.5 1.0 0.0
06/12/2024 12:47 104.0 7.9 1.0 0.0
06/12/2024 12:48 103.8 7.5 1.0 0.0
06/12/2024 12:49 102.7 7.6 1.0 0.0
06/12/2024 12:50 103.1 7.5 1.0 0.0
06/12/2024 12:51 99.7 7.6 1.0 0.0
06/12/2024 12:52 104.3 7.4 1.0 0.0
06/12/2024 12:53 104.8 7.7 1.0 0.0
06/12/2024 12:54 100.4 7.6 1.0 0.0
06/12/2024 12:55 102.9 7.4 1.0 0.0
06/12/2024 12:56 102.6 7.4 1.0 0.0
06/12/2024 12:57 108.1 7.7 1.0 0.0
06/12/2024 12:58 101.9 7.9 1.0 0.0
06/12/2024 12:59 101.7 7.7 1.0 0.0
06/12/2024 13:00 104.0 7.6 1.0 0.0
06/12/2024 13:01 102.9 7.8 1.0 0.0
06/12/2024 13:02 104.2 7.7 1.0 0.0
06/12/2024 13:03 100.7 7.6 1.0 0.0
06/12/2024 13:04 104.1 7.5 1.0 0.0
06/12/2024 13:05 103.4 7.7 1.0 0.0
06/12/2024 13:06 102.5 8.8 1.0 0.0
Average
Max
Min
Count
101.8
108.1
98.2
132
8.0
8.8
7.4
132
1
1
1
132
0
0
0
132
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 54 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 14:30 108.9 23.8 0.0 1.0
06/13/2024 14:31 108.8 24.1 0.0 1.0
06/13/2024 14:32 108.3 23.5 0.0 1.0
06/13/2024 14:33 107.8 23.6 0.0 1.0
06/13/2024 14:34 108.9 24.4 0.0 1.0
06/13/2024 14:35 108.1 24.4 0.0 1.0
06/13/2024 14:36 108.7 23.6 0.0 1.0
06/13/2024 14:37 108.7 24.0 0.0 1.0
06/13/2024 14:38 109.0 23.9 0.0 1.0
06/13/2024 14:39 108.6 23.8 0.0 1.0
06/13/2024 14:40 109.6 23.1 0.0 1.0
06/13/2024 14:41 109.1 23.2 0.0 1.0
06/13/2024 14:42 108.9 23.4 0.0 1.0
06/13/2024 14:43 108.6 23.6 0.0 1.0
06/13/2024 14:44 109.1 24.9 0.0 1.0
06/13/2024 14:45 108.6 24.9 0.0 1.0
06/13/2024 14:46 108.3 24.4 0.0 1.0
06/13/2024 14:47 108.9 25.1 0.0 1.0
06/13/2024 14:48 108.5 24.2 0.0 1.0
06/13/2024 14:49 108.6 24.4 0.0 1.0
06/13/2024 14:50 108.6 25.0 0.0 1.0
06/13/2024 14:51 108.6 25.0 0.0 1.0
06/13/2024 14:52 109.5 24.5 0.0 1.0
06/13/2024 14:53 109.5 24.4 0.0 1.0
06/13/2024 14:54 109.3 24.8 0.0 1.0
06/13/2024 14:55 108.7 24.9 0.0 1.0
06/13/2024 14:56 108.4 25.4 0.0 1.0
06/13/2024 14:57 108.8 24.8 0.0 1.0
06/13/2024 14:58 108.6 25.1 0.0 1.0
06/13/2024 14:59 109.2 24.9 0.0 1.0
06/13/2024 15:00 109.4 25.1 0.0 1.0
06/13/2024 15:01 109.5 25.5 0.0 1.0
06/13/2024 15:02 108.9 25.6 0.0 1.0
06/13/2024 15:03 109.0 25.3 0.0 1.0
06/13/2024 15:04 108.1 25.1 0.0 1.0
06/13/2024 15:05 109.2 24.5 0.0 1.0
06/13/2024 15:06 108.0 24.1 0.0 1.0
06/13/2024 15:07 109.0 24.6 0.0 1.0
06/13/2024 15:08 108.9 24.2 0.0 1.0
06/13/2024 15:09 109.5 24.4 0.0 1.0
06/13/2024 15:10 109.2 25.2 0.0 1.0
06/13/2024 15:11 108.6 25.1 0.0 1.0
06/13/2024 15:12 108.1 24.7 0.0 1.0
06/13/2024 15:13 109.0 25.1 0.0 1.0
06/13/2024 15:14 109.5 24.6 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 55 of 315 ©Mostardi Platt
06/13/2024 15:15 109.6 24.9 0.0 1.0
06/13/2024 15:16 109.7 25.6 0.0 1.0
06/13/2024 15:17 109.0 24.7 0.0 1.0
06/13/2024 15:18 108.4 24.6 0.0 1.0
06/13/2024 15:19 107.7 24.7 0.0 1.0
06/13/2024 15:20 108.5 24.1 0.0 1.0
06/13/2024 15:21 108.3 24.8 0.0 1.0
06/13/2024 15:22 108.6 24.8 0.0 1.0
06/13/2024 15:23 109.6 24.5 0.0 1.0
06/13/2024 15:24 109.8 24.5 0.0 1.0
06/13/2024 15:25 109.0 24.3 0.0 1.0
06/13/2024 15:26 109.1 24.4 0.0 1.0
06/13/2024 15:27 108.4 23.9 0.0 1.0
06/13/2024 15:28 108.4 24.1 0.0 1.0
06/13/2024 15:29 108.0 23.8 0.0 1.0
06/13/2024 15:30 108.6 24.6 0.0 1.0
06/13/2024 15:31 108.5 24.2 0.0 1.0
06/13/2024 15:32 108.6 24.8 0.0 1.0
06/13/2024 15:33 109.1 24.3 0.0 1.0
06/13/2024 15:34 108.6 24.1 0.0 1.0
06/13/2024 15:35 108.4 24.4 0.0 1.0
06/13/2024 15:36 108.6 24.2 0.0 1.0
06/13/2024 15:37 109.2 24.1 0.0 1.0
06/13/2024 15:38 108.9 24.6 0.0 1.0
06/13/2024 15:39 109.9 24.3 0.0 1.0
06/13/2024 15:40 109.6 24.5 0.0 1.0
06/13/2024 15:41 109.2 24.6 0.0 1.0
06/13/2024 15:42 107.9 23.9 0.0 1.0
06/13/2024 15:43 108.7 24.2 0.0 1.0
06/13/2024 15:44 108.2 23.4 0.0 1.0
06/13/2024 15:45 108.0 23.7 0.0 1.0
06/13/2024 15:46 108.6 24.1 0.0 1.0
06/13/2024 15:47 109.3 24.7 0.0 1.0
06/13/2024 15:48 109.3 24.0 0.0 1.0
06/13/2024 15:49 109.1 23.9 0.0 1.0
06/13/2024 15:50 108.5 23.1 0.0 1.0
06/13/2024 15:51 108.6 23.1 0.0 1.0
06/13/2024 15:52 108.6 22.4 0.0 1.0
06/13/2024 15:53 108.3 22.7 0.0 1.0
06/13/2024 15:54 108.6 22.8 0.0 1.0
06/13/2024 15:55 108.4 23.2 0.0 1.0
06/13/2024 15:56 108.6 23.6 0.0 1.0
06/13/2024 15:57 108.1 22.4 0.0 1.0
06/13/2024 15:58 109.0 22.8 0.0 1.0
06/13/2024 15:59 108.4 22.7 0.0 1.0
06/13/2024 16:00 108.4 22.4 0.0 1.0
06/13/2024 16:01 108.7 22.3 0.0 1.0
06/13/2024 16:02 109.1 22.3 0.0 1.0
06/13/2024 16:03 109.3 22.1 0.0 1.0
06/13/2024 16:04 109.5 21.9 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 56 of 315 ©Mostardi Platt
06/13/2024 16:05 109.6 22.3 0.0 1.0
06/13/2024 16:06 109.6 21.6 0.0 1.0
06/13/2024 16:07 107.9 22.3 0.0 1.0
06/13/2024 16:08 108.5 22.4 0.0 1.0
06/13/2024 16:09 108.2 22.2 0.0 1.0
06/13/2024 16:10 108.2 22.0 0.0 1.0
06/13/2024 16:11 108.7 21.2 0.0 1.0
06/13/2024 16:12 109.1 21.0 0.0 1.0
06/13/2024 16:13 109.3 21.5 0.0 1.0
06/13/2024 16:14 108.7 22.0 0.0 1.0
06/13/2024 16:15 108.3 21.8 0.0 1.0
06/13/2024 16:16 108.7 21.9 0.0 1.0
06/13/2024 16:17 108.5 22.3 0.0 1.0
06/13/2024 16:18 109.1 21.6 0.0 1.0
06/13/2024 16:19 108.7 21.8 0.0 1.0
06/13/2024 16:20 109.1 22.3 0.0 1.0
06/13/2024 16:21 108.8 22.0 0.0 1.0
06/13/2024 16:22 108.6 21.8 0.0 1.0
06/13/2024 16:23 109.0 21.6 0.0 1.0
06/13/2024 16:24 108.1 21.3 0.0 1.0
06/13/2024 16:25 108.7 22.0 0.0 1.0
06/13/2024 16:26 109.5 21.7 0.0 1.0
06/13/2024 16:27 109.8 21.2 0.0 1.0
06/13/2024 16:28 109.6 21.2 0.0 1.0
06/13/2024 16:29 109.4 21.3 0.0 1.0
06/13/2024 16:30 109.0 21.7 0.0 1.0
06/13/2024 16:31 108.6 21.3 0.0 1.0
06/13/2024 16:32 107.9 20.8 0.0 1.0
06/13/2024 16:33 108.1 20.7 0.0 1.0
06/13/2024 16:34 108.3 21.7 0.0 1.0
06/13/2024 16:35 109.1 20.8 0.0 1.0
06/13/2024 16:36 108.4 21.0 0.0 1.0
06/13/2024 16:37 109.2 21.2 0.0 1.0
06/13/2024 16:38 108.6 20.4 0.0 1.0
06/13/2024 16:39 108.7 20.3 0.0 1.0
Average
Max
Min
Count
108.8
109.9
107.7
130
23.5
25.6
20.3
130
0
0
0
130
1
1
1
130
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 57 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 07:30 107.2 10.2 0.0 1.0
06/13/2024 07:31 106.5 9.9 0.0 1.0
06/13/2024 07:32 106.6 10.4 0.0 1.0
06/13/2024 07:33 106.4 10.6 0.0 1.0
06/13/2024 07:34 106.1 10.4 0.0 1.0
06/13/2024 07:35 106.9 11.2 0.0 1.0
06/13/2024 07:36 107.1 10.3 0.0 1.0
06/13/2024 07:37 107.3 10.7 0.0 1.0
06/13/2024 07:38 107.2 10.5 0.0 1.0
06/13/2024 07:39 107.3 10.1 0.0 1.0
06/13/2024 07:40 106.8 10.6 0.0 1.0
06/13/2024 07:41 106.6 10.4 0.0 1.0
06/13/2024 07:42 106.2 10.4 0.0 1.0
06/13/2024 07:43 106.2 10.6 0.0 1.0
06/13/2024 07:44 106.8 10.3 0.0 1.0
06/13/2024 07:45 108.0 10.3 0.0 1.0
06/13/2024 07:46 107.1 10.2 0.0 1.0
06/13/2024 07:47 107.9 10.3 0.0 1.0
06/13/2024 07:48 108.0 10.0 0.0 1.0
06/13/2024 07:49 107.1 9.8 0.0 1.0
06/13/2024 07:50 107.2 10.1 0.0 1.0
06/13/2024 07:51 107.1 10.0 0.0 1.0
06/13/2024 07:52 108.3 10.0 0.0 1.0
06/13/2024 07:53 108.4 10.3 0.0 1.0
06/13/2024 07:54 106.7 10.9 0.0 1.0
06/13/2024 07:55 107.3 10.4 0.0 1.0
06/13/2024 07:56 107.0 11.1 0.0 1.0
06/13/2024 07:57 106.9 10.5 0.0 1.0
06/13/2024 07:58 105.3 10.6 0.0 1.0
06/13/2024 07:59 106.7 10.3 0.0 1.0
06/13/2024 08:00 107.6 10.0 0.0 1.0
06/13/2024 08:01 106.8 10.3 0.0 1.0
06/13/2024 08:02 106.0 10.0 0.0 1.0
06/13/2024 08:03 106.3 11.3 0.0 1.0
06/13/2024 08:04 107.1 10.6 0.0 1.0
06/13/2024 08:05 107.2 10.4 0.0 1.0
06/13/2024 08:06 106.9 10.2 0.0 1.0
06/13/2024 08:07 106.9 10.1 0.0 1.0
06/13/2024 08:08 107.2 10.3 0.0 1.0
06/13/2024 08:09 107.2 10.1 0.0 1.0
06/13/2024 08:10 107.2 10.0 0.0 1.0
06/13/2024 08:11 107.5 10.3 0.0 1.0
06/13/2024 08:12 108.1 10.8 0.0 1.0
06/13/2024 08:13 107.5 10.4 0.0 1.0
06/13/2024 08:14 107.4 10.3 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 58 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 08:15 107.4 10.0 0.0 1.0
06/13/2024 08:16 107.3 9.6 0.0 1.0
06/13/2024 08:17 107.3 10.0 0.0 1.0
06/13/2024 08:18 108.4 10.9 0.0 1.0
06/13/2024 08:19 108.1 11.1 0.0 1.0
06/13/2024 08:20 107.2 11.2 0.0 1.0
06/13/2024 08:21 107.2 11.0 0.0 1.0
06/13/2024 08:22 107.3 10.3 0.0 1.0
06/13/2024 08:23 106.7 10.0 0.0 1.0
06/13/2024 08:24 107.2 10.3 0.0 1.0
06/13/2024 08:25 106.7 10.7 0.0 1.0
06/13/2024 08:26 107.0 10.1 0.0 1.0
06/13/2024 08:27 107.0 10.2 0.0 1.0
06/13/2024 08:28 107.7 10.5 0.0 1.0
06/13/2024 08:29 106.5 10.9 0.0 1.0
06/13/2024 08:30 107.0 10.5 0.0 1.0
06/13/2024 08:31 107.1 10.6 0.0 1.0
06/13/2024 08:32 107.2 10.5 0.0 1.0
06/13/2024 08:33 108.5 10.3 0.0 1.0
06/13/2024 08:34 108.7 10.5 0.0 1.0
06/13/2024 08:35 108.3 10.3 0.0 1.0
06/13/2024 08:36 107.5 11.0 0.0 1.0
06/13/2024 08:37 106.8 10.5 0.0 1.0
06/13/2024 08:38 107.3 10.9 0.0 1.0
06/13/2024 08:39 107.3 11.7 0.0 1.0
06/13/2024 08:40 108.5 10.9 0.0 1.0
06/13/2024 08:41 108.1 11.1 0.0 1.0
06/13/2024 08:42 108.5 11.2 0.0 1.0
06/13/2024 08:43 108.9 10.8 0.0 1.0
06/13/2024 08:44 107.4 10.4 0.0 1.0
06/13/2024 08:45 107.7 10.2 0.0 1.0
06/13/2024 08:46 107.3 10.3 0.0 1.0
06/13/2024 08:47 107.0 10.7 0.0 1.0
06/13/2024 08:48 107.9 9.8 0.0 1.0
06/13/2024 08:49 108.1 10.1 0.0 1.0
06/13/2024 08:50 108.9 10.4 0.0 1.0
06/13/2024 08:51 109.1 10.2 0.0 1.0
06/13/2024 08:52 108.7 9.9 0.0 1.0
06/13/2024 08:53 107.3 10.0 0.0 1.0
06/13/2024 08:54 108.1 10.2 0.0 1.0
06/13/2024 08:55 108.0 10.4 0.0 1.0
06/13/2024 08:56 107.9 10.2 0.0 1.0
06/13/2024 08:57 109.0 10.2 0.0 1.0
06/13/2024 08:58 108.6 10.6 0.0 1.0
06/13/2024 08:59 108.9 10.6 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 59 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 09:00 108.9 10.9 0.0 1.0
06/13/2024 09:01 109.0 11.3 0.0 1.0
06/13/2024 09:02 108.8 10.6 0.0 1.0
06/13/2024 09:03 108.3 10.6 0.0 1.0
06/13/2024 09:04 107.9 10.5 0.0 1.0
06/13/2024 09:05 108.2 10.0 0.0 1.0
06/13/2024 09:06 108.1 9.6 0.0 1.0
06/13/2024 09:07 109.0 9.5 0.0 1.0
06/13/2024 09:08 108.9 9.8 0.0 1.0
06/13/2024 09:09 108.3 10.8 0.0 1.0
06/13/2024 09:10 108.4 10.6 0.0 1.0
06/13/2024 09:11 109.0 10.5 0.0 1.0
06/13/2024 09:12 109.0 10.2 0.0 1.0
06/13/2024 09:13 109.5 10.3 0.0 1.0
06/13/2024 09:14 109.1 9.8 0.0 1.0
06/13/2024 09:15 108.9 10.4 0.0 1.0
06/13/2024 09:16 109.0 9.0 0.0 1.0
06/13/2024 09:17 108.4 9.0 0.0 1.0
06/13/2024 09:18 108.0 8.9 0.0 1.0
06/13/2024 09:19 108.0 9.3 0.0 1.0
06/13/2024 09:20 108.8 8.7 0.0 1.0
06/13/2024 09:21 109.4 9.6 0.0 1.0
06/13/2024 09:22 109.0 10.0 0.0 1.0
06/13/2024 09:23 109.9 9.9 0.0 1.0
06/13/2024 09:24 108.7 9.5 0.0 1.0
06/13/2024 09:25 108.5 10.2 0.0 1.0
06/13/2024 09:26 108.3 9.9 0.0 1.0
06/13/2024 09:27 107.5 10.3 0.0 1.0
06/13/2024 09:28 108.5 9.9 0.0 1.0
06/13/2024 09:29 108.3 9.8 0.0 1.0
06/13/2024 09:30 108.9 9.8 0.0 1.0
06/13/2024 09:31 109.4 9.5 0.0 1.0
06/13/2024 09:32 109.1 10.6 0.0 1.0
06/13/2024 09:33 109.6 9.9 0.0 1.0
Average
Max
Min
Count
107.8
109.9
105.3
124
10.3
11.7
8.7
124
0
0
0
124
1
1
1
124
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 60 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 09:45 108.6 10.7 0.0 1.0
06/13/2024 09:46 108.1 10.4 0.0 1.0
06/13/2024 09:47 108.8 10.4 0.0 1.0
06/13/2024 09:48 109.2 9.9 0.0 1.0
06/13/2024 09:49 108.9 11.1 0.0 1.0
06/13/2024 09:50 108.9 11.0 0.0 1.0
06/13/2024 09:51 108.9 10.4 0.0 1.0
06/13/2024 09:52 108.4 10.4 0.0 1.0
06/13/2024 09:53 108.9 10.1 0.0 1.0
06/13/2024 09:54 108.3 10.7 0.0 1.0
06/13/2024 09:55 108.7 10.5 0.0 1.0
06/13/2024 09:56 109.0 10.0 0.0 1.0
06/13/2024 09:57 108.4 10.1 0.0 1.0
06/13/2024 09:58 108.6 10.2 0.0 1.0
06/13/2024 09:59 108.5 10.1 0.0 1.0
06/13/2024 10:00 108.5 10.0 0.0 1.0
06/13/2024 10:01 108.7 9.7 0.0 1.0
06/13/2024 10:02 108.1 10.1 0.0 1.0
06/13/2024 10:03 108.6 9.5 0.0 1.0
06/13/2024 10:04 108.8 10.2 0.0 1.0
06/13/2024 10:05 109.0 9.7 0.0 1.0
06/13/2024 10:06 109.0 10.3 0.0 1.0
06/13/2024 10:07 108.2 10.0 0.0 1.0
06/13/2024 10:08 108.5 10.4 0.0 1.0
06/13/2024 10:09 108.9 10.7 0.0 1.0
06/13/2024 10:10 109.2 10.7 0.0 1.0
06/13/2024 10:11 110.1 10.6 0.0 1.0
06/13/2024 10:12 109.3 10.6 0.0 1.0
06/13/2024 10:13 109.1 11.3 0.0 1.0
06/13/2024 10:14 108.4 10.4 0.0 1.0
06/13/2024 10:15 108.4 10.0 0.0 1.0
06/13/2024 10:16 108.5 10.0 0.0 1.0
06/13/2024 10:17 108.5 9.6 0.0 1.0
06/13/2024 10:18 109.2 9.9 0.0 1.0
06/13/2024 10:19 108.6 10.6 0.0 1.0
06/13/2024 10:20 108.8 10.1 0.0 1.0
06/13/2024 10:21 109.0 10.3 0.0 1.0
06/13/2024 10:22 108.7 10.3 0.0 1.0
06/13/2024 10:23 108.1 10.0 0.0 1.0
06/13/2024 10:24 108.8 10.2 0.0 1.0
06/13/2024 10:25 108.5 10.1 0.0 1.0
06/13/2024 10:26 109.5 10.1 0.0 1.0
06/13/2024 10:27 109.1 10.0 0.0 1.0
06/13/2024 10:28 109.8 10.1 0.0 1.0
06/13/2024 10:29 108.9 9.9 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 61 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 10:30 109.1 10.2 0.0 1.0
06/13/2024 10:31 108.8 10.3 0.0 1.0
06/13/2024 10:32 108.8 10.3 0.0 1.0
06/13/2024 10:33 109.2 10.2 0.0 1.0
06/13/2024 10:34 108.8 11.0 0.0 1.0
06/13/2024 10:35 109.3 10.2 0.0 1.0
06/13/2024 10:36 109.2 10.5 0.0 1.0
06/13/2024 10:37 109.2 10.6 0.0 1.0
06/13/2024 10:38 108.5 10.1 0.0 1.0
06/13/2024 10:39 108.4 9.8 0.0 1.0
06/13/2024 10:40 108.8 10.2 0.0 1.0
06/13/2024 10:41 108.5 10.1 0.0 1.0
06/13/2024 10:42 108.9 10.4 0.0 1.0
06/13/2024 10:43 108.7 10.4 0.0 1.0
06/13/2024 10:44 108.7 9.9 0.0 1.0
06/13/2024 10:45 108.7 9.6 0.0 1.0
06/13/2024 10:46 108.3 10.1 0.0 1.0
06/13/2024 10:47 107.9 10.0 0.0 1.0
06/13/2024 10:48 108.8 10.2 0.0 1.0
06/13/2024 10:49 110.2 9.6 0.0 1.0
06/13/2024 10:50 109.6 9.8 0.0 1.0
06/13/2024 10:51 109.5 10.1 0.0 1.0
06/13/2024 10:52 108.4 10.0 0.0 1.0
06/13/2024 10:53 108.4 10.1 0.0 1.0
06/13/2024 10:54 108.3 9.8 0.0 1.0
06/13/2024 10:55 108.5 9.6 0.0 1.0
06/13/2024 10:56 107.8 10.0 0.0 1.0
06/13/2024 10:57 109.5 10.5 0.0 1.0
06/13/2024 10:58 109.0 11.1 0.0 1.0
06/13/2024 10:59 109.1 10.7 0.0 1.0
06/13/2024 11:00 108.9 11.0 0.0 1.0
06/13/2024 11:01 107.9 10.3 0.0 1.0
06/13/2024 11:02 108.2 10.8 0.0 1.0
06/13/2024 11:03 108.4 10.1 0.0 1.0
06/13/2024 11:04 108.4 9.8 0.0 1.0
06/13/2024 11:05 108.7 9.8 0.0 1.0
06/13/2024 11:06 108.4 9.8 0.0 1.0
06/13/2024 11:07 109.2 9.7 0.0 1.0
06/13/2024 11:08 108.7 10.6 0.0 1.0
06/13/2024 11:09 109.2 10.4 0.0 1.0
06/13/2024 11:10 108.5 9.9 0.0 1.0
06/13/2024 11:11 108.7 9.8 0.0 1.0
06/13/2024 11:12 108.5 10.1 0.0 1.0
06/13/2024 11:13 108.6 10.1 0.0 1.0
06/13/2024 11:14 109.6 10.1 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 62 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 11:15 109.0 10.5 0.0 1.0
06/13/2024 11:16 109.4 10.0 0.0 1.0
06/13/2024 11:17 108.9 9.8 0.0 1.0
06/13/2024 11:18 108.9 9.2 0.0 1.0
06/13/2024 11:19 108.8 9.6 0.0 1.0
06/13/2024 11:20 107.8 10.0 0.0 1.0
06/13/2024 11:21 107.5 9.9 0.0 1.0
06/13/2024 11:22 109.6 9.7 0.0 1.0
06/13/2024 11:23 109.5 9.9 0.0 1.0
06/13/2024 11:24 109.7 10.5 0.0 1.0
06/13/2024 11:25 109.3 10.0 0.0 1.0
06/13/2024 11:26 108.0 10.3 0.0 1.0
06/13/2024 11:27 108.9 10.4 0.0 1.0
06/13/2024 11:28 108.6 9.9 0.0 1.0
06/13/2024 11:29 109.2 10.5 0.0 1.0
06/13/2024 11:30 109.4 10.5 0.0 1.0
06/13/2024 11:31 108.7 10.6 0.0 1.0
06/13/2024 11:32 108.6 10.2 0.0 1.0
06/13/2024 11:33 108.3 10.0 0.0 1.0
06/13/2024 11:34 109.5 10.1 0.0 1.0
06/13/2024 11:35 108.2 10.3 0.0 1.0
06/13/2024 11:36 108.3 10.2 0.0 1.0
06/13/2024 11:37 109.0 10.6 0.0 1.0
06/13/2024 11:38 109.1 10.1 0.0 1.0
06/13/2024 11:39 110.2 10.6 0.0 1.0
06/13/2024 11:40 109.7 10.4 0.0 1.0
06/13/2024 11:41 109.0 10.1 0.0 1.0
06/13/2024 11:42 108.1 10.3 0.0 1.0
06/13/2024 11:43 108.1 9.6 0.0 1.0
06/13/2024 11:44 107.6 9.3 0.0 1.0
06/13/2024 11:45 108.7 9.3 0.0 1.0
06/13/2024 11:46 108.9 9.3 0.0 1.0
06/13/2024 11:47 108.9 9.1 0.0 1.0
06/13/2024 11:48 109.3 9.4 0.0 1.0
06/13/2024 11:49 109.3 10.0 0.0 1.0
06/13/2024 11:50 108.6 10.0 0.0 1.0
06/13/2024 11:51 108.9 10.3 0.0 1.0
06/13/2024 11:52 109.1 10.2 0.0 1.0
06/13/2024 11:53 109.5 9.5 0.0 1.0
06/13/2024 11:54 108.0 10.6 0.0 1.0
Average
Max
Min
Count
108.8
110.2
107.5
130
10.2
11.3
9.1
130
0
0
0
130
1
1
1
130
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 63 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 12:10 108.9 10.1 0.0 1.0
06/13/2024 12:11 109.3 11.0 0.0 1.0
06/13/2024 12:12 109.5 10.2 0.0 1.0
06/13/2024 12:13 108.9 10.5 0.0 1.0
06/13/2024 12:14 109.1 11.2 0.0 1.0
06/13/2024 12:15 108.0 10.9 0.0 1.0
06/13/2024 12:16 107.7 10.8 0.0 1.0
06/13/2024 12:17 108.5 11.5 0.0 1.0
06/13/2024 12:18 108.4 10.7 0.0 1.0
06/13/2024 12:19 109.0 11.3 0.0 1.0
06/13/2024 12:20 109.0 10.8 0.0 1.0
06/13/2024 12:21 109.0 10.4 0.0 1.0
06/13/2024 12:22 108.7 10.3 0.0 1.0
06/13/2024 12:23 108.1 10.2 0.0 1.0
06/13/2024 12:24 108.5 10.5 0.0 1.0
06/13/2024 12:25 109.2 10.5 0.0 1.0
06/13/2024 12:26 109.6 11.0 0.0 1.0
06/13/2024 12:27 109.5 10.8 0.0 1.0
06/13/2024 12:28 109.1 11.1 0.0 1.0
06/13/2024 12:29 109.3 10.9 0.0 1.0
06/13/2024 12:30 108.9 11.2 0.0 1.0
06/13/2024 12:31 108.6 10.5 0.0 1.0
06/13/2024 12:32 108.1 10.3 0.0 1.0
06/13/2024 12:33 107.9 10.0 0.0 1.0
06/13/2024 12:34 108.5 10.2 0.0 1.0
06/13/2024 12:35 108.6 10.3 0.0 1.0
06/13/2024 12:36 108.1 10.7 0.0 1.0
06/13/2024 12:37 108.7 10.6 0.0 1.0
06/13/2024 12:38 108.5 10.6 0.0 1.0
06/13/2024 12:39 109.0 10.7 0.0 1.0
06/13/2024 12:40 108.7 10.9 0.0 1.0
06/13/2024 12:41 110.2 11.5 0.0 1.0
06/13/2024 12:42 109.6 11.2 0.0 1.0
06/13/2024 12:43 108.8 11.8 0.0 1.0
06/13/2024 12:44 109.0 11.0 0.0 1.0
06/13/2024 12:45 108.1 11.5 0.0 1.0
06/13/2024 12:46 108.3 10.7 0.0 1.0
06/13/2024 12:47 108.4 10.8 0.0 1.0
06/13/2024 12:48 108.5 10.9 0.0 1.0
06/13/2024 12:49 108.8 11.2 0.0 1.0
06/13/2024 12:50 109.2 10.8 0.0 1.0
06/13/2024 12:51 109.7 11.3 0.0 1.0
06/13/2024 12:52 108.8 10.8 0.0 1.0
06/13/2024 12:53 109.1 10.8 0.0 1.0
06/13/2024 12:54 109.2 10.4 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 64 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 12:55 108.4 11.2 0.0 1.0
06/13/2024 12:56 108.3 10.4 0.0 1.0
06/13/2024 12:57 107.9 10.4 0.0 1.0
06/13/2024 12:58 108.8 10.3 0.0 1.0
06/13/2024 12:59 109.1 10.4 0.0 1.0
06/13/2024 13:00 109.2 10.1 0.0 1.0
06/13/2024 13:01 108.4 10.7 0.0 1.0
06/13/2024 13:02 109.2 10.1 0.0 1.0
06/13/2024 13:03 108.7 10.9 0.0 1.0
06/13/2024 13:04 107.8 11.3 0.0 1.0
06/13/2024 13:05 108.5 11.1 0.0 1.0
06/13/2024 13:06 108.1 10.6 0.0 1.0
06/13/2024 13:07 108.8 11.6 0.0 1.0
06/13/2024 13:08 109.0 11.0 0.0 1.0
06/13/2024 13:09 109.1 10.2 0.0 1.0
06/13/2024 13:10 108.9 10.9 0.0 1.0
06/13/2024 13:11 108.7 10.5 0.0 1.0
06/13/2024 13:12 108.9 10.6 0.0 1.0
06/13/2024 13:13 108.7 10.3 0.0 1.0
06/13/2024 13:14 108.9 9.9 0.0 1.0
06/13/2024 13:15 109.1 10.5 0.0 1.0
06/13/2024 13:16 108.9 11.2 0.0 1.0
06/13/2024 13:17 109.0 11.1 0.0 1.0
06/13/2024 13:18 108.9 11.3 0.0 1.0
06/13/2024 13:19 108.7 10.9 0.0 1.0
06/13/2024 13:20 108.1 11.2 0.0 1.0
06/13/2024 13:21 107.8 10.8 0.0 1.0
06/13/2024 13:22 108.9 10.7 0.0 1.0
06/13/2024 13:23 109.5 10.7 0.0 1.0
06/13/2024 13:24 109.8 11.0 0.0 1.0
06/13/2024 13:25 109.8 10.8 0.0 1.0
06/13/2024 13:26 108.9 10.3 0.0 1.0
06/13/2024 13:27 108.4 10.4 0.0 1.0
06/13/2024 13:28 107.8 10.4 0.0 1.0
06/13/2024 13:29 108.9 10.9 0.0 1.0
06/13/2024 13:30 109.0 10.8 0.0 1.0
06/13/2024 13:31 109.0 11.0 0.0 1.0
06/13/2024 13:32 109.3 10.7 0.0 1.0
06/13/2024 13:33 109.3 11.0 0.0 1.0
06/13/2024 13:34 108.1 10.7 0.0 1.0
06/13/2024 13:35 107.5 10.9 0.0 1.0
06/13/2024 13:36 107.7 10.4 0.0 1.0
06/13/2024 13:37 108.6 10.5 0.0 1.0
06/13/2024 13:38 108.9 9.8 0.0 1.0
06/13/2024 13:39 109.1 10.2 0.0 1.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 65 of 315 ©Mostardi Platt
Date/Time
KILN:
CLINKER
(TNHR)
Expression
Value
KILN:
PM_BACK
(PCT)
Raw
Value
RAW_MILL_
OFF
(BITMASK)
Raw
Value
RAW_MILL_
ON
(BITMASK)
Raw
Value
06/13/2024 13:40 109.5 10.8 0.0 1.0
06/13/2024 13:41 109.2 11.2 0.0 1.0
06/13/2024 13:42 108.9 10.5 0.0 1.0
06/13/2024 13:43 108.7 10.6 0.0 1.0
06/13/2024 13:44 109.0 10.3 0.0 1.0
06/13/2024 13:45 109.2 10.7 0.0 1.0
06/13/2024 13:46 109.3 10.8 0.0 1.0
06/13/2024 13:47 109.0 10.3 0.0 1.0
06/13/2024 13:48 109.2 10.7 0.0 1.0
06/13/2024 13:49 109.1 10.1 0.0 1.0
06/13/2024 13:50 108.0 10.8 0.0 1.0
06/13/2024 13:51 108.0 10.3 0.0 1.0
06/13/2024 13:52 108.0 10.1 0.0 1.0
06/13/2024 13:53 109.0 10.4 0.0 1.0
06/13/2024 13:54 108.3 11.2 0.0 1.0
06/13/2024 13:55 109.3 11.2 0.0 1.0
06/13/2024 13:56 109.5 11.1 0.0 1.0
06/13/2024 13:57 108.7 11.3 0.0 1.0
06/13/2024 13:58 108.4 10.8 0.0 1.0
06/13/2024 13:59 108.7 10.7 0.0 1.0
06/13/2024 14:00 108.7 11.6 0.0 1.0
06/13/2024 14:01 108.6 11.0 0.0 1.0
06/13/2024 14:02 108.7 11.2 0.0 1.0
06/13/2024 14:03 109.5 10.7 0.0 1.0
06/13/2024 14:04 108.7 11.0 0.0 1.0
06/13/2024 14:05 108.9 11.1 0.0 1.0
06/13/2024 14:06 108.7 11.1 0.0 1.0
06/13/2024 14:07 107.9 11.2 0.0 1.0
06/13/2024 14:08 108.3 11.3 0.0 1.0
06/13/2024 14:09 108.6 11.5 0.0 1.0
06/13/2024 14:10 109.6 10.8 0.0 1.0
06/13/2024 14:11 108.8 10.6 0.0 1.0
06/13/2024 14:12 109.1 10.9 0.0 1.0
06/13/2024 14:13 109.3 10.7 0.0 1.0
06/13/2024 14:14 108.9 10.9 0.0 1.0
06/13/2024 14:15 108.7 10.7 0.0 1.0
06/13/2024 14:16 108.1 10.9 0.0 1.0
06/13/2024 14:17 108.0 10.1 0.0 1.0
06/13/2024 14:18 109.2 10.0 0.0 1.0
06/13/2024 14:19 109.6 14.2 0.0 1.0
Average
Max
Min
Count
108.8
110.2
107.5
130
10.8
14.2
9.8
130
0
0
0
130
1
1
1
130
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 66 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 07:30 5.8 107.2
06/13/2024 07:31 5.7 106.5
06/13/2024 07:32 5.9 106.6
06/13/2024 07:33 5.6 106.4
06/13/2024 07:34 6.0 106.1
06/13/2024 07:35 5.9 106.9
06/13/2024 07:36 5.7 107.1
06/13/2024 07:37 6.8 107.3
06/13/2024 07:38 6.2 107.2
06/13/2024 07:39 5.9 107.3
06/13/2024 07:40 5.8 106.8
06/13/2024 07:41 6.0 106.6
06/13/2024 07:42 6.0 106.2
06/13/2024 07:43 5.8 106.2
06/13/2024 07:44 5.9 106.8
06/13/2024 07:45 5.7 108.0
06/13/2024 07:46 5.7 107.1
06/13/2024 07:47 5.8 107.9
06/13/2024 07:48 6.1 108.0
06/13/2024 07:49 6.4 107.1
06/13/2024 07:50 6.0 107.2
06/13/2024 07:51 5.9 107.1
06/13/2024 07:52 5.8 108.3
06/13/2024 07:53 5.7 108.4
06/13/2024 07:54 6.0 106.7
06/13/2024 07:55 5.9 107.3
06/13/2024 07:56 6.0 107.0
06/13/2024 07:57 5.9 106.9
06/13/2024 07:58 6.0 105.3
06/13/2024 07:59 6.2 106.7
06/13/2024 08:00 5.8 107.6
06/13/2024 08:01 6.2 106.8
06/13/2024 08:02 6.1 106.0
06/13/2024 08:03 6.1 106.3
06/13/2024 08:04 5.9 107.1
06/13/2024 08:05 6.0 107.2
06/13/2024 08:06 6.1 106.9
06/13/2024 08:07 6.0 106.9
06/13/2024 08:08 5.9 107.2
06/13/2024 08:09 6.6 107.2
06/13/2024 08:10 6.2 107.2
06/13/2024 08:11 6.2 107.5
06/13/2024 08:12 6.1 108.1
06/13/2024 08:13 6.1 107.5
06/13/2024 08:14 6.4 107.4
06/13/2024 08:15 6.1 107.4
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 67 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 08:16 6.4 107.3
06/13/2024 08:17 6.1 107.3
06/13/2024 08:18 5.9 108.4
06/13/2024 08:19 6.0 108.1
06/13/2024 08:20 6.2 107.2
06/13/2024 08:21 6.2 107.2
06/13/2024 08:22 6.3 107.3
06/13/2024 08:23 6.2 106.7
06/13/2024 08:24 6.2 107.2
06/13/2024 08:25 6.3 106.7
06/13/2024 08:26 6.2 107.0
06/13/2024 08:27 6.3 107.0
06/13/2024 08:28 6.4 107.7
06/13/2024 08:29 6.4 106.5
06/13/2024 08:30 6.4 107.0
06/13/2024 08:31 6.6 107.1
06/13/2024 08:32 6.4 107.2
06/13/2024 08:33 6.4 108.5
06/13/2024 08:34 6.8 108.7
06/13/2024 08:35 6.7 108.3
06/13/2024 08:36 6.5 107.5
06/13/2024 08:37 6.7 106.8
06/13/2024 08:38 6.3 107.3
06/13/2024 08:39 6.3 107.3
06/13/2024 08:40 6.8 108.5
06/13/2024 08:41 7.0 108.1
06/13/2024 08:42 7.3 108.5
06/13/2024 08:43 6.5 108.9
06/13/2024 08:44 6.5 107.4
06/13/2024 08:45 6.4 107.7
06/13/2024 08:46 6.5 107.3
06/13/2024 08:47 6.4 107.0
06/13/2024 08:48 6.3 107.9
06/13/2024 08:49 6.2 108.1
06/13/2024 08:50 6.4 108.9
06/13/2024 08:51 6.3 109.1
06/13/2024 08:52 6.3 108.7
06/13/2024 08:53 6.4 107.3
06/13/2024 08:54 6.4 108.1
06/13/2024 08:55 6.3 108.0
06/13/2024 08:56 6.2 107.9
06/13/2024 08:57 6.4 109.0
06/13/2024 08:58 6.2 108.6
06/13/2024 08:59 6.2 108.9
06/13/2024 09:00 6.2 108.9
06/13/2024 09:01 6.3 109.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 68 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 09:02 6.5 108.8
06/13/2024 09:03 6.5 108.3
06/13/2024 09:04 6.4 107.9
06/13/2024 09:05 6.5 108.2
06/13/2024 09:06 7.0 108.1
06/13/2024 09:07 6.9 109.0
06/13/2024 09:08 6.6 108.9
06/13/2024 09:09 6.8 108.3
06/13/2024 09:10 7.0 108.4
06/13/2024 09:11 6.7 109.0
06/13/2024 09:12 6.6 109.0
06/13/2024 09:13 6.7 109.5
06/13/2024 09:14 7.1 109.1
06/13/2024 09:15 6.8 108.9
06/13/2024 09:16 7.2 109.0
06/13/2024 09:17 6.7 108.4
06/13/2024 09:18 6.9 108.0
06/13/2024 09:19 6.6 108.0
06/13/2024 09:20 6.7 108.8
06/13/2024 09:21 6.8 109.4
06/13/2024 09:22 6.9 109.0
06/13/2024 09:23 6.9 109.9
06/13/2024 09:24 6.8 108.7
06/13/2024 09:25 6.6 108.5
06/13/2024 09:26 6.4 108.3
06/13/2024 09:27 6.4 107.5
06/13/2024 09:28 6.5 108.5
06/13/2024 09:29 6.6 108.3
06/13/2024 09:30 6.4 108.9
06/13/2024 09:31 6.4 109.4
06/13/2024 09:32 6.3 109.1
06/13/2024 09:33 6.8 109.6
Average
Max
Min
Count
6.3
7.3
5.6
124
107.8
109.9
105.3
124
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 69 of 315 ©Mostardi Platt
Date/Time
CLINKER
(TNHR)
Expression
Value
PM_BACK
(PCT)
Raw
Value
06/13/2024 09:45 108.6 10.7
06/13/2024 09:46 108.1 10.4
06/13/2024 09:47 108.8 10.4
06/13/2024 09:48 109.2 9.9
06/13/2024 09:49 108.9 11.1
06/13/2024 09:50 108.9 11.0
06/13/2024 09:51 108.9 10.4
06/13/2024 09:52 108.4 10.4
06/13/2024 09:53 108.9 10.1
06/13/2024 09:54 108.3 10.7
06/13/2024 09:55 108.7 10.5
06/13/2024 09:56 109.0 10.0
06/13/2024 09:57 108.4 10.1
06/13/2024 09:58 108.6 10.2
06/13/2024 09:59 108.5 10.1
06/13/2024 10:00 108.5 10.0
06/13/2024 10:01 108.7 9.7
06/13/2024 10:02 108.1 10.1
06/13/2024 10:03 108.6 9.5
06/13/2024 10:04 108.8 10.2
06/13/2024 10:05 109.0 9.7
06/13/2024 10:06 109.0 10.3
06/13/2024 10:07 108.2 10.0
06/13/2024 10:08 108.5 10.4
06/13/2024 10:09 108.9 10.7
06/13/2024 10:10 109.2 10.7
06/13/2024 10:11 110.1 10.6
06/13/2024 10:12 109.3 10.6
06/13/2024 10:13 109.1 11.3
06/13/2024 10:14 108.4 10.4
06/13/2024 10:15 108.4 10.0
06/13/2024 10:16 108.5 10.0
06/13/2024 10:17 108.5 9.6
06/13/2024 10:18 109.2 9.9
06/13/2024 10:19 108.6 10.6
06/13/2024 10:20 108.8 10.1
06/13/2024 10:21 109.0 10.3
06/13/2024 10:22 108.7 10.3
06/13/2024 10:23 108.1 10.0
06/13/2024 10:24 108.8 10.2
06/13/2024 10:25 108.5 10.1
06/13/2024 10:26 109.5 10.1
06/13/2024 10:27 109.1 10.0
06/13/2024 10:28 109.8 10.1
06/13/2024 10:29 108.9 9.9
06/13/2024 10:30 109.1 10.2
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 70 of 315 ©Mostardi Platt
Date/Time
CLINKER
(TNHR)
Expression
Value
PM_BACK
(PCT)
Raw
Value
06/13/2024 10:31 108.8 10.3
06/13/2024 10:32 108.8 10.3
06/13/2024 10:33 109.2 10.2
06/13/2024 10:34 108.8 11.0
06/13/2024 10:35 109.3 10.2
06/13/2024 10:36 109.2 10.5
06/13/2024 10:37 109.2 10.6
06/13/2024 10:38 108.5 10.1
06/13/2024 10:39 108.4 9.8
06/13/2024 10:40 108.8 10.2
06/13/2024 10:41 108.5 10.1
06/13/2024 10:42 108.9 10.4
06/13/2024 10:43 108.7 10.4
06/13/2024 10:44 108.7 9.9
06/13/2024 10:45 108.7 9.6
06/13/2024 10:46 108.3 10.1
06/13/2024 10:47 107.9 10.0
06/13/2024 10:48 108.8 10.2
06/13/2024 10:49 110.2 9.6
06/13/2024 10:50 109.6 9.8
06/13/2024 10:51 109.5 10.1
06/13/2024 10:52 108.4 10.0
06/13/2024 10:53 108.4 10.1
06/13/2024 10:54 108.3 9.8
06/13/2024 10:55 108.5 9.6
06/13/2024 10:56 107.8 10.0
06/13/2024 10:57 109.5 10.5
06/13/2024 10:58 109.0 11.1
06/13/2024 10:59 109.1 10.7
06/13/2024 11:00 108.9 11.0
06/13/2024 11:01 107.9 10.3
06/13/2024 11:02 108.2 10.8
06/13/2024 11:03 108.4 10.1
06/13/2024 11:04 108.4 9.8
06/13/2024 11:05 108.7 9.8
06/13/2024 11:06 108.4 9.8
06/13/2024 11:07 109.2 9.7
06/13/2024 11:08 108.7 10.6
06/13/2024 11:09 109.2 10.4
06/13/2024 11:10 108.5 9.9
06/13/2024 11:11 108.7 9.8
06/13/2024 11:12 108.5 10.1
06/13/2024 11:13 108.6 10.1
06/13/2024 11:14 109.6 10.1
06/13/2024 11:15 109.0 10.5
06/13/2024 11:16 109.4 10.0
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 71 of 315 ©Mostardi Platt
Date/Time
CLINKER
(TNHR)
Expression
Value
PM_BACK
(PCT)
Raw
Value
06/13/2024 11:17 108.9 9.8
06/13/2024 11:18 108.9 9.2
06/13/2024 11:19 108.8 9.6
06/13/2024 11:20 107.8 10.0
06/13/2024 11:21 107.5 9.9
06/13/2024 11:22 109.6 9.7
06/13/2024 11:23 109.5 9.9
06/13/2024 11:24 109.7 10.5
06/13/2024 11:25 109.3 10.0
06/13/2024 11:26 108.0 10.3
06/13/2024 11:27 108.9 10.4
06/13/2024 11:28 108.6 9.9
06/13/2024 11:29 109.2 10.5
06/13/2024 11:30 109.4 10.5
06/13/2024 11:31 108.7 10.6
06/13/2024 11:32 108.6 10.2
06/13/2024 11:33 108.3 10.0
06/13/2024 11:34 109.5 10.1
06/13/2024 11:35 108.2 10.3
06/13/2024 11:36 108.3 10.2
06/13/2024 11:37 109.0 10.6
06/13/2024 11:38 109.1 10.1
06/13/2024 11:39 110.2 10.6
06/13/2024 11:40 109.7 10.4
06/13/2024 11:41 109.0 10.1
06/13/2024 11:42 108.1 10.3
06/13/2024 11:43 108.1 9.6
06/13/2024 11:44 107.6 9.3
06/13/2024 11:45 108.7 9.3
06/13/2024 11:46 108.9 9.3
06/13/2024 11:47 108.9 9.1
06/13/2024 11:48 109.3 9.4
06/13/2024 11:49 109.3 10.0
06/13/2024 11:50 108.6 10.0
06/13/2024 11:51 108.9 10.3
06/13/2024 11:52 109.1 10.2
06/13/2024 11:53 109.5 9.5
06/13/2024 11:54 108.0 10.6
Average
Max
Min
Count
108.8
110.2
107.5
130
10.2
11.3
9.1
130
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 72 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 12:10 6.7 108.9
06/13/2024 12:11 6.8 109.3
06/13/2024 12:12 6.7 109.5
06/13/2024 12:13 6.8 108.9
06/13/2024 12:14 6.5 109.1
06/13/2024 12:15 7.1 108.0
06/13/2024 12:16 6.9 107.7
06/13/2024 12:17 7.0 108.5
06/13/2024 12:18 7.1 108.4
06/13/2024 12:19 7.0 109.0
06/13/2024 12:20 7.0 109.0
06/13/2024 12:21 6.8 109.0
06/13/2024 12:22 7.2 108.7
06/13/2024 12:23 7.1 108.1
06/13/2024 12:24 6.7 108.5
06/13/2024 12:25 6.7 109.2
06/13/2024 12:26 6.7 109.6
06/13/2024 12:27 6.4 109.5
06/13/2024 12:28 6.6 109.1
06/13/2024 12:29 6.6 109.3
06/13/2024 12:30 6.6 108.9
06/13/2024 12:31 6.7 108.6
06/13/2024 12:32 6.7 108.1
06/13/2024 12:33 6.6 107.9
06/13/2024 12:34 6.6 108.5
06/13/2024 12:35 6.8 108.6
06/13/2024 12:36 6.8 108.1
06/13/2024 12:37 6.6 108.7
06/13/2024 12:38 6.7 108.5
06/13/2024 12:39 7.0 109.0
06/13/2024 12:40 7.0 108.7
06/13/2024 12:41 7.1 110.2
06/13/2024 12:42 6.6 109.6
06/13/2024 12:43 6.7 108.8
06/13/2024 12:44 6.8 109.0
06/13/2024 12:45 6.7 108.1
06/13/2024 12:46 6.9 108.3
06/13/2024 12:47 7.4 108.4
06/13/2024 12:48 7.2 108.5
06/13/2024 12:49 6.6 108.8
06/13/2024 12:50 6.9 109.2
06/13/2024 12:51 7.9 109.7
06/13/2024 12:52 7.0 108.8
06/13/2024 12:53 6.3 109.1
06/13/2024 12:54 6.8 109.2
06/13/2024 12:55 7.1 108.4
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 73 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 12:56 6.8 108.3
06/13/2024 12:57 6.5 107.9
06/13/2024 12:58 6.7 108.8
06/13/2024 12:59 6.8 109.1
06/13/2024 13:00 6.6 109.2
06/13/2024 13:01 6.1 108.4
06/13/2024 13:02 6.7 109.2
06/13/2024 13:03 6.6 108.7
06/13/2024 13:04 6.6 107.8
06/13/2024 13:05 6.6 108.5
06/13/2024 13:06 6.6 108.1
06/13/2024 13:07 6.8 108.8
06/13/2024 13:08 7.1 109.0
06/13/2024 13:09 6.6 109.1
06/13/2024 13:10 6.6 108.9
06/13/2024 13:11 6.2 108.7
06/13/2024 13:12 6.8 108.9
06/13/2024 13:13 6.8 108.7
06/13/2024 13:14 6.5 108.9
06/13/2024 13:15 6.5 109.1
06/13/2024 13:16 6.8 108.9
06/13/2024 13:17 6.6 109.0
06/13/2024 13:18 6.8 108.9
06/13/2024 13:19 6.9 108.7
06/13/2024 13:20 6.5 108.1
06/13/2024 13:21 6.9 107.8
06/13/2024 13:22 7.2 108.9
06/13/2024 13:23 6.9 109.5
06/13/2024 13:24 6.8 109.8
06/13/2024 13:25 6.9 109.8
06/13/2024 13:26 6.2 108.9
06/13/2024 13:27 6.3 108.4
06/13/2024 13:28 6.6 107.8
06/13/2024 13:29 6.7 108.9
06/13/2024 13:30 6.7 109.0
06/13/2024 13:31 6.3 109.0
06/13/2024 13:32 6.6 109.3
06/13/2024 13:33 6.4 109.3
06/13/2024 13:34 6.6 108.1
06/13/2024 13:35 6.5 107.5
06/13/2024 13:36 6.3 107.7
06/13/2024 13:37 6.2 108.6
06/13/2024 13:38 6.1 108.9
06/13/2024 13:39 6.5 109.1
06/13/2024 13:40 6.8 109.5
06/13/2024 13:41 6.7 109.2
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 74 of 315 ©Mostardi Platt
Date/Time
PM_BACK
(PCT)
Raw
Value
CLINKER
(TNHR)
Expression
Value
06/13/2024 13:42 6.5 108.9
06/13/2024 13:43 6.7 108.7
06/13/2024 13:44 6.4 109.0
06/13/2024 13:45 6.6 109.2
06/13/2024 13:46 6.6 109.3
06/13/2024 13:47 6.6 109.0
06/13/2024 13:48 7.0 109.2
06/13/2024 13:49 6.7 109.1
06/13/2024 13:50 6.3 108.0
06/13/2024 13:51 6.5 108.0
06/13/2024 13:52 6.9 108.0
06/13/2024 13:53 7.1 109.0
06/13/2024 13:54 7.1 108.3
06/13/2024 13:55 7.0 109.3
06/13/2024 13:56 6.7 109.5
06/13/2024 13:57 6.7 108.7
06/13/2024 13:58 6.9 108.4
06/13/2024 13:59 6.7 108.7
06/13/2024 14:00 6.7 108.7
06/13/2024 14:01 7.1 108.6
06/13/2024 14:02 6.8 108.7
06/13/2024 14:03 6.7 109.5
06/13/2024 14:04 6.7 108.7
06/13/2024 14:05 6.9 108.9
06/13/2024 14:06 6.9 108.7
06/13/2024 14:07 6.6 107.9
06/13/2024 14:08 6.6 108.3
06/13/2024 14:09 6.9 108.6
06/13/2024 14:10 6.8 109.6
06/13/2024 14:11 6.6 108.8
06/13/2024 14:12 7.2 109.1
06/13/2024 14:13 7.0 109.3
06/13/2024 14:14 6.7 108.9
06/13/2024 14:15 8.4 108.7
06/13/2024 14:16 7.3 108.1
06/13/2024 14:17 7.1 108.0
06/13/2024 14:18 7.2 109.2
06/13/2024 14:19 7.4 109.6
Average
Max
Min
Count
6.8
8.4
6.1
130
108.8
110.2
107.5
130
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 75 of 315 ©Mostardi Platt
Appendix B - Test Section Diagrams
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 76 of 315 ©Mostardi Platt
GASEOUS TRAVERSE FOR ROUND DUCTS
( SO2, O2 and CO2)
1
Disturbance
Measurement
Site
Length
> 1/2 Dia.
Length
> 2 Dia.Disturbance
12 3
Project: Ash Grove Cement Company
Leamington Plant
Leamington, Utah
Test Location: Main Kiln Stack
Test Date: June 11 through 13, 2024
No. Sample Points: 3
Diameter: 132 Inches
Flue Area: 94.99 Square Feet
Upstream Diameters: 4.09 diameters
Downstream
Diameters: 5.45 diameters
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 77 of 315 ©Mostardi Platt
EQUAL AREA TRAVERSE FOR ROUND DUCTS
(PM)
3
2
1
4
Disturbance
Measurement
Site
Length
> 1/2 Dia.
Length
> 2 Dia.Disturbance
5
4
3
2
1
1
2
3
4
5
12345
12345
Project: Ash Grove Cement Company
Leamington Plant
Leamington, Utah
Test Location:
Test Dates:
No. Sample Points: 20
Diameter: 132 Inches
Flue Area: 94.99 Square Feet
Upstream Diameters: 4.09 diameters
Downstream
Diameters: 5.45 diameters
Main Kiln Stack
June 11 through 13, 2024
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 78 of 315 ©Mostardi Platt
GASEOUS TRAVERSE FOR ROUND DUCTS
(Hg)
1
Disturbance
Measurement
Site
Length
> 1/2 Dia.
Length
> 2 Dia.Disturbance
12 3
Project: Ash Grove Cement Company
Leamington Plant
Leamington, Utah
Test Location:
Test Date:
No. Sample Points: 3
Diameter: 29 Inches
Flue Area: 4.59 Square Feet
Upstream Diameters: 1.8
Downstream
Diameters: 6.3
Coal Mill Stack
June 13, 2024
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 79 of 315 ©Mostardi Platt
EQUAL AREA TRAVERSE FOR ROUND DUCTS
(PM)
2
1
Disturbance
Measurement
Site
Length
> 1/2 Dia.
Length
> 2 Dia.Disturbance
2
3
4
5
6
7
8
9
10
11
65432
78 910 12
1
11
1
12
Project: Ash Grove Cement Company
Leamington Plant
Leamington, Utah
Test Location:
Test Dates:
No. Sample Points: 24
Diameter: 29 Inches
Flue Area: 4.59 Square Feet
Upstream Diameters: 1.8
Downstream
Diameters: 6.3
Coal Mill Stack
June 13, 2024
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 80 of 315 ©Mostardi Platt
GASEOUS TRAVERSE FOR ROUND DUCTS
(PM)
3
2
1
4
Disturbance
Measurement
Site
Length
> 1/2 Dia.
Length
> 2 Dia.Disturbance
5
4
3
2
1
1
2
3
4
5
12345
1234 6
6
5
6
6
Project: Ash Grove Cement Company
Leamington Plant
Leamington, Utah
Test Location:
Test Date:
No. Sample Points: 24
Diameter: 105 Inches
Flue Area: 60.10 Square Feet
Upstream Diameters: 2.51
Downstream
Diameters: 3.43
Clinker Cooler Stack
June 13, 2024
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 81 of 315 ©Mostardi Platt
Appendix C - Sample Train Diagrams
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 82 of 315 ©Mostardi Platt
ATD-001 USEPA Method 2 Rev. 1.2 1/1/2021
USEPA Method 2 – Type S Pitot Tube Manometer Assembly
1.90-2.54 cm (0.75 -1.0 in.)*
7.62 cm (3 in.)*
Temperature Sensor
Manometer
Leak-Free
Connections
*Suggested (Interference Free)Pitot tube/ ThermocoupleSpacing
Ga
s

F
l
o
w

Flexible
Tubing (0.25 in.)
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 83 of 315 ©Mostardi Platt
ATD-012 Extractive 3A Rev. 1.3 1/1/2021
USEPA Method 3A Extractive Gaseous Sampling Diagram
Heated Probe
3-Way
Calibration “T”
Heated Line
Sample Gas Line
Calibration Gas Line

Sample Gas Manifold
Calibration
Gases
Data Acquisition and
Report Generation
Moisture
Removal
System
In-Line Filter
CO
CO2
O2/CO2
CO2
Gas Analyzer
Exhaust to Safe
Location
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 84 of 315 ©Mostardi Platt
ATD-035 USEPA Method 5 Rev. 1.2 1/1/2021
USEPA Method 5- Particulate Matter Sample Train Diagram
Nozzle
S-Type Pitot
Heated Probe Sheath
Filter Holder
Oven Box
Temperature Sensors
Ice Bath
Silica Gel Empty
100 mL each
DI H2O
Temperature Sensors
Manometer/Orifice
Incline Gauge
Vacuum
Gauge Vacuum Line
Dry Gas
Meter
Air Tight Pump
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 85 of 315 ©Mostardi Platt
ATD-061 USEPA Method 23 Rev. 1.2 1/1/2021
Method 23 - Determination of Polychlorinated Dibenzo-p-dioxins and
Polychlorinated Dibenzofurans from Municipal Waste Combustors
Glass or
Quartz
Nozzle
Teflon
Coated
Union
Heated Probe Sheath
Glass or Quartz Liner S-Type Pitot
Filter Holder
with M23
Prepared Filter
Temperature Sensor
Temperature Sensors
To “S” Bend
From Filter Holder
Condenser Coil
Oven Box
“S” Bend
Recirculation
Pump
XAD-2
Resin Trap
Empty
Large
Knockout
Impinger
100 mL
each
HPLC
H2O
Empty
Impinger
Silica
Ice
Bath Vacuum Line
Temperature Sensors
Dry Gas Meter
Manometer/Orifice
Incline Gauge
Vacuum Gauge
Air Tight Pump
Ice Water
Should
Remain
Below
Trap
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 86 of 315 ©Mostardi Platt
ATD-071 USEPA Method 30B Rev. 1.2 1/1/2021
USEPA Method 30B- Mercury Sorbent Trap Sampling Train
(Top View)
(Side View)
Probe
Sorbent
Traps
Temperature Sensor
Sample
Lines
Knockout
Buffer
Solution
Desiccant
Flow Meter Temperature

Vacuum Gauge
Totalizer
Display
Flow
Controls
Pump
Probe Temperature
Controller
Temperature
Display
Selector Knob
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 87 of 315 ©Mostardi Platt

USEPA Method 320 and 321 – Vapor Phase Organic and Inorganic
Emissions by Extractive Fourier Transform Infrared (FTIR)
Spectroscopy
Sample Train Diagram

Heated Wet
Sample

Heated

Extractive

Initial
Particulate

Calibration

Data Acquisition System
FTIR

FTIR Analyzer
Heated

Secondary

Heated

Orifice
Liquid
Nitrogen
Reservoir
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 88 of 315 ©Mostardi Platt
Appendix D - Calculation Nomenclature and Formulas
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 89 of 315 ©Mostardi Platt
Client:Facility:
Test Location:
Run:
Date:Method:
Source Condition:
Dry Molecular Weight
Md = 0.44 x (%CO2) + 0.32 x (%O2) + 0.28 x %N2
%CO2 = 13.7 %O2 = 10.2 %N2 = 76.1
Md = 30.600
Wet Molecular Weight
Ms = Md x (1-Bws) + (18.0 x Bws)
Md = 30.600 Bws = 0.106
Ms = 29.263
Meter Volume at Standard Conditions
Vm(std) = 17.647 x Y x Vm x (Pbar +DH/13.6)
Tm
Y = 0.990 Vm = 121.148 Pbar = 25.03DH = 2.56 Tm = 537.4
Vm(std) =99.318
Volume of Water Vapor Condensed
Vw(std) =0.0471 x (net H2O gain)
Net H2O = 250.4
Vw(std) = 11.794
Moisture Content
Bws =
Vw(std) = 11.794 Vm(std) = 99.318
Bws = 0.106
Ash Grove Cememnt Company Leamington Cement Plant
Main Kiln Stack
1
6/12/20245
Mill Off
Vw(std)
Vw(std) + Vm(std)
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 90 of 315 ©Mostardi Platt
Client:Facility:
Test Location:
Run:
Date:Method:
Source Condition:
Ash Grove Cememnt Company Leamington Cement Plant
Main Kiln Stack
1
6/12/20245
Mill Off
Average Duct Velocity
Vs = 85.49 x Cp x Sqrt DP (avg) x (Ts (avg) + 460/ (Ps x Ms))
1/2
Cp = 0.840 Ts (avg) = 346.2 Sqrt DP (avg): 0.712Ps = 24.99 Ms = 29.263
Vs = 53.671
Volumetric Flow Rate (Actual Basis)
Q = Vs x A x 60
Vs = 53.671 A = 95.033
Q = 306,032
Volumetric Flow Rate (Standard Basis)
Qstd = 17.647 x Q x Ps
Ts (avg) + 460
Q = 306,032 Ps = 24.99 Ts (avg) = 346.2
Qstd = 167,422
Volumetric Flow Rate (Standard Dry Basis)
Qstd(dry) = Qstd x (1-Bws)
Qstd = 167,422 Bws = 0.106
Qstd(dry) = 149,651
Isokinetic Variation:
%ISO =
Ts = 346.2 Vm(std) = 99.318 Vs = 53.671
An = 0.0005343 θ = 120 Ps = 24.99
Bws = 0.106
%ISO = 98.4
Vs x θ x An x Ps x (1-Bws)
0.0945 x (Ts +460) x Vm(std)
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 91 of 315 ©Mostardi Platt
Client:Facility:
Test Location:
Run:
Date:Method:
Source Condition:
Ash Grove Cememnt Company Leamington Cement Plant
Main Kiln Stack
1
6/12/20245
Mill Off
PM Concentration:
Co = mn x 15.43
Vm(std)
mn (g) = 0.00498 Vm(std) = 99.318
Co = 0.0008 gr/dscf
PM Emission Rate:
Emission Rate lb/hr = Co x Qstd(dry) x 60
7,000
Co = 0.0008 Qstd(dry) = 149,651
Emission Rate lb/hr = 0.992 lb/hr
This example represents the filterable fraction. For other fractions, use the obtained mn for that particulate
fraction.
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 92 of 315 ©Mostardi Platt
Client:Location:
Facility:Date:
Project #:
( 13.65 % - 0.00 %) x
( 10.15 % - 0.05 %) x
Cgas = (C - Co) x Cma
Cm - Co
where:
Cgas = Effluent gas concentration, dry basis, ppm
C = Average gas concentration indicated by gas analyzer, dry basis, ppm
Co = Average of initial and final system calibration bias check responses for the zero gas, ppm
Cm = Average of initital and final system calibration bias check responses for the upscale calibration gas, ppm
Cma = Actual concentration of the upscale calibration gas, ppm
CO2 % (dry)
O2 % (dry)
11.15 % - 0.05 %
11.26 %= 13.70 %11.20 % - 0.00 %
Sample Calculations
Ash Grove Cement Company
Leamington Cement Plant
M242413
Main Kiln Stack
6/12/24
11.24 %= 10.20 %
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 93 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Run:
Date:
Method:
Source Condition:
Dry Molecular Weight
Md = 0.44 x (%CO2) + 0.32 x (%O2) + 0.28 x %N2
%CO2 = 14.60 %O2 = 12.0 %N2 =73.4
Md = 30.816
Wet Molecular Weight
Ms = Md x (1-Bws) + (18.0 x Bws)
Md = 30.816 Bws = 0.140
Ms = 29.019
Meter Volume at Standard Conditions
Vm(std) = 17.647 x Y x Vm x (Pbar +DH/13.6)
Tm
Y = 0.995 Vm = 162.246 Pbar = 25.09
DH = 1.98 Tm = 536.4
Vm(std) =134.034
Volume of Water Vapor Condensed
Vw(std) = 0.0471 x (net H2O gain)
Net H2O = 464.0
Vw(std) = 21.854
Moisture Content
Bws =
Vw(std) = 21.854 Vm(std) = 134.034
Bws = 0.140
Vw(std)
Vw(std) + Vm(std)
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
1
6/11/2024
23
Mill On
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 94 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Run:
Date:
Method:
Source Condition:
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
1
6/11/2024
23
Mill On
Average Duct Velocity
Vs = 85.49 x Cp x Sqrt DP (avg) x (Ts (avg) + 460/ (Ps x Ms))
1/2
Cp = 0.840 Ts (avg) = 231.3 Sqrt DP (avg): 0.767
Ps = 25.05 Ms = 29.02
Vs = 53.703
Volumetric Flow Rate (Actual Basis)
Q = Vs x A x 60
Vs = 53.703 A = 95.033
Q = 306214
Volumetric Flow Rate (Standard Basis)
Qstd = 17.647 x Q x Ps
Ts (avg) + 460
Q = 306,214 Ps = 25.05 Ts (avg) = 231.3
Qstd = 195,769
Volumetric Flow Rate (Standard Dry Basis)
Qstd(dry) = Qstd x (1-Bws)
Qstd = 195,769 Bws = 0.140
Qstd(dry) =168,324
Isokinetic Variation:
%ISO =
Ts = 231.3 Vm(std) = 134.034 Vs = 53.703
An = 0.0004155 θ = 180.0 Ps = 25.05
Bws = 0.140
%ISO = 101.2
Vs x θ x An x Ps x (1-Bws)
0.0945 x (Ts + 460) x Vm(std)
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 95 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Run:
Date:
Method:
Source Condition:
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
1
6/11/2024
23
Mill On
PCDD/PCDF Concentration:
ng/m3=
ng= 0.11 Vm(std) = 134.034
ng/m3=0.03 O2% =12
ng/m3 @ 7% O2 =
ng/m3 @ 7% O2 = 1.87E-03
ng/m3 * (20.9-7.0)
(20.9-O2%)
ng of PCDD/PCDF
Vm(std) x 0.02832 m3/ft3
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 96 of 315 ©Mostardi Platt
Client:Location:
Facility:Date:
Project #:
( 5.9 ppm - 0.0 ppm) x
( 17.3 ppm - 0.1 ppm) x
Cgas = (C - Co) x Cma
Cm - Co
where:
Cgas = Effluent gas concentration, dry basis, ppm
C = Average gas concentration indicated by gas analyzer, dry basis, ppm
Co = Average of initial and final system calibration bias check responses for the zero gas, ppm
Cm = Average of initital and final system calibration bias check responses for the upscale calibration gas, ppm
Cma = Actual concentration of the upscale calibration gas, ppm
CO2 % (dry)
O2 % (dry)
11.5 ppm - 0.1 ppm
11.3 ppm = 5.90 %11.2 ppm - 0.0 ppm
Sample Calculations
Ash Grove Cement Company
Leamington Plant
M242413
Coal Mill
6/13/24
11.2 ppm = 17.00 %
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 97 of 315 ©Mostardi Platt
Client:
Plant:
Test Location:
Run:1A
Date:6/12/2024
Mercury Meter Volume at Standard Conditions (Liters)
Vm(std) = 17.647 x Y x Vm x Pbar
Tm
Y = 1.007 Vm = 60.042
Tm = 547.00
Vm(std) = 48.921
Hg Concentration:
ppb Hg =(ng of Hg /1x109) x (0.002046226/Vm(std)*0.0353)*385x106/200.59*1000
Total ng Hg = 43.9 Vm(std) = 48.921
ppb Hg = 0.108
ug/dscm = (total ng of Hg on trap/1000)/Vm(std)/1000
ug/dscm = 0.897
ug/wscm = ug/dscm*(1-Bws)
ug/wscm = 0.816
lb/hr = ((ug/wscm) / (1,000,000ug/g) / (453.592g/lb) / (35.3147 ft3/m3)) x scf/hr
lb/hr = (0.558 x 1,000,000/453.6/35.3147) x 770,760
lb/hr = 3.92E-05
lb/MMton of clinker = ((lb/hr) / tons of clinker/hr) x 1,000,000
lb/MMton of clinker = (0.0004/115.3) x 1,000,000
lb/MMton of clinker = 0.33
Ash Grove Cement Company
Leamington Plant
Coal Mill Stack
FT-008 Hg Template V5.0 10/31/17
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 98 of 315 ©Mostardi Platt
MOSTARDI PLATT
Volumetric Air Flow Calculations
𝑉𝑉𝑉𝑉 (𝑠𝑠𝑠𝑠𝑠𝑠) =17.647 × 𝑉𝑉𝑉𝑉× ��𝑃𝑃𝑏𝑏𝑏𝑏𝑏𝑏+�𝐷𝐷𝐷𝐷13.6��(460 +𝑇𝑇𝑉𝑉)�× 𝑌𝑌
𝑉𝑉𝑉𝑉 (𝑠𝑠𝑠𝑠𝑠𝑠)= 0.0471 × 𝑉𝑉𝑉𝑉𝑉𝑉
𝐵𝐵𝑉𝑉𝑠𝑠=�𝑉𝑉𝑉𝑉 (𝑠𝑠𝑠𝑠𝑠𝑠)𝑉𝑉𝑉𝑉 (𝑠𝑠𝑠𝑠𝑠𝑠)+𝑉𝑉𝑉𝑉 (𝑠𝑠𝑠𝑠𝑠𝑠)�
𝑀𝑀𝑠𝑠=(0.44 × %𝐶𝐶𝐶𝐶2)+(0.32 × %𝐶𝐶2)+[0.28 × (100 −%𝐶𝐶𝐶𝐶2 −%𝐶𝐶2)]
𝑀𝑀𝑠𝑠=𝑀𝑀𝑠𝑠× (1 −𝐵𝐵𝑉𝑉𝑠𝑠)+(18 × 𝐵𝐵𝑉𝑉𝑠𝑠)
𝑉𝑉𝑠𝑠=�(𝑇𝑇𝑠𝑠+460)𝑀𝑀𝑠𝑠× 𝑃𝑃𝑠𝑠× √𝐷𝐷𝑃𝑃× 𝐶𝐶𝐶𝐶× 85.49
𝐴𝐴𝑉𝑉𝐴𝐴𝑉𝑉=𝑉𝑉𝑠𝑠× 𝐴𝐴𝐴𝐴𝐴𝐴𝐴𝐴 (𝑜𝑜𝐴𝐴 𝑠𝑠𝑠𝑠𝐴𝐴𝑉𝑉𝑠𝑠 𝑜𝑜𝐴𝐴 𝑠𝑠𝑑𝑑𝑉𝑉𝑠𝑠) × 60
𝑆𝑆𝑉𝑉𝐴𝐴𝑉𝑉=𝐴𝐴𝑉𝑉𝐴𝐴𝑉𝑉× 17.647 × �𝑃𝑃𝑠𝑠(460 +𝑇𝑇𝑠𝑠)�
𝑆𝑆𝑉𝑉𝐴𝐴ℎ=𝑆𝑆𝑉𝑉𝐴𝐴𝑉𝑉× 60 𝑉𝑉𝑚𝑚𝑚𝑚ℎ𝐴𝐴
𝐷𝐷𝑠𝑠𝑉𝑉𝐴𝐴𝑉𝑉=𝑆𝑆𝑉𝑉𝐴𝐴𝑉𝑉× (1 −𝐵𝐵𝑉𝑉𝑠𝑠)
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 99 of 315 ©Mostardi Platt
MOISTURE CALCULATIONS
m(std)wsg(std)wc(std)
wsg(std)wc(std)
ws
m
bar
mm(std)
if
w std
stdifwsg(std)
if
wstd
stdwifwc(std)
VVV
VVB
T 13.6
HP
Y V 17.714V
)W(W 0.04715MP
T R )W(WV
)V0.04707(VMP
T R )V(VV
++
+=
∆+
=
−=−=
−=−=ρ
Where:
Bws = Water vapor in gas stream, proportion by volume
Mw = Molecular weight of water, 18.015 lb/lb-mole
Pbar = Barometric pressure at the testing site, in. Hg
Pstd = Standard absolute pressure, 29.92 in. Hg
R = Ideal gas constant, 0.048137 (in. Hg)(ft3)/(g-mole)(°R) =
[21.8348(in. Hg)(ft3)/(lb-mole)(°R)]/453.592 g-mole/lb-mole
Tm = Absolute average dry gas meter temperature, °R
Tstd = Standard absolute temperature, 530 °R
Vf = Final volume of condenser water, ml
Vi = Initial volume of condenser water, ml
Vm = Dry gas volume measured by dry gas meter, dcf
Vm(std) = Dry gas volume measured by dry gas meter, corrected to standard conditions, scf
Vwc(std) = Volume of condensed water vapor, corrected to standard conditions, scf
Vwsg(std) = Volume of water vapor collected in silica gel, corrected to standard conditions, scf
Wf = Final weight of silica gel, g
Wi = Initial weight of silica gel, g
Y = Dry gas meter calibration factor
∆H = Average pressure exerted on dry gas meter outlet by gas sample bag, in. H2O
ρw = Density of water, 0.9982 g/ml
13.6 = Specific gravity of mercury (Hg)
17.714 = Tstd/Pstd
0.04707 = ft3/ml 0.04715 = ft3/g
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 100 of 315 ©Mostardi Platt
MOSTARDI PLATT
Volumetric Flow Nomenclature
A = Cross-sectional area of stack or duct, ft2
Bws = Water vapor in gas stream, proportion by volume
Cp = Pitot tube coefficient, dimensionless
Md = Dry molecular weight of gas, lb/lb-mole
Ms = Molecular weight of gas, wet basis, lb/lb-mole
Mw = Molecular weight of water, 18.0 lb/lb-mole
Pbar = Barometric pressure at testing site, in. Hg
Pg = Static pressure of gas, in. Hg (in. H2O/13.6)
Ps = Absolute pressure of gas, in. Hg = Pbar + Pg
Pstd = Standard absolute pressure, 29.92 in. Hg
Qacfm = Actual volumetric gas flow rate, acfm
Qsd = Dry volumetric gas flow rate corrected to standard conditions, dscf/hr
R = Ideal gas constant, 21.85 in. Hg-ft3/°R-lb-mole
Ts = Absolute gas temperature, °R
Tstd = Standard absolute temperature, 530°R
vs = Gas velocity, ft/sec
Vw(std) = Volume of water vapor in gas sample, corrected to standard conditions, scf
Y = Dry gas meter calibration factor
∆p = Velocity head of gas, in. H2O
K1 = 17.714 °R/in. Hg
%EA = Percent excess air
%CO2 = Percent carbon dioxide by volume, dry basis
%O2 = Percent oxygen by volume, dry basis
%N2 = Percent nitrogen by volume, dry basis
0.264 = Ratio of O2 to N2 in air, v/v
0.28 = Molecular weight of N2 or CO, divided by 100
0.32 = Molecular weight of O2 divided by 100
0.44 = Molecular weight of CO2 divided by 100
13.6 = Specific gravity of mercury (Hg)
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 101 of 315 ©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.
CO2 – (X lbs/scf) x (Fc) x (100/CO2) = X lbs/mmBtu
O2 – (X lbs/scf) x (Fd) x (20.9/(20.9-O2)) = X lbs/mmBtu
Conversion Factors
NOx – 1.19396 x 10-7
CO – 7.2664 x 10-8
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 102 of 315 ©Mostardi Platt
CN&F-007 Correction of Pollutant to %O2 Rev. 2.2 1/1/2021
MOSTARDI PLATT
Pollutant Concentration Correction 7% for Percent Oxygen
𝐶𝐶𝑎𝑎𝑎𝑎𝑎𝑎=𝐶𝐶𝑎𝑎20.9 −7%20.9 −%𝑂𝑂2
where:
Cadj = Pollutant concentration corrected to percent O2
20.9 - 7% = Percent O2, the defined O2 correction value, percent
20.9 = Percent O2 in air
%O2 = Measured O2 concentration dry basis, percent
Cd = Pollutant concentration measured, dry basis, ppm.
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 103 of 315 ©Mostardi Platt
CN&F-003A Isokinetic Particulates Rev. 1.2 1/1/2021
MOSTARDI PLATT
Isokinetic Calculation Formulas
1. lc2std
std
w
wlcw(std)VKP
RT
MVV =







=ρ
2.
m
bar
m1std
bar
m
stdmm(std)T
))13.6
H((P
Y VK P
))13.6
H((P
T
TY VV
∆+
=





∆+


=
3. )V(V
VB
w(std)m(std)
w(std)
ws +=
4.)0.28(%N)0.32(%O)0.44(%COM 222d++=
5.)18.0(B)B(1MM wswsds+−=
6.
aa
aaV
mCρ=
7.aawaaVCWρ=
8. 





+=
sm(std)w(std)
sniacf T VV
Pm15.43KC
9.)Vm( )gramgrains 15.43(C m(std)nS=
10.
ss
sppsMP
T PCKv∆=
11.)A(60vQsec/minsacfm=
12. A PT
PTv )B)(1(3600Q
stds
sstdswssec/hrsd 

−=
13.()lbgrains 7000CQ )hrlbs rate, (emission E sstd=
14. ( )( )wsnss
m(std)s4wssnsstd
stdm(std)s
B1AvP
VTKB160PAvT
PVTIKV −=−=θθ
15. 100%CO) 0.5(%O%N 0.264
%CO) (0.5%O%EA
22
2 ×


−−
−=
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 104 of 315 ©Mostardi Platt
CN&F-023A Isokinetic Nomenclature Rev. 1.2 1/1/2021
MOSTARDI PLATT
Isokinetic Nomenclature
A = Cross-sectional area of stack or duct, square feet
An = Cross-sectional area of nozzle, square feet
Bws = Water vapor in gas stream, by volume
Ca = Acetone blank residue concentration, g/g
Cacf = Concentration of particulate matter in gas stream at actual conditions, gr/acf
Cp = Pitot tube coefficient
Cs = Concentration of particulate matter in gas stream, dry basis, corrected to standard conditions, gr/dscf
IKV = Isokinetic sampling variance, must be 90.0 % ≤ IKV ≤ 110.0%
Md = Dry molecular weight of gas, lb/lb-mole
Ms = Molecular weight of gas, wet basis, lb/lb-mole
Mw = Molecular weight of water, 18.0 lb/lb-mole
ma = Mass of residue of acetone after evaporation, grams
Pbar = Barometric pressure at testing site, inches mercury
Pg = Static pressure of gas, inches mercury (inches water/13.6)
Ps = Absolute pressure of gas, inches mercury = Pbar + Pg
Pstd = Standard absolute pressure, 29.92 inches mercury
Qacfm = Actual volumetric gas flow rate, acfm
Qsd = Dry volumetric gas flow rate corrected to standard conditions, dscfh
R = Ideal gas constant, 21.85 inches mercury cubic foot/°R-lb-mole
Tm = Dry gas meter temperature, °R
Ts = Gas temperature, °R
Tstd = Absolute temperature, 528°R
Va = Volume of acetone blank, ml
Vaw = Volume of acetone used in wash, ml
Wa = Weight of residue in acetone wash, grams
mn = Total amount of particulate matter collected, grams
V1c = Total volume of liquid collected in impingers and silica gel, ml
Vm = Volume of gas sample as measured by dry gas meter, dcf
Vm(std) = Volume of gas sample measured by dry gas meter, corrected to standard conditions, dscf
vs = Gas velocity, ft/sec
Vw(std) = Volume of water vapor in gas sample, corrected to standard conditions, scf
Y = Dry gas meter calibration factor
∆H = Average pressure differential across the orifice meter, inches water
∆p = Velocity head of gas, inches water
ρa = Density of acetone, 0.7855 g/ml (average)
ρw = Density of water, 0.002201 lb/ml
θ = Total sampling time, minutes
K1 = 17.647 °R/in. Hg
K2 = 0.04707 ft3/ml
K4 = 0.09450/100 = 0.000945
Kp = Pitot tube constant, 85.49 𝑓𝑓𝑠𝑠𝑠�(𝑙𝑙𝑙𝑙⁄−𝑚𝑚𝑙𝑠)(𝑖𝑖. 𝐻𝐻)(°𝑅)(𝑖𝑖. 𝐻2𝑂)�1 2�
%EA = Percent excess air
%CO2 = Percent carbon dioxide by volume, dry basis
%O2 = Percent oxygen by volume, dry basis
%CO = Percent carbon monoxide by volume, dry basis
%N2 = Percent nitrogen by volume, dry basis
0.264 = Ratio of O2 to N2 in air, v/v
28 = Molecular weight of N2 or CO
32 = Molecular weight of O2
44 = Molecular weight of CO2
13.6 = Specific gravity of mercury (Hg)
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 105 of 315 ©Mostardi Platt
CN&F-018A Mercury Sample Analysis Calcs Rev. 1.1 1/1/2021
MOSTARDI PLATT
Mercury Sample Analysis Calculations
Spike Recovery (Analytical Bias Test)
R =Mrecovered
Mspiked x 100
% Breakthrough
B =m2
m1 x 100
Hg Concentration
Ca =(m1 +m2)
Vt
Moisture Correction
Cw =Cd x (1 −Bws)
Paired Trap Agreement
RD =|Ca −Cb|
Ca +Cb x 100
Measured Spike Hg Concentration
Crec =m𝑠
vs − mu
vu
Spiked Hg Recovery
R =Crec x vs
Mspiked x 100
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 106 of 315 ©Mostardi Platt
CN&F-046 SSOL Nomenclature Rev. 0.1 1/1/2021
MOSTARDI PLATT
Site Specific Operating Limit (SSOL) Nomenclature
ECm = Combined hourly emission rate of PM from the kiln and bypass stack and/or inline coal mill, lb/ton of kiln clinker production
EK = Hourly emissions of PM emissions from the kiln, lb
EB = Hourly PM emissions from the alkali bypass stack, lb
EC = Hourly PM emissions from the inline coal mill stack, lb
Ol = The operating limit for your PM CPMS on a 30-day rolling average, in milliamps or the digital equivalent.
L = Your source emission limit expressed in lb/ton clinker
P = Hourly clinker production, tons
R = The relative lb/ton-clinker per milliamp or digital equivalent for your PM CPMS
Y1 = The three run average lb/ton-clinker PM concentration
X1 = The three run average milliamp or digital equivalent output from the PM CPMS
z = The milliamp or digital equivalent of instrument zero determined
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 107 of 315 ©Mostardi Platt
Appendix F - Laboratory Sample Analysis
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 108 of 315 ©Mostardi Platt
Client:
Facility:
Project Number:
Test Location:
Test Method:Filter Drying Temp oF: 220
Filterable Analysis Date: Analyst:LNT
Condensable Analysis Date: Analyst:LNT
Sample Date ID#Initial Weight
(grams)
Final Weight
(grams)
Run 1 6/13/2024
Source Condition:Normal
M5 Filter 10524 0.45457 0.45511 0.00054
Acetone Wash (M5 Pans)16523 50 mL 5.01460 5.01482 ≤0.00025
Acetone Blank ≤0.00025
Total Filterable Weight ≤0.00079
Acetone/Hexane Wash 16008 225 mL 21.09582 21.09596 ≤0.00025
DI Wash 16561 175 mL 21.29863 21.30129 0.00266
NH4OH Correction mL 0.00000
Field Blank ≤0.00025Total Condensable Weight ≤0.00266
Total Particulate Weight ≤0.00345
Run 2 6/13/2024
Source Condition: Normal
M5 Filter 10526 0.45195 0.45240 0.00045
Acetone Wash (M5 Pans) 16534 60 mL 4.96322 4.96357 0.00035
Acetone Blank ≤0.00025
Total Filterable Weight 0.00080
Run 3 6/13/2024
Source Condition: Normal
M5 Filter 9258 0.45206 0.45307 0.00101
Acetone Wash (M5 Pans) 16524 50 mL 5.03261 5.03612 0.00351
Acetone Blank ≤0.00025
Total Filterable Weight 0.00452
Run 4 6/13/2024
Source Condition: Spiked
M5 Filter 15538 0.45985 0.45999 ≤0.00015
Acetone Wash (M5 Pans) 16525 60 mL 5.00237 5.00736 0.00499
Acetone Blank ≤0.00025
Total Filterable Weight ≤0.00514
Acetone/Hexane Wash 16010 100 mL 20.99824 20.99828 ≤0.00025
DI Wash 16560 120 mL 20.96725 20.96727 ≤0.00025
NH4OH Correction 0 mL 0.00000
Total Field Train Blank ≤0.00025
Acetone/Hexane Wash 16011 150 mL 21.05796 21.05799 ≤0.00025
DI Wash 16558 110 mL 21.00367 21.00376 ≤0.00025
Acetone Wash (M5 Pans) 16422 100 mL 4.96193 4.96079 ≤0.00025
Media
M5 Filter
Acetone Wash (M5 Pans)
Sample Vials (M202)
Filterable Particulate
Filterable Particulate
Filterable Particulate
Condensable Particulate
Ash Grove Cement Company
Leamington Cement Plant
M242413
Clinker Cooler Stack
5
6/20/2024
6/21/2024
0.00008
0.00015
0.00025
0.00025
vol. (ml)Description Net Weight Gain (grams)
Reagent Blank Summary
Field Proof Blank Summary
0.00008
Filterable Particulate
Field Train Blank Summary
RDL/MDL Summary
MDL, grams RDL, grams
0.00005
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 109 of 315 ©Mostardi Platt
Client:
Facility:
Project Number:
Test Location:
Test Method:Filter Drying Temp oF: 220
Filterable Analysis Date: Analyst:LNT
Sample Date ID#Initial Weight
(grams)
Final Weight
(grams)
Run 1 6/12/2024
Source Condition:Mill Off
M5 Filter 15524 0.46178 0.46619 0.00441
Acetone Wash (M5 Pans)16529 75 mL 4.99882 4.99939 0.00057
Acetone Blank ≤0.00025
Total Filterable Weight 0.00498
Run 2 6/12/2024
Source Condition:Mill Off
M5 Filter 15526 0.46254 0.46504 0.00250
Acetone Wash (M5 Pans)16530 60 mL 4.97374 4.97562 0.00188
Acetone Blank ≤0.00025
Total Filterable Weight 0.00438
Run 3 6/12/2024
Source Condition:Mill Off
M5 Filter 14851 0.46648 0.46690 0.00042
Acetone Wash (M5 Pans)16531 50 mL 4.96696 4.96869 0.00173
Acetone Blank ≤0.00025
Total Filterable Weight 0.00215
Acetone Wash (M5 Pans)16422 100 mL 4.96193 4.96079 ≤0.00025
Media
M5 Filter
Acetone Wash (M5 Pans)
Sample Vials (M202)
0.00008
RDL/MDL Summary
MDL, grams RDL, grams
0.00005
0.00008
0.00015
0.00025
0.00025
vol. (ml)Description Net Weight Gain (grams)
Reagent Blank Summary
Ash Grove Cememnt Company
Leamington Cement Plant
M242413
Main Kiln Stack
5
6/25/2024
Filterable Particulate
Filterable Particulate
Filterable Particulate
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 110 of 315 ©Mostardi Platt
Client:
Facility:
Project Number:
Test Location:
Test Method:Filter Drying Temp oF: 220
Filterable Analysis Date: Analyst: LNT
Sample Date ID# Initial Weight
(grams)
Final Weight
(grams)
Run 1 6/13/2024
Source Condition: Mill On
M5 Filter 15550 0.45781 0.45947 0.00166
Acetone Wash (M5 Pans) 16545 50 mL 5.00829 5.01024 0.00195
Acetone Blank ≤0.00025
Total Filterable Weight 0.00361
Run 2 6/13/2024
Source Condition: Mill On
M5 Filter 15551 0.45509 0.45694 0.00185
Acetone Wash (M5 Pans) 16544 50 mL 5.00512 5.00661 0.00149
Acetone Blank ≤0.00025
Total Filterable Weight 0.00334
Run 3 6/13/2024
Source Condition: Mill On
M5 Filter 15553 0.45447 0.45627 0.00180
Acetone Wash (M5 Pans) 16541 52 mL 5.03147 5.03066 ≤0.00025
Acetone Blank ≤0.00025
Total Filterable Weight ≤0.00205
Acetone Wash (M5 Pans) 16422 100 mL 4.96193 4.96079 ≤0.00025
Media
M5 Filter
Acetone Wash (M5 Pans)
Sample Vials (M202)
0.00008
RDL/MDL Summary
MDL, grams RDL, grams
0.00005
0.00008
0.00015
0.00025
0.00025
vol. (ml)Description Net Weight Gain (grams)
Reagent Blank Summary
Ash Grove Cememnt Company
Leamington Cement Plant
M222606
Main Kiln Stack
5
6/16/2024
Filterable Particulate
Filterable Particulate
Filterable Particulate
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 111 of 315 ©Mostardi Platt
Client:
Facility:
Project Number:
Test Location:
Test Method:Filter Drying Temp oF: Ambient-Des. 24 hrs
Filterable Analysis Date: Analyst: LNT
Sample Date ID# Initial Weight
(grams)
Final Weight
(grams)
Run 1 6/13/2024
Source Condition: MILL ON
M5 Filter 15535 0.46251 0.49561 0.03310
Acetone Wash (M5 Pans) 16533 55 mL 4.99636 5.00221 0.00585
Acetone Blank ≤0.00025
Total Filterable Weight 0.03895
Run 2 6/13/2024
Source Condition: MILL ON
M5 Filter 14843 0.46322 0.49673 0.03351
Acetone Wash (M5 Pans) 16532 50 mL 4.97745 4.98303 0.00558
Acetone Blank ≤0.00025
Total Filterable Weight 0.03909
Run 3 6/13/2024
Source Condition: MILL ON
M5 Filter 10476 0.45875 0.48157 0.02282
Acetone Wash (M5 Pans) 16547 60 mL 5.03479 5.03835 0.00356
Acetone Blank ≤0.00025
Total Filterable Weight 0.02638
Run 4 6/13/2024
Source Condition: SPIKED
M5 Filter 15552 0.45616 0.50152 0.04536
Acetone Wash (M5 Pans) 16546 70 mL 4.98343 4.98846 0.00503
Acetone Blank ≤0.00025
Total Filterable Weight 0.05039
Acetone Wash (M5 Pans) 16422 100 mL 4.96193 4.96079 ≤0.00025
Media
M5 Filter
Acetone Wash (M5 Pans)
Sample Vials (M202)
0.00008
Filterable Particulate
RDL/MDL Summary
MDL, grams RDL, grams
0.00005
0.00008
0.00015
0.00025
0.00025
vol. (ml)Description Net Weight Gain (grams)
Reagent Blank Summary
Ash Grove Cement Company
Leamington Cement Plant
M242413
Coal Mill Stack
5
6/26/2023
Filterable Particulate
Filterable Particulate
Filterable Particulate
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 112 of 315 ©Mostardi Platt
Client:
Facility:
Project Number:
Test Location:
Test Method:Filter Drying Temp oF: Ambient-Des. 24 hrs
Filterable Analysis Date: Analyst: LNT
Sample Date ID# Initial Weight
()
Final Weight
()
Run 1 6/12/2024
Source Condition:Mill Off
M5 Filter 10486 0.45494 0.48126 0.02632
Acetone Wash (M5 Pans)16526 65 mL 4.98789 4.99943 0.01154
Acetone Blank ≤0.00025
Total Filterable Weight 0.03786
Acetone/Hexane Wash 16557 350 mL 21.13418 21.13726 0.00308
DI Wash 16007 200 mL 21.26715 21.26741 0.00026
Field Blank 0.00168
Total Condensable Weight 0.00166
Total Particulate Weight 0.03952
Run 2 6/12/2024
Source Condition:Mill Off
M5 Filter 10522 0.45197 0.48618 0.03421
Acetone Wash (M5 Pans)16527 50 mL 4.98689 4.99145 0.00456
Acetone Blank ≤0.00025
Total Filterable Weight 0.03877
Run 3 6/12/2024
Source Condition:Mill Off
M5 Filter 10528 0.45191 0.48485 0.03294
Acetone Wash (M5 Pans)16528 50 mL 5.01340 5.02106 0.00766
Acetone Blank ≤0.00025
Total Filterable Weight 0.04060
Acetone/Hexane Wash 16010 100 mL 21.32227 21.32186 ≤0.00025
DI Wash 16560 120 mL 21.16595 21.16763 0.00168
Total Field Train Blank 0.00168
Acetone/Hexane Wash 16011 150 mL 21.43264 21.43581 0.00317
DI Wash 16558 110 mL 21.43188 21.43287 0.00099
Normality of NH4OH 0.1000
Acetone Wash (M5 Pans) 16422 100 mL 4.96193 4.96079 ≤0.00025
Media
M5 Filter
Acetone Wash (M5 Pans)
Sample Vials (M202)
0.00008
Field Train Blank Summary
RDL/MDL Summary
MDL, grams RDL, grams
0.00005
0.00008
0.00015
0.00025
0.00025
vol. (ml)Description Net Weight Gain (grams)
Reagent Blank Summary
Field Proof Blank Summary
Ash Grove Cement Company
Leamington Cement Plant
M242413
Coal Mill Stack
5
6/24/2024
Filterable Particulate
Filterable Particulate
Filterable Particulate
Condensable Particulate
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 113 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 1.14 1.14 1.14E-06 3.00E-07 0.09 0.00E+00 1.0 3.00E-07 0.09 0 1.14
12378-PeCDD 1.71 1.71 1.71E-06 4.51E-07 0.13 0.00E+00 1.0 4.51E-07 0.13 0 1.71
123478-HxCDD 1.96 1.96 1.96E-06 5.16E-07 0.15 0.00E+00 0.1 5.16E-08 0.01 0 0.196
123678-HxCDD 1.88 1.88 1.88E-06 4.95E-07 0.14 0.00E+00 0.1 4.95E-08 0.01 0 0.188
123789-HxCDD 2.37 2.37 2.37E-06 6.24E-07 0.18 0.00E+00 0.1 6.24E-08 0.02 0 0.237
1234678-HpCDD 3.68 3.68 3.68E-06 9.70E-07 0.28 0.00E+00 0.01 9.70E-09 0.00 0 0.0368
OCDD 6.61 6.61 6.61E-06 1.74E-06 0.50 0.00E+00 0.0003 5.22E-10 0.00 0 0.001983
2378 -TCDF 2.06 2.06 2.06E-06 5.43E-07 0.16 0.00E+00 0.1 5.43E-08 0.02 0 0.206
12378-PeCDF 0.96 0.96 9.60E-07 2.53E-07 0.07 0.00E+00 0.03 7.59E-09 0.00 0 0.0288
23478-PeCDF 0.96 0.96 9.55E-07 2.52E-07 0.07 0.00E+00 0.3 7.55E-08 0.02 0 0.2865
123478-HxCDF 1.34 1.34 1.34E-06 3.53E-07 0.10 0.00E+00 0.1 3.53E-08 0.01 0 0.134
123678-HxCDF 1.37 1.37 1.37E-06 3.61E-07 0.10 0.00E+00 0.1 3.61E-08 0.01 0 0.137
234678-HxCDF 1.46 1.46 1.46E-06 3.85E-07 0.11 0.00E+00 0.1 3.85E-08 0.01 0 0.146
123789-HxCDF 2.32 2.32 2.32E-06 6.11E-07 0.17 0.00E+00 0.1 6.11E-08 0.02 0 0.232
1234678-HpCDF 1.61 1.61 1.61E-06 4.24E-07 0.12 0.00E+00 0.01 4.24E-09 0.00 0 0.0161
1234789-HpCDF 2.96 2.96 2.96E-06 7.80E-07 0.22 0.00E+00 0.01 7.80E-09 0.00 0 0.0296
OCDF 3.15 3.15 3.15E-06 8.30E-07 0.24 0.00E+00 0.0003 2.49E-10 0.00 0 0.000945
Total TCDD 13.80 13.80 1.38E-05 3.64E-06 1.04 0.00E+00 0
Total PeCDD 6.76 6.76 6.76E-06 1.78E-06 0.51 0.00E+00 0
Total HxCDD 19.90 19.90 1.99E-05 5.24E-06 1.50 0.00E+00 0
Total HpCDD 3.68 3.68 3.68E-06 9.70E-07 0.28 0.00E+00 0
Total OCDD 6.61 6.61 6.61E-06 1.74E-06 0.50 0.00E+00 0
Total TCDF 49.70 49.70 4.97E-05 1.31E-05 3.74 0.00E+00 0
Total PeCDF 0.96 0.96 9.58E-07 2.52E-07 0.07 0.00E+00 0
Total HxCDF 1.62 1.62 1.62E-06 4.27E-07 0.12 0.00E+00 0
Total HpCDF 2.29 2.29 2.29E-06 6.03E-07 0.17 0.00E+00 0
Total OCDF 3.15 3.15 3.15E-06 8.30E-07 0.24 0.00E+00 0
Total PCDD/PCDF 108.47 1.08E-04 2.86E-05 8.17 0.00E+00
TEQ Total 4.726728 1.25E-06 0.36
Sample volume (Vmstd, dscf)134.03
Volumetric Air Flow (DSCFM)168,323.92
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 14.60
Average % O2 by volume, dry 12.00
Source Condition: Mill On
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 1
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 11, 2024
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 114 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 2.11 2.11 2.11E-06 5.57E-07 0.16 0.00E+00 1.0 5.57E-07 0.16 0 2.11
12378-PeCDD 2.34 2.34 2.34E-06 6.17E-07 0.18 0.00E+00 1.0 6.17E-07 0.18 0 2.34
123478-HxCDD 2.59 2.59 2.59E-06 6.83E-07 0.19 0.00E+00 0.1 6.83E-08 0.02 0 0.259
123678-HxCDD 2.24 2.24 2.24E-06 5.91E-07 0.17 0.00E+00 0.1 5.91E-08 0.02 0 0.224
123789-HxCDD 2.96 2.96 2.96E-06 7.81E-07 0.22 0.00E+00 0.1 7.81E-08 0.02 0 0.296
1234678-HpCDD 5.58 5.58 5.58E-06 1.47E-06 0.42 0.00E+00 0.01 1.47E-08 0.00 0 0.0558
OCDD 10.90 10.90 1.09E-05 2.88E-06 0.82 0.00E+00 0.0003 8.63E-10 0.00 0 0.00327
2378 -TCDF 2.90 2.90 2.90E-06 7.65E-07 0.22 0.00E+00 0.1 7.65E-08 0.02 0 0.29
12378-PeCDF 1.20 1.20 1.20E-06 3.17E-07 0.09 0.00E+00 0.03 9.50E-09 0.00 0 0.036
23478-PeCDF 1.20 1.20 1.20E-06 3.17E-07 0.09 0.00E+00 0.3 9.50E-08 0.03 0 0.36
123478-HxCDF 1.95 1.95 1.95E-06 5.14E-07 0.15 0.00E+00 0.1 5.14E-08 0.01 0 0.195
123678-HxCDF 2.17 2.17 2.17E-06 5.73E-07 0.16 0.00E+00 0.1 5.73E-08 0.02 0 0.217
234678-HxCDF 2.26 2.26 2.26E-06 5.96E-07 0.17 0.00E+00 0.1 5.96E-08 0.02 0 0.226
123789-HxCDF 3.75 3.75 3.75E-06 9.89E-07 0.28 0.00E+00 0.1 9.89E-08 0.03 0 0.375
1234678-HpCDF 2.68 2.68 2.68E-06 7.07E-07 0.20 0.00E+00 0.01 7.07E-09 0.00 0 0.0268
1234789-HpCDF 2.74 2.74 2.74E-06 7.23E-07 0.21 0.00E+00 0.01 7.23E-09 0.00 0 0.0274
OCDF 7.78 7.78 7.78E-06 2.05E-06 0.58 0.00E+00 0.0003 6.16E-10 0.00 0 0.002334
Total TCDD 16.70 16.70 1.67E-05 4.41E-06 1.25 0.00E+00 0
Total PeCDD 10.70 10.70 1.07E-05 2.82E-06 0.80 0.00E+00 0
Total HxCDD 26.80 26.80 2.68E-05 7.07E-06 2.01 0.00E+00 0
Total HpCDD 5.58 5.58 5.58E-06 1.47E-06 0.42 0.00E+00 0
Total OCDD 10.90 10.90 1.09E-05 2.88E-06 0.82 0.00E+00 0
Total TCDF 55.40 55.40 5.54E-05 1.46E-05 4.16 0.00E+00 0
Total PeCDF 1.20 1.20 1.20E-06 3.17E-07 0.09 0.00E+00 0
Total HxCDF 2.53 2.53 2.53E-06 6.68E-07 0.19 0.00E+00 0
Total HpCDF 2.71 2.71 2.71E-06 7.15E-07 0.20 0.00E+00 0
Total OCDF 7.78 7.78 7.78E-06 2.05E-06 0.58 0.00E+00 0
Total PCDD/PCDF 140.30 1.40E-04 3.70E-05 10.53 0.00E+00
TEQ Total 7.043604 1.86E-06 0.53
Sample volume (Vmstd, dscf)133.85
Volumetric Air Flow (DSCFM)167,495.71
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 16.10
Average % O2 by volume, dry 11.70
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 2
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 11, 2024
Source Condition: Mill On
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 115 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 2.23 2.23 2.23E-06 5.90E-07 0.17 0.00E+00 1.0 5.90E-07 0.17 0 2.23
12378-PeCDD 1.60 1.60 1.60E-06 4.23E-07 0.12 0.00E+00 1.0 4.23E-07 0.12 0 1.6
123478-HxCDD 2.53 2.53 2.53E-06 6.69E-07 0.19 0.00E+00 0.1 6.69E-08 0.02 0 0.253
123678-HxCDD 2.42 2.42 2.42E-06 6.40E-07 0.18 0.00E+00 0.1 6.40E-08 0.02 0 0.242
123789-HxCDD 2.87 2.87 2.87E-06 7.59E-07 0.22 0.00E+00 0.1 7.59E-08 0.02 0 0.287
1234678-HpCDD 4.70 4.70 4.70E-06 1.24E-06 0.35 0.00E+00 0.01 1.24E-08 0.00 0 0.047
OCDD 8.44 8.44 8.44E-06 2.23E-06 0.63 0.00E+00 0.0003 6.70E-10 0.00 0 0.002532
2378 -TCDF 2.44 2.44 2.44E-06 6.45E-07 0.18 0.00E+00 0.1 6.45E-08 0.02 0 0.244
12378-PeCDF 1.19 1.19 1.19E-06 3.15E-07 0.09 0.00E+00 0.03 9.44E-09 0.00 0 0.0357
23478-PeCDF 1.16 1.16 1.16E-06 3.07E-07 0.09 0.00E+00 0.3 9.20E-08 0.03 0 0.348
123478-HxCDF 1.35 1.35 1.35E-06 3.57E-07 0.10 0.00E+00 0.1 3.57E-08 0.01 0 0.135
123678-HxCDF 1.34 1.34 1.34E-06 3.54E-07 0.10 0.00E+00 0.1 3.54E-08 0.01 0 0.134
234678-HxCDF 1.45 1.45 1.45E-06 3.84E-07 0.11 0.00E+00 0.1 3.84E-08 0.01 0 0.145
123789-HxCDF 2.64 2.64 2.64E-06 6.98E-07 0.20 0.00E+00 0.1 6.98E-08 0.02 0 0.264
1234678-HpCDF 4.25 4.25 4.25E-06 1.12E-06 0.32 0.00E+00 0.01 1.12E-08 0.00 0 0.0425
1234789-HpCDF 6.67 6.67 6.67E-06 1.76E-06 0.50 0.00E+00 0.01 1.76E-08 0.01 0 0.0667
OCDF 6.50 6.50 6.50E-06 1.72E-06 0.49 0.00E+00 0.0003 5.16E-10 0.00 0 0.00195
Total TCDD 11.70 11.70 1.17E-05 3.09E-06 0.88 0.00E+00 0
Total PeCDD 10.70 10.70 1.07E-05 2.83E-06 0.80 0.00E+00 0
Total HxCDD 24.40 24.40 2.44E-05 6.45E-06 1.83 0.00E+00 0
Total HpCDD 4.70 4.70 4.70E-06 1.24E-06 0.35 0.00E+00 0
Total OCDD 8.40 8.40 8.40E-06 2.22E-06 0.63 0.00E+00 0
Total TCDF 37.50 37.50 3.75E-05 9.92E-06 2.81 0.00E+00 0
Total PeCDF 1.18 1.18 1.18E-06 3.12E-07 0.09 0.00E+00 0
Total HxCDF 1.70 1.70 1.70E-06 4.50E-07 0.13 0.00E+00 0
Total HpCDF 5.46 5.46 5.46E-06 1.44E-06 0.41 0.00E+00 0
Total OCDF 6.50 6.50 6.50E-06 1.72E-06 0.49 0.00E+00 0
Total PCDD/PCDF 112.28 1.12E-04 2.97E-05 8.43 0.00E+00 0
TEQ Total 6.078382 1.61E-06 0.46
Sample volume (Vmstd, dscf)133.51
Volumetric Air Flow (DSCFM)166,975.66
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 16.30
Average % O2 by volume, dry 11.60
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 3
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 11, 2024
Source Condition: Mill On
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 116 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 12.60 12.60 1.26E-05 3.90E-06 0.94 0.00E+00 1.0 3.90E-06 0.94 0 12.6
12378-PeCDD 1.90 1.90 1.90E-06 5.88E-07 0.14 0.00E+00 1.0 5.88E-07 0.14 0 1.9
123478-HxCDD 1.48 1.48 1.48E-06 4.58E-07 0.11 0.00E+00 0.1 4.58E-08 0.01 0 0.148
123678-HxCDD 1.54 1.54 1.54E-06 4.77E-07 0.12 0.00E+00 0.1 4.77E-08 0.01 0 0.154
123789-HxCDD 1.63 1.63 1.63E-06 5.05E-07 0.12 0.00E+00 0.1 5.05E-08 0.01 0 0.163
1234678-HpCDD 2.78 2.78 2.78E-06 8.61E-07 0.21 0.00E+00 0.01 8.61E-09 0.00 0 0.0278
OCDD 7.37 7.37 7.37E-06 2.28E-06 0.55 0.00E+00 0.0003 6.84E-10 0.00 0 0.00221
2378 -TCDF 1,450.00 1,450.00 1.45E-03 4.49E-04 108.69 0.00E+00 0.1 4.49E-05 10.87 0 145
12378-PeCDF 154.00 154.00 1.54E-04 4.77E-05 11.54 0.00E+00 0.03 1.43E-06 0.35 0 4.62
23478-PeCDF 190.00 190.00 1.90E-04 5.88E-05 14.24 0.00E+00 0.3 1.76E-05 4.27 0 57
123478-HxCDF 15.60 15.60 1.56E-05 4.83E-06 1.17 0.00E+00 0.1 4.83E-07 0.12 0 1.56
123678-HxCDF 11.50 11.50 1.15E-05 3.56E-06 0.86 0.00E+00 0.1 3.56E-07 0.09 0 1.15
234678-HxCDF 7.02 7.02 7.02E-06 2.17E-06 0.53 0.00E+00 0.1 2.17E-07 0.05 0 0.702
123789-HxCDF 4.66 4.66 4.66E-06 1.44E-06 0.35 0.00E+00 0.1 1.44E-07 0.03 0 0.466
1234678-HpCDF 2.68 2.68 2.68E-06 8.30E-07 0.20 0.00E+00 0.01 8.30E-09 0.00 0 0.0268
1234789-HpCDF 4.18 4.18 4.18E-06 1.29E-06 0.31 0.00E+00 0.01 1.29E-08 0.00 0 0.0418
OCDF 4.34 4.34 4.34E-06 1.34E-06 0.33 0.00E+00 0.0003 4.03E-10 0.00 0 0.001302
Total TCDD 579.00 579.00 5.79E-04 1.79E-04 43.40 0.00E+00 0
Total PeCDD 43.90 43.90 4.39E-05 1.36E-05 3.29 0.00E+00 0
Total HxCDD 30.40 30.40 3.04E-05 9.41E-06 2.28 0.00E+00 0
Total HpCDD 2.78 2.78 2.78E-06 8.61E-07 0.21 0.00E+00 0
Total OCDD 7.37 7.37 7.37E-06 2.28E-06 0.55 0.00E+00 0
Total TCDF 75,700.00 75,700.00 7.57E-02 2.34E-02 5674.36 0.00E+00 0
Total PeCDF 3,940.00 3,940.00 3.94E-03 1.22E-03 295.34 0.00E+00 0
Total HxCDF 134.00 134.00 1.34E-04 4.15E-05 10.04 0.00E+00 0
Total HpCDF 3.43 3.43 3.43E-06 1.06E-06 0.26 0.00E+00 0
Total OCDF 4.34 4.34 4.34E-06 1.34E-06 0.33 0.00E+00 0
Total PCDD/PCDF 80,445.22 8.04E-02 2.49E-02 6030.06 0.00E+00
TEQ Total 225.562912 6.98E-05 16.91
Sample volume (Vmstd, dscf)114.06
Volumetric Air Flow (DSCFM)142,496.28
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 13.70
Average % O2 by volume, dry 10.20
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 1
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 12, 2024
Source Condition: Mill Off
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 117 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 15.60 15.60 1.56E-05 5.31E-06 1.18 0.00E+00 1.0 5.31E-06 1.18 0 15.6
12378-PeCDD 1.63 1.63 1.63E-06 5.55E-07 0.12 0.00E+00 1.0 5.55E-07 0.12 0 1.63
123478-HxCDD 1.59 1.59 1.59E-06 5.42E-07 0.12 0.00E+00 0.1 5.42E-08 0.01 0 0.159
123678-HxCDD 1.69 1.69 1.69E-06 5.76E-07 0.13 0.00E+00 0.1 5.76E-08 0.01 0 0.169
123789-HxCDD 1.79 1.79 1.79E-06 6.10E-07 0.14 0.00E+00 0.1 6.10E-08 0.01 0 0.179
1234678-HpCDD 4.28 4.28 4.28E-06 1.46E-06 0.32 0.00E+00 0.01 1.46E-08 0.00 0 0.0428
OCDD 5.91 5.91 5.91E-06 2.01E-06 0.45 0.00E+00 0.0003 6.04E-10 0.00 0 0.001773
2378 -TCDF 1,610.00 1,610.00 1.61E-03 5.48E-04 121.74 0.00E+00 0.1 5.48E-05 12.17 0 161
12378-PeCDF 237.00 237.00 2.37E-04 8.07E-05 17.92 0.00E+00 0.03 2.42E-06 0.54 0 7.11
23478-PeCDF 276.00 276.00 2.76E-04 9.40E-05 20.87 0.00E+00 0.3 2.82E-05 6.26 0 82.8
123478-HxCDF 37.00 37.00 3.70E-05 1.26E-05 2.80 0.00E+00 0.1 1.26E-06 0.28 0 3.7
123678-HxCDF 20.60 20.60 2.06E-05 7.02E-06 1.56 0.00E+00 0.1 7.02E-07 0.16 0 2.06
234678-HxCDF 13.40 13.40 1.34E-05 4.56E-06 1.01 0.00E+00 0.1 4.56E-07 0.10 0 1.34
123789-HxCDF 5.47 5.47 5.47E-06 1.86E-06 0.41 0.00E+00 0.1 1.86E-07 0.04 0 0.547
1234678-HpCDF 2.93 2.93 2.93E-06 9.98E-07 0.22 0.00E+00 0.01 9.98E-09 0.00 0 0.0293
1234789-HpCDF 4.48 4.48 4.48E-06 1.53E-06 0.34 0.00E+00 0.01 1.53E-08 0.00 0 0.0448
OCDF 4.21 4.21 4.21E-06 1.43E-06 0.32 0.00E+00 0.0003 4.30E-10 0.00 0 0.001263
Total TCDD 692.00 692.00 6.92E-04 2.36E-04 52.33 0.00E+00 0
Total PeCDD 76.90 76.90 7.69E-05 2.62E-05 5.81 0.00E+00 0
Total HxCDD 29.00 29.00 2.90E-05 9.88E-06 2.19 0.00E+00 0
Total HpCDD 4.28 4.28 4.28E-06 1.46E-06 0.32 0.00E+00 0
Total OCDD 5.91 5.91 5.91E-06 2.01E-06 0.45 0.00E+00 0
Total TCDF 80,100.00 80,100.00 8.01E-02 2.73E-02 6056.89 0.00E+00 0
Total PeCDF 5,480.00 5,480.00 5.48E-03 1.87E-03 414.38 0.00E+00 0
Total HxCDF 237.00 237.00 2.37E-04 8.07E-05 17.92 0.00E+00 0
Total HpCDF 3.71 3.71 3.71E-06 1.26E-06 0.28 0.00E+00 0
Total OCDF 4.21 4.21 4.21E-06 1.43E-06 0.32 0.00E+00 0
Total PCDD/PCDF 86,633.01 8.66E-02 2.95E-02 6550.90 0.00E+00
TEQ Total 276.413936 9.42E-05 20.90
Sample volume (Vmstd, dscf)103.67
Volumetric Air Flow (DSCFM)130,649.89
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 13.60
Average % O2 by volume, dry 10.40
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 2
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 12, 2024
Source Condition: Mill Off
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 118 of 315 ©Mostardi Platt
Concentration Emissions Blank TEQ
(pg) (pg-Blank) (ug) (ug/dcsm) (ug/hr) (lbs/mmBtu) TEQ Factor (ug/dscm) (ug/hr) (pg) (pg)
2378-TCDD 18.70 18.70 1.87E-05 6.31E-06 1.41 0.00E+00 1.0 6.31E-06 1.41 0 18.7
12378-PeCDD 1.59 1.59 1.59E-06 5.37E-07 0.12 0.00E+00 1.0 5.37E-07 0.12 0 1.59
123478-HxCDD 1.21 1.21 1.21E-06 4.08E-07 0.09 0.00E+00 0.1 4.08E-08 0.01 0 0.121
123678-HxCDD 1.24 1.24 1.24E-06 4.19E-07 0.09 0.00E+00 0.1 4.19E-08 0.01 0 0.124
123789-HxCDD 1.32 1.32 1.32E-06 4.46E-07 0.10 0.00E+00 0.1 4.46E-08 0.01 0 0.132
1234678-HpCDD 2.19 2.19 2.19E-06 7.39E-07 0.17 0.00E+00 0.01 7.39E-09 0.00 0 0.0219
OCDD 4.02 4.02 4.02E-06 1.36E-06 0.30 0.00E+00 0.0003 4.07E-10 0.00 0 0.001206
2378 -TCDF 1,740.00 1,740.00 1.74E-03 5.87E-04 131.55 0.00E+00 0.1 5.87E-05 13.15 0 174
12378-PeCDF 226.00 226.00 2.26E-04 7.63E-05 17.09 0.00E+00 0.03 2.29E-06 0.51 0 6.78
23478-PeCDF 292.00 292.00 2.92E-04 9.86E-05 22.08 0.00E+00 0.3 2.96E-05 6.62 0 87.6
123478-HxCDF 40.90 40.90 4.09E-05 1.38E-05 3.09 0.00E+00 0.1 1.38E-06 0.31 0 4.09
123678-HxCDF 25.20 25.20 2.52E-05 8.51E-06 1.91 0.00E+00 0.1 8.51E-07 0.19 0 2.52
234678-HxCDF 13.00 13.00 1.30E-05 4.39E-06 0.98 0.00E+00 0.1 4.39E-07 0.10 0 1.3
123789-HxCDF 7.08 7.08 7.08E-06 2.39E-06 0.54 0.00E+00 0.1 2.39E-07 0.05 0 0.708
1234678-HpCDF 8.68 8.68 8.68E-06 2.93E-06 0.66 0.00E+00 0.01 2.93E-08 0.01 0 0.0868
1234789-HpCDF 3.34 3.34 3.34E-06 1.13E-06 0.25 0.00E+00 0.01 1.13E-08 0.00 0 0.0334
OCDF 2.16 2.16 2.16E-06 7.29E-07 0.16 0.00E+00 0.0003 2.19E-10 0.00 0 0.000648
Total TCDD 763.00 763.00 7.63E-04 2.58E-04 57.68 0.00E+00 0
Total PeCDD 77.70 77.70 7.77E-05 2.62E-05 5.87 0.00E+00 0
Total HxCDD 31.30 31.30 3.13E-05 1.06E-05 2.37 0.00E+00 0
Total HpCDD 2.19 2.19 2.19E-06 7.39E-07 0.17 0.00E+00 0
Total OCDD 4.02 4.02 4.02E-06 1.36E-06 0.30 0.00E+00 0
Total TCDF 89,800.00 89,800.00 8.98E-02 3.03E-02 6789.01 0.00E+00 0
Total PeCDF 5,620.00 5,620.00 5.62E-03 1.90E-03 424.88 0.00E+00 0
Total HxCDF 258.00 258.00 2.58E-04 8.71E-05 19.51 0.00E+00 0
Total HpCDF 8.68 8.68 8.68E-06 2.93E-06 0.66 0.00E+00 0
Total OCDF 2.16 2.16 2.16E-06 7.29E-07 0.16 0.00E+00 0
Total PCDD/PCDF 96,567.05 9.66E-02 3.26E-02 7300.61 0.00E+00 0
TEQ Total 297.808954 1.01E-04 22.51
Sample volume (Vmstd, dscf)104.61
Volumetric Air Flow (DSCFM)131,810.52
Fd-Factor dscf/MMBtu 0.0
Average % CO2 by volume, dry 13.90
Average % O2 by volume, dry 10.90
Analytes
Sample Catch TEQ Factor Results
PCDD/PCDF TEST RESULTS SUMMARY
Run 3
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
June 12, 2024
Source Condition: Mill Off
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 119 of 315 ©Mostardi Platt
Mostardi Platt Environmental -
Elmhurst
888 N Industrial Dr
Elmhurst, IL 60126-1121
Main Kiln Stack
Client Project#AshGrove Leamington
Samples Received:6/20/2024
Analytical Report
0524-877
EPA Method 23
PCDD/PCDF
Report Issue Date:7/22/2024
I certify that to the best of my knowledge all analytical data presented in this report have been checked for completeness,
accuracy, errors and legibility in addition to having been conducted in accordance with approved protocol, and that all
deviations and analytical problems are summarized in the appropriate narrative(s). This analytical report was prepared in
Portable Document Format (.PDF) and contains _32_ pages. This report shall not be reproduced except in full without
approval of the laboratory. This will provide assurance that parts of the report are not taken out of context.
Amendment(s):
Signature:
Amanda Valois, QA Associate
Christina Kurnath, Project Manager
[e-mail] / www.enthalpy.com
O: 910-876-6895
Enthalpy Analytical
2714 Exchange Drive Wilmington NC 28405
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Summary of Results
EU 0524-877 Page 2 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Summary
Compound CAS Mill On Run 1
pg
Mill On Run 2
pg
Mill On Run 3
pg
Mill Off Run 1
pg
Mill Off Run 2
pg
TCDD 2378-TCDD (S)1746-01-6 ND U ND U ND U 12.6 15.6
PeCDD 12378-PeCDD (S)40321-76-4 ND U ND U ND U ND U ND U
HxCDD 123478-HxCDD (S)39227-28-6 ND U ND U ND U ND U ND U
123678-HxCDD (S)57653-85-7 ND U ND U ND U ND U ND U
123789-HxCDD (S)19408-74-3 ND U ND U ND U ND U ND U
HpCDD 1234678-HpCDD (S)35822-46-9 ND U ND U ND U ND U ND U
OCDD OCDD (S)3268-87-9 ND U ND U ND U ND U ND U
TCDF 2378-TCDF (S)51207-31-9 ND U ND U ND U 1450 1610
PeCDF 12378-PeCDF (S)57117-41-6 ND U ND U ND U 154 237
23478-PeCDF (S)57117-31-4 ND U ND U ND U 190 276
HxCDF 123478-HxCDF (S)70648-26-9 ND U ND U ND U 15.6 J-EMPC 37.0
123678-HxCDF (S)57117-44-9 ND U ND U ND U 11.5 J 20.6 J
234678-HxCDF (S)60851-34-5 ND U ND U ND U 7.02 J 13.4 J
123789-HxCDF (S)72918-21-9 ND U ND U ND U 4.66 J-EMPC ND U
HpCDF 1234678-HpCDF (S)67562-39-4 ND U ND U ND U ND U ND U
1234789-HpCDF (S)55673-89-7 ND U ND U ND U ND U ND U
OCDF OCDF (S)39001-02-0 ND U ND U ND U ND U ND U
TCDD Group Total 41903-57-5 13.8 16.7 11.7 579 692
PeCDD Group Total 36088-22-9 6.76 10.7 10.7 43.9 76.9
HxCDD Group Total 34465-46-8 19.9 26.8 24.4 30.4 29.0
HpCDD Group Total 37871-00-4 ND ND ND ND ND
OCDD Group Total ND ND ND ND ND
TCDF Group Total 55722-27-5 49.7 55.4 37.5 75700 80100
PeCDF Group Total 30402-15-4 ND ND ND 3940 5480
HxCDF Group Total 55684-94-1 ND ND ND 134 237
HpCDF Group Total 38998-75-3 ND ND ND ND ND
OCDF Group Total ND ND ND ND ND
TEQ ITEQ (ND=0; EMPC=0)0 0 0 263 334
ITEQ (ND=1/2EDL;EMPC=1/2EDL)2.04 3.08 2.77 264 335
ITEQ (ND=EDL EMPC=EDL)4.09 6.15 5.54 265 336
ITEQ (ND=0; EMPC=EMPC)0 0 0 265 334
ITEQ (ND=1/2EDL; EMPC=EMPC)2.04 3.08 2.77 265 335
ITEQ (ND=EDL; EMPC=EMPC)4.09 6.15 5.54 266 336
WTEQ (ND=0; EMPC=0)0 0 0 221 274
WTEQ (ND=1/2EDL;EMPC=1/2EDL)2.36 3.52 3.04 223 275
WTEQ (ND=EDL EMPC=EDL)4.72 7.04 6.08 225 277
WTEQ (ND=0; EMPC=EMPC)0 0 0 223 274
WTEQ (ND=1/2EDL; EMPC=EMPC)2.36 3.52 3.04 225 275
WTEQ (ND=EDL; EMPC=EMPC)4.72 7.04 6.08 226 277
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 3 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Summary
Compound CAS Mill Off Run 3
pg
TCDD 2378-TCDD (S)1746-01-6 18.7
PeCDD 12378-PeCDD (S)40321-76-4 ND U
HxCDD 123478-HxCDD (S)39227-28-6 ND U
123678-HxCDD (S)57653-85-7 ND U
123789-HxCDD (S)19408-74-3 ND U
HpCDD 1234678-HpCDD (S)35822-46-9 ND U
OCDD OCDD (S)3268-87-9 ND U
TCDF 2378-TCDF (S)51207-31-9 1740
PeCDF 12378-PeCDF (S)57117-41-6 226
23478-PeCDF (S)57117-31-4 292
HxCDF 123478-HxCDF (S)70648-26-9 40.9
123678-HxCDF (S)57117-44-9 25.2
234678-HxCDF (S)60851-34-5 13.0 J-EMPC
123789-HxCDF (S)72918-21-9 7.08 J
HpCDF 1234678-HpCDF (S)67562-39-4 8.68 J
1234789-HpCDF (S)55673-89-7 ND U
OCDF OCDF (S)39001-02-0 ND U
TCDD Group Total 41903-57-5 763
PeCDD Group Total 36088-22-9 77.7
HxCDD Group Total 34465-46-8 31.3
HpCDD Group Total 37871-00-4 ND
OCDD Group Total ND
TCDF Group Total 55722-27-5 89800
PeCDF Group Total 30402-15-4 5620
HxCDF Group Total 55684-94-1 258
HpCDF Group Total 38998-75-3 8.68
OCDF Group Total ND
TEQ ITEQ (ND=0; EMPC=0)358
ITEQ (ND=1/2EDL;EMPC=1/2EDL)358
ITEQ (ND=EDL EMPC=EDL)359
ITEQ (ND=0; EMPC=EMPC)359
ITEQ (ND=1/2EDL; EMPC=EMPC)360
ITEQ (ND=EDL; EMPC=EMPC)360
WTEQ (ND=0; EMPC=0)295
WTEQ (ND=1/2EDL;EMPC=1/2EDL)296
WTEQ (ND=EDL EMPC=EDL)297
WTEQ (ND=0; EMPC=EMPC)296
WTEQ (ND=1/2EDL; EMPC=EMPC)297
WTEQ (ND=EDL; EMPC=EMPC)298
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 4 of 32
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Detailed Results
EU 0524-877 Page 5 of 32
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Details
Sample Name Mill On Run 1
Sampling Site
Enthalpy ID 0524-877-001-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 05:37 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062426A ND 5.00 1.14 U
PeCDD 12378-PeCDD (S)40321-76-4 G28062426A ND 25.0 1.71 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062426A ND 25.0 1.96 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062426A ND 25.0 1.88 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062426A ND 25.0 2.37 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062426A ND 25.0 3.68 U
OCDD OCDD (S)3268-87-9 G28062426A ND 50.0 6.61 U
TCDF 2378-TCDF (S)51207-31-9 G28062426A ND 5.00 2.06 U
PeCDF 12378-PeCDF (S)57117-41-6 G28062426A ND 25.0 0.960 U
PeCDF 23478-PeCDF (S)57117-31-4 G28062426A ND 25.0 0.955 U
HxCDF 123478-HxCDF (S)70648-26-9 G28062426A ND 25.0 1.34 U
HxCDF 123678-HxCDF (S)57117-44-9 G28062426A ND 25.0 1.37 U
HxCDF 234678-HxCDF (S)60851-34-5 G28062426A ND 25.0 1.46 U
HxCDF 123789-HxCDF (S)72918-21-9 G28062426A ND 25.0 2.32 U
HpCDF 1234678-HpCDF (S)67562-39-4 G28062426A ND 25.0 1.61 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062426A ND 25.0 2.96 U
OCDF OCDF (S)39001-02-0 G28062426A ND 50.0 3.15 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062426A 5.24 40-135%61.3%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062426A 9.79 40-135%62.1%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062426A 12.6 40-135%77.5%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062426A 11.6 40-135%87.1%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062426A 11.8 40-135%84.7%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062426A 16.2 40-135%70.0%
ES 13C-OCDD (ES)114423-97-1 G28062426A 31.6 40-135%57.9%
ES 13C-2378-TCDF (ES)89059-46-1 G28062426A 12.2 40-135%109.0%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062426A 13.3 40-135%104.6%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062426A 13.7 40-135%105.4%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062426A 15.0 40-135%79.3%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062426A 13.2 40-135%80.4%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062426A 13.8 40-135%75.9%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062426A 16.6 40-135%82.3%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062426A 16.7 40-135%70.1%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062426A 19.7 40-135%70.8%
ES 13C-OCDF (ES)109719-78-0 G28062426A 6.23 40-135%60.1%
SS 37Cl-2378-TCDD (SS)G28062426A 3.72 70-130%97.4%
SS 13C-12347-PeCDD (SS)G28062426A 17.5 70-130%91.5%
SS 13C-12346-PeCDF (SS)G28062426A 11.1 70-130%102.9%
SS 13C-123469-HxCDF (SS)G28062426A 35.6 70-130%94.0%
SS 13C-1234689-HpCDF (SS)G28062426A 61.9 70-130%102.0%
AS 13C-1368-TCDD (AS)G28062426A 4.89 20-150%60.9%
AS 13C-1368-TCDF (AS)G28062426A 10.1 20-150%106.7%
TCDD Group Total 41903-57-5 13.8 1.14
PeCDD Group Total 36088-22-9 6.76 1.71
HxCDD Group Total 34465-46-8 19.9 2.07
HpCDD Group Total 37871-00-4 ND 3.68
OCDD Group Total ND 6.61
TCDF Group Total 55722-27-5 49.7 2.06
PeCDF Group Total 30402-15-4 ND 0.958
HxCDF Group Total 55684-94-1 ND 1.62
HpCDF Group Total 38998-75-3 ND 2.29
OCDF Group Total ND 3.15
TEQ ITEQ (ND=0; EMPC=0)0
ITEQ (ND=1/2EDL;EMPC=1/2EDL)2.04
ITEQ (ND=EDL EMPC=EDL)4.09
ITEQ (ND=0; EMPC=EMPC)0
ITEQ (ND=1/2EDL; EMPC=EMPC)2.04
ITEQ (ND=EDL; EMPC=EMPC)4.09
WTEQ (ND=0; EMPC=0)0
WTEQ (ND=1/2EDL;EMPC=1/2EDL)2.36
WTEQ (ND=EDL EMPC=EDL)4.72
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 6 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Details
Sample Name Mill On Run 1
Sampling Site
Enthalpy ID 0524-877-001-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 05:37 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)0
WTEQ (ND=1/2EDL; EMPC=EMPC)2.36
WTEQ (ND=EDL; EMPC=EMPC)4.72
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
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Details
Sample Name Mill On Run 2
Sampling Site
Enthalpy ID 0524-877-002-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 06:28 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062427A ND 5.00 2.11 U
PeCDD 12378-PeCDD (S)40321-76-4 G28062427A ND 25.0 2.34 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062427A ND 25.0 2.59 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062427A ND 25.0 2.24 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062427A ND 25.0 2.96 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062427A ND 25.0 5.58 U
OCDD OCDD (S)3268-87-9 G28062427A ND 50.0 10.9 U
TCDF 2378-TCDF (S)51207-31-9 G28062427A ND 5.00 2.90 U
PeCDF 12378-PeCDF (S)57117-41-6 G28062427A ND 25.0 1.20 U
PeCDF 23478-PeCDF (S)57117-31-4 G28062427A ND 25.0 1.20 U
HxCDF 123478-HxCDF (S)70648-26-9 G28062427A ND 25.0 1.95 U
HxCDF 123678-HxCDF (S)57117-44-9 G28062427A ND 25.0 2.17 U
HxCDF 234678-HxCDF (S)60851-34-5 G28062427A ND 25.0 2.26 U
HxCDF 123789-HxCDF (S)72918-21-9 G28062427A ND 25.0 3.75 U
HpCDF 1234678-HpCDF (S)67562-39-4 G28062427A ND 25.0 2.68 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062427A ND 25.0 2.74 U
OCDF OCDF (S)39001-02-0 G28062427A ND 50.0 7.78 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062427A 8.06 40-135%63.6%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062427A 10.8 40-135%62.8%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062427A 15.0 40-135%75.3%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062427A 13.8 40-135%102.1%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062427A 14.1 40-135%94.3%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062427A 16.8 40-135%65.7%
ES 13C-OCDD (ES)114423-97-1 G28062427A 7.70 40-135%42.6%
ES 13C-2378-TCDF (ES)89059-46-1 G28062427A 23.2 40-135%111.4%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062427A 26.8 40-135%103.7%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062427A 27.7 40-135%105.7%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062427A 19.4 40-135%86.7%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062427A 17.0 40-135%92.9%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062427A 17.8 40-135%79.9%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062427A 21.4 40-135%85.6%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062427A 47.9 40-135%68.0%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062427A 56.5 40-135%86.0%
ES 13C-OCDF (ES)109719-78-0 G28062427A 16.5 40-135%46.9%
SS 37Cl-2378-TCDD (SS)G28062427A 5.03 70-130%103.5%
SS 13C-12347-PeCDD (SS)G28062427A 19.5 70-130%98.5%
SS 13C-12346-PeCDF (SS)G28062427A 22.3 70-130%115.4%
SS 13C-123469-HxCDF (SS)G28062427A 47.0 70-130%96.2%
SS 13C-1234689-HpCDF (SS)G28062427A 196 70-130%118.0%
AS 13C-1368-TCDD (AS)G28062427A 7.53 20-150%65.0%
AS 13C-1368-TCDF (AS)G28062427A 19.2 20-150%118.5%
TCDD Group Total 41903-57-5 16.7 2.11
PeCDD Group Total 36088-22-9 10.7 2.34
HxCDD Group Total 34465-46-8 26.8 2.60
HpCDD Group Total 37871-00-4 ND 5.58
OCDD Group Total ND 10.9
TCDF Group Total 55722-27-5 55.4 2.90
PeCDF Group Total 30402-15-4 ND 1.20
HxCDF Group Total 55684-94-1 ND 2.53
HpCDF Group Total 38998-75-3 ND 2.71
OCDF Group Total ND 7.78
TEQ ITEQ (ND=0; EMPC=0)0
ITEQ (ND=1/2EDL;EMPC=1/2EDL)3.08
ITEQ (ND=EDL EMPC=EDL)6.15
ITEQ (ND=0; EMPC=EMPC)0
ITEQ (ND=1/2EDL; EMPC=EMPC)3.08
ITEQ (ND=EDL; EMPC=EMPC)6.15
WTEQ (ND=0; EMPC=0)0
WTEQ (ND=1/2EDL;EMPC=1/2EDL)3.52
WTEQ (ND=EDL EMPC=EDL)7.04
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
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Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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Details
Sample Name Mill On Run 2
Sampling Site
Enthalpy ID 0524-877-002-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 06:28 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)0
WTEQ (ND=1/2EDL; EMPC=EMPC)3.52
WTEQ (ND=EDL; EMPC=EMPC)7.04
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 9 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 128 of 315 ©Mostardi Platt
Details
Sample Name Mill On Run 3
Sampling Site
Enthalpy ID 0524-877-003-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 07:20 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062428A ND 5.00 2.23 U
PeCDD 12378-PeCDD (S)40321-76-4 G28062428A ND 25.0 1.60 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062428A ND 25.0 2.53 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062428A ND 25.0 2.42 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062428A ND 25.0 2.87 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062428A ND 25.0 4.70 U
OCDD OCDD (S)3268-87-9 G28062428A ND 50.0 8.44 U
TCDF 2378-TCDF (S)51207-31-9 G28062428A ND 5.00 2.44 U
PeCDF 12378-PeCDF (S)57117-41-6 G28062428A ND 25.0 1.19 U
PeCDF 23478-PeCDF (S)57117-31-4 G28062428A ND 25.0 1.16 U
HxCDF 123478-HxCDF (S)70648-26-9 G28062428A ND 25.0 1.35 U
HxCDF 123678-HxCDF (S)57117-44-9 G28062428A ND 25.0 1.34 U
HxCDF 234678-HxCDF (S)60851-34-5 G28062428A ND 25.0 1.45 U
HxCDF 123789-HxCDF (S)72918-21-9 G28062428A ND 25.0 2.64 U
HpCDF 1234678-HpCDF (S)67562-39-4 G28062428A ND 25.0 4.25 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062428A ND 25.0 6.67 U
OCDF OCDF (S)39001-02-0 G28062428A ND 50.0 6.50 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062428A 6.96 40-135%52.8%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062428A 13.1 40-135%52.7%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062428A 10.2 40-135%74.3%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062428A 9.42 40-135%92.8%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062428A 9.59 40-135%88.0%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062428A 9.48 40-135%59.8%
ES 13C-OCDD (ES)114423-97-1 G28062428A 16.1 40-135%40.1%
ES 13C-2378-TCDF (ES)89059-46-1 G28062428A 16.3 40-135%98.0%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062428A 14.9 40-135%86.8%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062428A 15.4 40-135%91.1%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062428A 14.3 40-135%84.3%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062428A 12.6 40-135%83.6%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062428A 13.2 40-135%75.7%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062428A 15.8 40-135%78.1%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062428A 16.7 40-135%63.1%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062428A 19.7 40-135%64.3%
ES 13C-OCDF (ES)109719-78-0 G28062428A 12.6 40-135%42.4%
SS 37Cl-2378-TCDD (SS)G28062428A 3.86 70-130%100.6%
SS 13C-12347-PeCDD (SS)G28062428A 28.1 70-130%90.3%
SS 13C-12346-PeCDF (SS)G28062428A 15.2 70-130%107.6%
SS 13C-123469-HxCDF (SS)G28062428A 33.3 70-130%95.7%
SS 13C-1234689-HpCDF (SS)G28062428A 79.5 70-130%105.3%
AS 13C-1368-TCDD (AS)G28062428A 6.51 20-150%50.4%
AS 13C-1368-TCDF (AS)G28062428A 13.6 20-150%92.5%
TCDD Group Total 41903-57-5 11.7 2.23
PeCDD Group Total 36088-22-9 10.7 1.60
HxCDD Group Total 34465-46-8 24.4 2.60
HpCDD Group Total 37871-00-4 ND 4.70
OCDD Group Total ND 8.44
TCDF Group Total 55722-27-5 37.5 2.44
PeCDF Group Total 30402-15-4 ND 1.18
HxCDF Group Total 55684-94-1 ND 1.70
HpCDF Group Total 38998-75-3 ND 5.46
OCDF Group Total ND 6.50
TEQ ITEQ (ND=0; EMPC=0)0
ITEQ (ND=1/2EDL;EMPC=1/2EDL)2.77
ITEQ (ND=EDL EMPC=EDL)5.54
ITEQ (ND=0; EMPC=EMPC)0
ITEQ (ND=1/2EDL; EMPC=EMPC)2.77
ITEQ (ND=EDL; EMPC=EMPC)5.54
WTEQ (ND=0; EMPC=0)0
WTEQ (ND=1/2EDL;EMPC=1/2EDL)3.04
WTEQ (ND=EDL EMPC=EDL)6.08
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 10 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 129 of 315 ©Mostardi Platt
Details
Sample Name Mill On Run 3
Sampling Site
Enthalpy ID 0524-877-003-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-11 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 07:20 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)0
WTEQ (ND=1/2EDL; EMPC=EMPC)3.04
WTEQ (ND=EDL; EMPC=EMPC)6.08
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 11 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 130 of 315 ©Mostardi Platt
Details
Sample Name Mill Off Run 1
Sampling Site
Enthalpy ID 0524-877-004-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 08:11 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062429A 12.6 5.00 4.71
PeCDD 12378-PeCDD (S)40321-76-4 G28062429A ND 25.0 1.90 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062429A ND 25.0 1.48 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062429A ND 25.0 1.54 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062429A ND 25.0 1.63 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062429A ND 25.0 2.78 U
OCDD OCDD (S)3268-87-9 G28062429A ND 50.0 7.37 U
TCDF 2378-TCDF (S)51207-31-9 G28062429A 1450 5.00 4.50
PeCDF 12378-PeCDF (S)57117-41-6 G28062429A 154 25.0 3.73
PeCDF 23478-PeCDF (S)57117-31-4 G28062429A 190 25.0 3.54
HxCDF 123478-HxCDF (S)70648-26-9 G28062429A 15.6 25.0 3.59 J-EMPC
HxCDF 123678-HxCDF (S)57117-44-9 G28062429A 11.5 25.0 3.79 J
HxCDF 234678-HxCDF (S)60851-34-5 G28062429A 7.02 25.0 3.96 J
HxCDF 123789-HxCDF (S)72918-21-9 G28062429A 4.66 25.0 6.72 J-EMPC
HpCDF 1234678-HpCDF (S)67562-39-4 G28062429A ND 25.0 2.68 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062429A ND 25.0 4.18 U
OCDF OCDF (S)39001-02-0 G28062429A ND 50.0 4.34 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062429A 4.82 40-135%49.1%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062429A 6.04 40-135%49.7%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062429A 11.7 40-135%61.2%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062429A 10.8 40-135%72.1%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062429A 10.9 40-135%70.8%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062429A 29.2 40-135%56.3%
ES 13C-OCDD (ES)114423-97-1 G28062429A 19.3 40-135%43.0%
ES 13C-2378-TCDF (ES)89059-46-1 G28062429A 10.4 40-135%91.2%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062429A 14.5 40-135%84.1%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062429A 14.9 40-135%86.1%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062429A 12.8 40-135%65.5%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062429A 11.2 40-135%65.0%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062429A 11.7 40-135%62.6%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062429A 14.1 40-135%65.6%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062429A 10.6 40-135%58.0%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062429A 12.5 40-135%59.8%
ES 13C-OCDF (ES)109719-78-0 G28062429A 4.95 40-135%45.8%
SS 37Cl-2378-TCDD (SS)G28062429A 3.39 70-130%105.0%
SS 13C-12347-PeCDD (SS)G28062429A 13.4 70-130%94.6%
SS 13C-12346-PeCDF (SS)G28062429A 15.3 70-130%110.2%
SS 13C-123469-HxCDF (SS)G28062429A 35.1 70-130%105.2%
SS 13C-1234689-HpCDF (SS)G28062429A 45.8 70-130%109.7%
AS 13C-1368-TCDD (AS)G28062429A 4.51 20-150%49.8%
AS 13C-1368-TCDF (AS)G28062429A 8.61 20-150%86.5%
TCDD Group Total 41903-57-5 579 4.71
PeCDD Group Total 36088-22-9 43.9 1.90
HxCDD Group Total 34465-46-8 30.4 1.55
HpCDD Group Total 37871-00-4 ND 2.78
OCDD Group Total ND 7.37
TCDF Group Total 55722-27-5 75700 4.50
PeCDF Group Total 30402-15-4 3940 3.63
HxCDF Group Total 55684-94-1 134 4.51
HpCDF Group Total 38998-75-3 ND 3.43
OCDF Group Total ND 4.34
TEQ ITEQ (ND=0; EMPC=0)263
ITEQ (ND=1/2EDL;EMPC=1/2EDL)264
ITEQ (ND=EDL EMPC=EDL)265
ITEQ (ND=0; EMPC=EMPC)265
ITEQ (ND=1/2EDL; EMPC=EMPC)265
ITEQ (ND=EDL; EMPC=EMPC)266
WTEQ (ND=0; EMPC=0)221
WTEQ (ND=1/2EDL;EMPC=1/2EDL)223
WTEQ (ND=EDL EMPC=EDL)225
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 12 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 131 of 315 ©Mostardi Platt
Details
Sample Name Mill Off Run 1
Sampling Site
Enthalpy ID 0524-877-004-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 08:11 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)223
WTEQ (ND=1/2EDL; EMPC=EMPC)225
WTEQ (ND=EDL; EMPC=EMPC)226
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 13 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 132 of 315 ©Mostardi Platt
Details
Sample Name Mill Off Run 2
Sampling Site
Enthalpy ID 0524-877-005-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 09:02 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062430A 15.6 5.00 4.68
PeCDD 12378-PeCDD (S)40321-76-4 G28062430A ND 25.0 1.63 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062430A ND 25.0 1.59 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062430A ND 25.0 1.69 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062430A ND 25.0 1.79 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062430A ND 25.0 4.28 U
OCDD OCDD (S)3268-87-9 G28062430A ND 50.0 5.91 U
TCDF 2378-TCDF (S)51207-31-9 G28062430A 1610 5.00 4.11
PeCDF 12378-PeCDF (S)57117-41-6 G28062430A 237 25.0 3.90
PeCDF 23478-PeCDF (S)57117-31-4 G28062430A 276 25.0 3.83
HxCDF 123478-HxCDF (S)70648-26-9 G28062430A 37.0 25.0 2.88
HxCDF 123678-HxCDF (S)57117-44-9 G28062430A 20.6 25.0 3.15 J
HxCDF 234678-HxCDF (S)60851-34-5 G28062430A 13.4 25.0 3.27 J
HxCDF 123789-HxCDF (S)72918-21-9 G28062430A ND 25.0 5.47 U
HpCDF 1234678-HpCDF (S)67562-39-4 G28062430A ND 25.0 2.93 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062430A ND 25.0 4.48 U
OCDF OCDF (S)39001-02-0 G28062430A ND 50.0 4.21 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062430A 5.27 40-135%57.6%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062430A 9.14 40-135%54.2%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062430A 16.1 40-135%72.8%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062430A 14.9 40-135%84.7%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062430A 15.1 40-135%80.5%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062430A 9.94 40-135%65.9%
ES 13C-OCDD (ES)114423-97-1 G28062430A 32.9 40-135%47.4%
ES 13C-2378-TCDF (ES)89059-46-1 G28062430A 12.9 40-135%114.0%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062430A 10.7 40-135%95.9%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062430A 11.1 40-135%100.7%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062430A 12.4 40-135%78.7%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062430A 10.9 40-135%76.9%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062430A 11.4 40-135%73.1%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062430A 13.7 40-135%77.1%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062430A 16.3 40-135%66.8%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062430A 19.2 40-135%64.7%
ES 13C-OCDF (ES)109719-78-0 G28062430A 5.78 40-135%50.5%
SS 37Cl-2378-TCDD (SS)G28062430A 9.20 70-130%101.2%
SS 13C-12347-PeCDD (SS)G28062430A 16.1 70-130%96.3%
SS 13C-12346-PeCDF (SS)G28062430A 9.55 70-130%109.1%
SS 13C-123469-HxCDF (SS)G28062430A 29.2 70-130%101.3%
SS 13C-1234689-HpCDF (SS)G28062430A 63.8 70-130%107.1%
AS 13C-1368-TCDD (AS)G28062430A 4.93 20-150%58.1%
AS 13C-1368-TCDF (AS)G28062430A 10.7 20-150%108.0%
TCDD Group Total 41903-57-5 692 4.68
PeCDD Group Total 36088-22-9 76.9 1.63
HxCDD Group Total 34465-46-8 29.0 1.69
HpCDD Group Total 37871-00-4 ND 4.28
OCDD Group Total ND 5.91
TCDF Group Total 55722-27-5 80100 4.11
PeCDF Group Total 30402-15-4 5480 3.87
HxCDF Group Total 55684-94-1 237 3.69
HpCDF Group Total 38998-75-3 ND 3.71
OCDF Group Total ND 4.21
TEQ ITEQ (ND=0; EMPC=0)334
ITEQ (ND=1/2EDL;EMPC=1/2EDL)335
ITEQ (ND=EDL EMPC=EDL)336
ITEQ (ND=0; EMPC=EMPC)334
ITEQ (ND=1/2EDL; EMPC=EMPC)335
ITEQ (ND=EDL; EMPC=EMPC)336
WTEQ (ND=0; EMPC=0)274
WTEQ (ND=1/2EDL;EMPC=1/2EDL)275
WTEQ (ND=EDL EMPC=EDL)277
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 14 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 133 of 315 ©Mostardi Platt
Details
Sample Name Mill Off Run 2
Sampling Site
Enthalpy ID 0524-877-005-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 09:02 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)274
WTEQ (ND=1/2EDL; EMPC=EMPC)275
WTEQ (ND=EDL; EMPC=EMPC)277
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
Mostardi Platt Environmental - Elmhurst AshGrove Leamington Main Kiln Stack
EU 0524-877 Page 15 of 32
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 134 of 315 ©Mostardi Platt
Details
Sample Name Mill Off Run 3
Sampling Site
Enthalpy ID 0524-877-006-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 09:54 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062431A 18.7 5.00 2.83
PeCDD 12378-PeCDD (S)40321-76-4 G28062431A ND 25.0 1.59 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062431A ND 25.0 1.21 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062431A ND 25.0 1.24 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062431A ND 25.0 1.32 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062431A ND 25.0 2.19 U
OCDD OCDD (S)3268-87-9 G28062431A ND 50.0 4.02 U
TCDF 2378-TCDF (S)51207-31-9 G28062431A 1740 5.00 2.09
PeCDF 12378-PeCDF (S)57117-41-6 G28062431A 226 25.0 3.14
PeCDF 23478-PeCDF (S)57117-31-4 G28062431A 292 25.0 2.99
HxCDF 123478-HxCDF (S)70648-26-9 G28062431A 40.9 25.0 1.99
HxCDF 123678-HxCDF (S)57117-44-9 G28062431A 25.2 25.0 2.07
HxCDF 234678-HxCDF (S)60851-34-5 G28062431A 13.0 25.0 2.31 J-EMPC
HxCDF 123789-HxCDF (S)72918-21-9 G28062431A 7.08 25.0 3.47 J
HpCDF 1234678-HpCDF (S)67562-39-4 G28062431A 8.68 25.0 2.17 J
HpCDF 1234789-HpCDF (S)55673-89-7 G28062431A ND 25.0 3.34 U
OCDF OCDF (S)39001-02-0 G28062431A ND 50.0 2.16 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062431A 4.93 40-135%75.2%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062431A 8.20 40-135%74.4%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062431A 14.2 40-135%105.3%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062431A 13.1 40-135%118.9%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062431A 13.3 40-135%113.6%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062431A 13.8 40-135%102.5%
ES 13C-OCDD (ES)114423-97-1 G28062431A 7.12 40-135%81.5%
ES 13C-2378-TCDF (ES)89059-46-1 G28062431A 10.8 40-135%133.0%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062431A 13.4 40-135%120.6%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062431A 13.9 40-135%125.9%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062431A 13.2 40-135%108.9%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062431A 11.6 40-135%102.8%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062431A 12.2 40-135%99.3%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062431A 14.6 40-135%110.4%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062431A 8.23 40-135%100.6%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062431A 9.72 40-135%105.4%
ES 13C-OCDF (ES)109719-78-0 G28062431A 6.44 40-135%84.8%
SS 37Cl-2378-TCDD (SS)G28062431A 3.48 70-130%103.3%
SS 13C-12347-PeCDD (SS)G28062431A 10.9 70-130%96.5%
SS 13C-12346-PeCDF (SS)G28062431A 8.95 70-130%107.8%
SS 13C-123469-HxCDF (SS)G28062431A 23.0 70-130%104.4%
SS 13C-1234689-HpCDF (SS)G28062431A 23.7 70-130%107.1%
AS 13C-1368-TCDD (AS)G28062431A 4.60 20-150%75.5%
AS 13C-1368-TCDF (AS)G28062431A 8.96 20-150%127.1%
TCDD Group Total 41903-57-5 763 2.83
PeCDD Group Total 36088-22-9 77.7 1.59
HxCDD Group Total 34465-46-8 31.3 1.26
HpCDD Group Total 37871-00-4 ND 2.19
OCDD Group Total ND 4.02
TCDF Group Total 55722-27-5 89800 2.09
PeCDF Group Total 30402-15-4 5620 3.06
HxCDF Group Total 55684-94-1 258 2.46
HpCDF Group Total 38998-75-3 8.68 2.76
OCDF Group Total ND 2.16
TEQ ITEQ (ND=0; EMPC=0)358
ITEQ (ND=1/2EDL;EMPC=1/2EDL)358
ITEQ (ND=EDL EMPC=EDL)359
ITEQ (ND=0; EMPC=EMPC)359
ITEQ (ND=1/2EDL; EMPC=EMPC)360
ITEQ (ND=EDL; EMPC=EMPC)360
WTEQ (ND=0; EMPC=0)295
WTEQ (ND=1/2EDL;EMPC=1/2EDL)296
WTEQ (ND=EDL EMPC=EDL)297
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Details
Sample Name Mill Off Run 3
Sampling Site
Enthalpy ID 0524-877-006-1 Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date 2024-06-12 00:00 Instrument Gandalf
Received Date 2024-06-20 Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 09:54 Split Factor 2
SampleType Sample Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)296
WTEQ (ND=1/2EDL; EMPC=EMPC)297
WTEQ (ND=EDL; EMPC=EMPC)298
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QC Data

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Details
Sample Name MB-17642-DF
Sampling Site
Enthalpy ID MB-17642-DF Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date Instrument Gandalf
Received Date Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 04:46 Split Factor 2
SampleType Blank Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062425A ND 5.00 3.15 U
PeCDD 12378-PeCDD (S)40321-76-4 G28062425A ND 25.0 2.30 U
HxCDD 123478-HxCDD (S)39227-28-6 G28062425A ND 25.0 2.69 U
HxCDD 123678-HxCDD (S)57653-85-7 G28062425A ND 25.0 2.48 U
HxCDD 123789-HxCDD (S)19408-74-3 G28062425A ND 25.0 3.47 U
HpCDD 1234678-HpCDD (S)35822-46-9 G28062425A ND 25.0 7.55 U
OCDD OCDD (S)3268-87-9 G28062425A ND 50.0 16.4 U
TCDF 2378-TCDF (S)51207-31-9 G28062425A ND 5.00 1.61 U
PeCDF 12378-PeCDF (S)57117-41-6 G28062425A ND 25.0 1.44 U
PeCDF 23478-PeCDF (S)57117-31-4 G28062425A ND 25.0 1.36 U
HxCDF 123478-HxCDF (S)70648-26-9 G28062425A ND 25.0 1.96 U
HxCDF 123678-HxCDF (S)57117-44-9 G28062425A ND 25.0 2.08 U
HxCDF 234678-HxCDF (S)60851-34-5 G28062425A ND 25.0 2.35 U
HxCDF 123789-HxCDF (S)72918-21-9 G28062425A ND 25.0 4.58 U
HpCDF 1234678-HpCDF (S)67562-39-4 G28062425A ND 25.0 4.68 U
HpCDF 1234789-HpCDF (S)55673-89-7 G28062425A ND 25.0 8.72 U
OCDF OCDF (S)39001-02-0 G28062425A ND 50.0 11.2 U
ES 13C-2378-TCDD (ES)76523-40-5 G28062425A 12.7 40-135%75.4%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062425A 12.6 40-135%66.0%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062425A 24.3 40-135%79.5%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062425A 22.4 40-135%120.7%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062425A 22.8 40-135%97.7%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062425A 24.9 40-135%66.5%
ES 13C-OCDD (ES)114423-97-1 G28062425A 43.3 40-135%44.3%
ES 13C-2378-TCDF (ES)89059-46-1 G28062425A 35.1 40-135%129.8%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062425A 41.0 40-135%115.2%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062425A 42.3 40-135%112.5%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062425A 29.1 40-135%96.9%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062425A 25.6 40-135%113.3%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062425A 26.7 40-135%89.0%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062425A 32.1 40-135%100.2%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062425A 38.7 40-135%72.6%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062425A 45.7 40-135%66.4%
ES 13C-OCDF (ES)109719-78-0 G28062425A 19.1 40-135%43.8%
SS 37Cl-2378-TCDD (SS)G28062425A 9.94 70-130%96.8%
SS 13C-12347-PeCDD (SS)G28062425A 21.0 70-130%97.4%
SS 13C-12346-PeCDF (SS)G28062425A 34.2 70-130%108.6%
SS 13C-123469-HxCDF (SS)G28062425A 50.2 70-130%85.9%
SS 13C-1234689-HpCDF (SS)G28062425A 139 70-130%102.7%
AS 13C-1368-TCDD (AS)G28062425A 11.8 20-150%83.5%
AS 13C-1368-TCDF (AS)G28062425A 29.1 20-150%136.6%
TCDD Group Total 41903-57-5 5.77 3.15
PeCDD Group Total 36088-22-9 ND 2.30
HxCDD Group Total 34465-46-8 15.6 2.88
HpCDD Group Total 37871-00-4 ND 7.55
OCDD Group Total ND 16.4
TCDF Group Total 55722-27-5 ND 1.61
PeCDF Group Total 30402-15-4 ND 1.40
HxCDF Group Total 55684-94-1 ND 2.74
HpCDF Group Total 38998-75-3 ND 6.70
OCDF Group Total ND 11.2
TEQ ITEQ (ND=0; EMPC=0)0
ITEQ (ND=1/2EDL;EMPC=1/2EDL)3.70
ITEQ (ND=EDL EMPC=EDL)7.41
ITEQ (ND=0; EMPC=EMPC)0
ITEQ (ND=1/2EDL; EMPC=EMPC)3.70
ITEQ (ND=EDL; EMPC=EMPC)7.41
WTEQ (ND=0; EMPC=0)0
WTEQ (ND=1/2EDL;EMPC=1/2EDL)4.12
WTEQ (ND=EDL EMPC=EDL)8.24
Enthalpy Analytical
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Details
Sample Name MB-17642-DF
Sampling Site
Enthalpy ID MB-17642-DF Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date Instrument Gandalf
Received Date Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.02
AnalysisDate 2024-06-29 04:46 Split Factor 2
SampleType Blank Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)0
WTEQ (ND=1/2EDL; EMPC=EMPC)4.12
WTEQ (ND=EDL; EMPC=EMPC)8.24
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
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Details
Sample Name BCS-17642-DF
Sampling Site
Enthalpy ID BCS-17642-DF Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date Instrument Gandalf
Received Date Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.04
AnalysisDate 2024-06-29 03:03 Split Factor N/A
SampleType Control Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
TCDD 2378-TCDD (S)1746-01-6 G28062423A 450 10.0 4.78 70-130%112.4%
PeCDD 12378-PeCDD (S)40321-76-4 G28062423A 1980 50.0 9.98 70-130%99.0%
HxCDD 123478-HxCDD (S)39227-28-6 G28062423A 1970 50.0 12.9 70-130%98.6%
HxCDD 123678-HxCDD (S)57653-85-7 G28062423A 1980 50.0 12.5 70-130%99.2%
HxCDD 123789-HxCDD (S)19408-74-3 G28062423A 1940 50.0 14.1 70-130%97.1%
HpCDD 1234678-HpCDD (S)35822-46-9 G28062423A 2030 50.0 27.0 70-130%101.5%
OCDD OCDD (S)3268-87-9 G28062423A 4290 100 37.5 70-130%107.3%
TCDF 2378-TCDF (S)51207-31-9 G28062423A 482 10.0 4.81 70-130%120.4%
PeCDF 12378-PeCDF (S)57117-41-6 G28062423A 2220 50.0 9.90 70-130%110.9%
PeCDF 23478-PeCDF (S)57117-31-4 G28062423A 2300 50.0 9.39 70-130%114.8%
HxCDF 123478-HxCDF (S)70648-26-9 G28062423A 2170 50.0 21.7 70-130%108.5%
HxCDF 123678-HxCDF (S)57117-44-9 G28062423A 2150 50.0 23.1 70-130%107.3%
HxCDF 234678-HxCDF (S)60851-34-5 G28062423A 2040 50.0 22.8 70-130%102.2%
HxCDF 123789-HxCDF (S)72918-21-9 G28062423A 1960 50.0 41.5 70-130%97.9%
HpCDF 1234678-HpCDF (S)67562-39-4 G28062423A 2290 50.0 20.5 70-130%114.5%
HpCDF 1234789-HpCDF (S)55673-89-7 G28062423A 2070 50.0 38.0 70-130%103.3%
OCDF OCDF (S)39001-02-0 G28062423A 4390 100 56.4 70-130%109.9%
ES 13C-2378-TCDD (ES)76523-40-5 G28062423A 14.4 40-135%71.0%
ES 13C-12378-PeCDD (ES)109719-79-1 G28062423A 22.7 40-135%70.8%
ES 13C-123478-HxCDD (ES)109719-80-4 G28062423A 29.4 40-135%112.6%
ES 13C-123678-HxCDD (ES)109719-81-5 G28062423A 27.1 40-135%133.6%
ES 13C-123789-HxCDD (ES)109719-82-6 G28062423A 27.6 40-135%126.1%
ES 13C-1234678-HpCDD (ES)109719-83-7 G28062423A 22.9 40-135%111.2%
ES 13C-OCDD (ES)114423-97-1 G28062423A 18.4 40-135%102.4%
ES 13C-2378-TCDF (ES)89059-46-1 G28062423A 42.5 40-135%127.2%
ES 13C-12378-PeCDF (ES)109719-77-9 G28062423A 43.4 40-135%118.6%
ES 13C-23478-PeCDF (ES)116843-02-8 G28062423A 44.8 40-135%119.1%
ES 13C-123478-HxCDF (ES)114423-98-2 G28062423A 36.7 40-135%117.9%
ES 13C-123678-HxCDF (ES)116843-03-9 G28062423A 32.3 40-135%120.8%
ES 13C-234678-HxCDF (ES)116843-05-1 G28062423A 33.7 40-135%115.9%
ES 13C-123789-HxCDF (ES)116843-04-0 G28062423A 40.5 40-135%129.0%
ES 13C-1234678-HpCDF (ES)109719-84-8 G28062423A 40.6 40-135%112.6%
ES 13C-1234789-HpCDF (ES)109719-94-0 G28062423A 47.9 40-135%117.5%
ES 13C-OCDF (ES)109719-78-0 G28062423A 10.2 40-135%106.9%
SS 37Cl-2378-TCDD (SS)G28062423A 7.48 70-130%98.5%
SS 13C-12347-PeCDD (SS)G28062423A 29.2 70-130%91.5%
SS 13C-12346-PeCDF (SS)G28062423A 26.7 70-130%102.6%
SS 13C-123469-HxCDF (SS)G28062423A 69.6 70-130%95.6%
SS 13C-1234689-HpCDF (SS)G28062423A 106 70-130%103.7%
AS 13C-1368-TCDD (AS)G28062423A 13.4 20-150%72.4%
AS 13C-1368-TCDF (AS)G28062423A 35.3 20-150%124.4%
TCDD Group Total 41903-57-5 1720 4.78
PeCDD Group Total 36088-22-9 7030 9.98
HxCDD Group Total 34465-46-8 9130 13.2
HpCDD Group Total 37871-00-4 4980 27.0
OCDD Group Total 4290 37.5
TCDF Group Total 55722-27-5 1970 4.81
PeCDF Group Total 30402-15-4 7460 9.64
HxCDF Group Total 55684-94-1 13400 27.3
HpCDF Group Total 38998-75-3 4360 29.2
OCDF Group Total 4390 56.4
TEQ ITEQ (ND=0; EMPC=0)4240
ITEQ (ND=1/2EDL;EMPC=1/2EDL)4240
ITEQ (ND=EDL EMPC=EDL)4240
ITEQ (ND=0; EMPC=EMPC)4240
ITEQ (ND=1/2EDL; EMPC=EMPC)4240
ITEQ (ND=EDL; EMPC=EMPC)4240
WTEQ (ND=0; EMPC=0)4720
WTEQ (ND=1/2EDL;EMPC=1/2EDL)4720
WTEQ (ND=EDL EMPC=EDL)4720
Enthalpy Analytical
Job No.: 0524-877-1 EPA Method 23
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Details
Sample Name BCS-17642-DF
Sampling Site
Enthalpy ID BCS-17642-DF Prep Batch EU17642
Matrix air Analyst jemunoz
Sampling Date Instrument Gandalf
Received Date Sample Vol mL N/A
Prep Date 2024-06-24 16:18 Extract Vol mL 0.04
AnalysisDate 2024-06-29 03:03 Split Factor N/A
SampleType Control Method Code EU-045-23
Compound CAS Injection
File
Name
Sample
Concentration
pg
LOQ
pg
EDL
pg
Recovery
Limits
Recovery Flags
WTEQ (ND=0; EMPC=EMPC)4720
WTEQ (ND=1/2EDL; EMPC=EMPC)4720
WTEQ (ND=EDL; EMPC=EMPC)4720
Enthalpy Analytical
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Narrative Summary

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Enthalpy Analytical Narrative Summary
Company
Job No.
Client ID.
Mostardi Platt Environmental - Elmhurst
0524-877-1
AshGrove Leamington Site: Main Kiln Stack
1. Custody
Cherith McCullagh received the samples in two separate coolers ranging from 24.2 °C to 24.9 °
after being relinquished by Mostardi Platt Environmental - Elmhurst.
The samples were received in good condition. Prior to, during, and after analysis, the samples
were kept under lock with access only to authorized personnel by Enthalpy Analytical, LLC.
Table 1 - Sample Inventory
EU Lab Sample ID Client Sample ID Matrix Received
0524-877-001-1 Mill On Run 1 air 2024-06-20
0524-877-002-1 Mill On Run 2 air 2024-06-20
0524-877-003-1 Mill On Run 3 air 2024-06-20
0524-877-004-1 Mill Off Run 1 air 2024-06-20
0524-877-005-1 Mill Off Run 2 air 2024-06-20
0524-877-006-1 Mill Off Run 3 air 2024-06-20
2. Methods and Analytes
A list of analytes of interest and corresponding methods of analysis is shown in Table 3.
Abbreviations are defined in the listed Appendices.
Table 3 - Methods and Analytes
EU Method Analytes Cleanup Method
EU-045 PCDD/PCDF EU-046
3. Analysis
The samples were analyzed using Agilent Technologies Model# 6890 High-Resolution GC/
Waters High-Resolution Mass-Spectrometer (HRGC/HRMS "Gandalf").
4. Calibration
The Initial Calibration (ICAL), Initial Calibration Verification (ICV), and continuing calibration
(concal) met method criteria.
5. QC Notes
The HRMS system displayed mass resolving power of at least 10,000 during the analysis.
Labeled standard recovery values in the Batch Control Sample (BCS) and method blank (MB)
were acceptable. The analyte recovery values in the BCS were acceptable.
GC column performance check passed method criteria.
EPA Method 23 samples were extracted within 30 days, and extracts analyzed within 45 days.
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Enthalpy Analytical Narrative Summary
Company
Job No.
Client ID.
Mostardi Platt Environmental - Elmhurst
0524-877-1
AshGrove Leamington Site: Main Kiln Stack
6. Reporting Notes
The results presented in this report are representative of the samples as provided to the
laboratory.
The TEQ was calculated and reported using I-TEF and WHO-2005 TEF, calculated by
multiplying the concentration for each 2,3,7,8-substituted PCDD/F by its toxic equivalency factor
(TEF). The Totals and Detection Limits have been included in the report. The TEQ is reported
with and without EMPCs included. Additionally, the TEQ may be reported with non-detects
treated as having a concentration of zero, a concentration of one-half the EDL, and/or a
concentration equal to the EDL.
These analyses met the requirements of the TNI Standard. Any deviations from the
requirements of the reference method or TNI Standard have been stated above.
Enthalpy Analytical, LLC in Wilmington NC is accredited by the Louisiana Department of
Environmental Quality to the 2009 TNI Standard under certificate number 05075.
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General Reporting Notes – Data Qualifiers

EU116_v8 (General Reporting Notes-Data Qualifiers) Enthalpy Analytical, LLC – Wilmington, NC
The following are general reporting notes that are applicable to all Enthalpy Analytical, LLC -
Wilmington, NC data reports, unless specifically noted otherwise.
General Data Qualifiers
 Ac - Alternate calculation flag indicates the es recovery was calculated using the opening concal
when either of the following situations is encountered in the data processing software: the ES
recovery is over 400% or the JS is not detected.
 B – The analyte was found in the method blank, at a concentration that was at least 10% of the
amount in the sample.
 Cxx – Two or more congeners co-elute. In EDDs, C denotes the lowest IUPAC congener in a co-
elution group and additional co-eluters for the group (‘xx’) are shown with the number of the
lowest IUPAC co-eluter.
 E – The reported concentration exceeds the calibration range (upper point of the calibration
curve). For HRMS data, this condition does not imply additional measurement uncertainty. For
LC-MS/MS data, these values should be considered as having measurement uncertainty higher
than values within the calibration range.
 EDL – Estimated Detection Level: The EDL is unique to isotope dilution methods and reflects
the conditions of analysis at the time of analysis, including the equipment used. Where the MDL
is a static value, the EDL is a dynamic value.
 EMPC – Estimated Maximum Possible Concentration: EMPC is specific to Dioxin/Furan tests to
indicate the determined ion-abundance ratio was outside the allowed theoretical range (usually
due to being near the detection limit, although it can very rarely be caused by a co-eluting
interference). The EMPC concentration is adjusted to reflect the value at the theoretical ion-
abundance ratio.
 I/IR – The ion ratio between the primary and secondary ions was observed to be outside the
method criteria. The analyte concentration may be inaccurate due to interference.
 J – The analyte has a concentration below the minimum calibration level (LOQ value) but greater
than the LOD. These values should be considered as having measurement uncertainty higher than
values within the calibration range
 L - For reports containing PFAS analytes only, this flag indicates that an analyte has a
concentration below the Minimum Detection Limit (MDL) . The reported concentration is not
recommended for regulatory use as the analyte signal may have a signal-to-noise ratio less than
the criteria deemed necessary to be considered a detected analyte.
 LOD – Limit of Detection: For reports conforming to the DOD ELAP QSM, this is the QSM-
defined LOD. For reports conforming to TNI requirements (but not DOD ELAP QSM
requirements), this value is the minimum detection limit (MDL). The LOD is adjusted for sample
weight or volume.
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Page 145 of 315 ©Mostardi Platt
General Reporting Notes – Data Qualifiers

EU116_v8 (General Reporting Notes-Data Qualifiers) Enthalpy Analytical, LLC – Wilmington, NC
 LOQ – Limit of Quantitation: For reports conforming to the DOD ELAP QSM, this is the QSM-
defined LOQ. For reports conforming to TNI requirements (but not DOD ELAP QSM
requirements), this value is the reporting limit (RL). The LOQ is adjusted for sample weight or
volume.
 <LOD() – Analyte was not found at a concentration high enough to be reported as detected. It is
reported as less than the LOD, and the LOD is given in the parentheses.
 <LOQ() – Analyte was not found at a concentration high enough to be reported as above the
QSM-defined LOQ or TNI defined Reporting Limit. It is reported as less than the LOQ, and the
LOQ is given in the parentheses.
 ND – Indicates a non-detect.
 NR – Indicates a value that is not reportable due to issues observed in sample preparation or
analysis.
 PR – The associated congener(s) is(are) poorly resolved.
 QI – Indicates the presence of a quantitative interference.
 RL – Reporting Limit. Lowest reportable value. The level is higher than the MDL.
 SI – Denotes “Single Ion Mode” and is utilized for PCBs where the secondary ion trace has a
significantly elevated noise level due to background PFK. Responses for such peaks are
calculated using an EMPC approach based solely on the primary ion area(s) and may be
considered estimates.
 U – The analyte was not detected.
 V / Q – The labeled standard recovery is not within method control limits.
 X – Indicates the result is from re-injection/repeat/second-column analysis.
Lab Identifiers/ Data Attributes
 AR – Indicates use of the archived portion of the sample extract.
 CU – Indicates a sample that required additional clean-up prior to HRMS injection/processing.
 D – Dilution Data. Result was obtained from the analysis of a dilution. The number that follows
the “D” indicates the dilution factor.
 DE – Indicates a dilution performed with the addition of ES (Extraction Standard) solution.
 DUP – Designation for a duplicate sample.
 MS – Designation for a matrix spike.
 MSD – Designation for a matrix spike duplicate.
EU 0524-877 Page 27 of 32
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Page 146 of 315 ©Mostardi Platt
General Reporting Notes – Data Qualifiers

EU116_v8 (General Reporting Notes-Data Qualifiers) Enthalpy Analytical, LLC – Wilmington, NC
 R – Indicates a re-extraction of the sample.
 RJ – Indicates a reinjection of the sample extract.
 S – Indicates a sample split. The number that follows the “S” indicates the split factor.
 SAT – Indicates an analyte saturated the detector.
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Page 147 of 315 ©Mostardi Platt

Sample Custody
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EU 0524-877 Page 30 of 32
Project No. M242413B
Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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EU 0524-877 Page 31 of 32
Project No. M242413B
Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
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This Is The Last Page
Of This Report.

EU 0524-877 Page 32 of 32
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Page 151 of 315 ©Mostardi Platt
Appendix D - Reference Method Test Data
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 152 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Run 1 Run 2 Run 3 Run 4
Temp ID:CM18 CM18 CM18 CM18
Meter ID:CM18 CM18 CM18 CM18
Pitot ID:4067 4067 4067 4067
Filter ID:10524 10526 9258 15538
Filter Pre-Weight (grams):0.45457 0.45195 0.45206 0.45985
Nozzle Diameter (Inches):0.311 0.311 0.311 0.311
Meter Calibration Date:5/21/2024 5/21/2024 5/21/2024 5/21/2024
Meter Calibration Factor (Y):0.990 0.990 0.990 0.990
Meter Orifice Setting (Delta H):1.736 1.736 1.736 1.736
Nozzle Kit ID Number and Material:Quartz Quartz Quartz Quartz
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Moisture Balance ID:
# of Runs
Glass
EROD
RODS
24
Flange
Ash Grove Cement Company
Leamington Cement Plant
Clinker Cooler Stack
M242413
5
5.0
5.0
6
5.00
0.840
6.0
3.4
120
Hot Box
Normal
4
LV 1
Horizontal
Circular
4
8.75
2.5
4.75
60.132
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 153 of 315 ©Mostardi Platt
Project Number M242413 Source Condition:NormalClient:Ash Grove Cement Company Run No.: 1
Facility:Leamington Cement Plant Date:6/13/2024
Location:Clinker Cooler Stack Start Time:6:45
Pitot ID: 4067 End Time:7:05Pitot Coefficient:0.840 RM Testers:ER
Probe Length:6 Port Length:4.75
DP Sqrt. Temp Yaw Velocity DP Sqrt. Temp Yaw Velocity
Port Point (in. H2O) DP (oF)(o) (V) Port Point (in. H2O) DP (oF)(o) (V)
A10.35 0.5916 233.0 3.0 3.0 43.27 C10.34 0.5831 233.0 3.0 3.0 42.65
A20.32 0.5657 233.0 1.0 1.0 41.37 C20.32 0.5657 233.0 1.0 1.0 41.37
A30.30 0.5477 233.0 4.0 4.0 40.06 C30.29 0.5385 233.0 1.0 1.0 39.39
A40.28 0.5292 235.0 2.0 2.0 38.76 C40.27 0.5196 235.0 3.0 3.0 38.06
A50.25 0.5000 235.0 3.0 3.0 36.62 C50.24 0.4899 235.0 0.0 0.0 35.88
A60.20 0.4472 235.0 2.0 2.0 32.76 C60.22 0.4690 235.0 0.0 0.0 34.35
B10.33 0.5745 230.0 0.0 0.0 41.92 D10.31 0.5568 232.0 2.0 2.0 40.69
B20.32 0.5657 231.0 2.0 2.0 41.31 D20.30 0.5477 232.0 3.0 3.0 40.03
B30.30 0.5477 231.0 1.0 1.0 40.00 D30.29 0.5385 232.0 0.0 0.0 39.36
B40.28 0.5292 232.0 0.0 0.0 38.67 D40.26 0.5099 232.0 1.0 1.0 37.27
B50.25 0.5000 233.0 3.0 3.0 36.57 D50.23 0.4796 232.0 0.0 0.0 35.05
B60.21 0.4583 233.0 4.0 4.0 33.52 D60.22 0.4690 232.0 4.0 4.0 34.28
Average Yaw Angle 1.8
Test Parameters
Pbar - Barometric pressure, inches Hg 25.08 % CO2 0.00
Pg - Stack Pressure, inches of H2O -0.40 % O2 20.90
Ps - Absolute stack pressure, inches Hg 25.05 % N2 79.10
ts - Average stack temperature, oF 232.9 Md - dry basis lb/lb mole 28.84
Shape of Duct: (C or R)C Ms - wet basis lb/lb mole 26.67
Stack Diameter, Feet Average Sqrt DP 0.5260
Bws - Moisture content fraction 0.200
Cross Sectional Area of Stack, Ft2 60.13
METHOD 2 VOLUMETRIC FLOW DATA
AET-014 ISO Template V24.4 4/6/2022
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Page 154 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Normal
2.16 in. H2O -0.40 in. H2O
81.9 °F 25.05 in. Hg. abs.
0.533 in. H2O %
232.7 °F %
111.808 ft3 #VALUE! %
90.982 dscf 29.000 lb/lb mole
1.700 wscf 28.798 lb/lb mole
102.1 %I #VALUE! %
37.472 fps
120.00 in mins. 135,197 acfm
0.311 in inches 84,696 dscfm
25.08 in Hg 86,279 scfm
Calculated Fo:
Fo Validity: #N/A
2136.1 ml 788.7 grams
2154.6 ml 806.3 grams
18.5 ml 17.6 grams
36.1 0.018
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 7:30:00 0.32 2.42 93.407 230 77 77 243 243 50
1-2 7:35:00 0.30 2.27 98.331 230 77 77 250 250 50
1-3 7:40:00 0.29 2.19 103.090 232 77 77 250 245 51
1-4 7:45:00 0.27 2.04 107.761 232 77 77 250 245 51
1-5 7:50:00 0.25 1.89 112.249 232 78 78 255 250 51
1-6 7:55:00 0.24 1.81 116.614 232 78 78 253 250 51
8:00:00 120.872
2-1 8:03:00 0.35 2.66 120.872 231 79 79 250 253 52
2-2 8:08:00 0.32 2.43 126.017 231 79 79 255 245 52
2-3 8:13:00 0.30 2.28 130.946 231 79 79 253 250 53
2-4 8:18:00 0.29 2.20 135.719 231 80 80 245 252 53
2-5 8:23:00 0.25 1.90 140.440 231 80 80 250 252 54
2-6 8:28:00 0.22 1.68 144.784 231 81 81 250 250 54
8:33:00 148.887
3-1 8:36:00 0.34 2.59 148.887 232 82 82 250 253 55
3-2 8:41:00 0.32 2.44 153.982 232 82 82 255 245 55
3-3 8:46:00 0.29 2.21 158.955 234 83 83 253 250 55
3-4 8:51:00 0.30 2.29 163.672 234 84 84 245 252 53
3-5 8:56:00 0.27 2.06 168.459 234 84 84 250 245 52
3-6 9:01:00 0.27 2.06 173.018 235 85 85 252 250 53
9:06:00 177.583
4-1 9:09:00 0.31 2.36 177.583 235 85 85 250 250 53
4-2 9:14:00 0.30 2.29 182.484 235 86 86 252 250 54
4-3 9:19:00 0.27 2.07 187.285 235 87 87 252 255 54
4-4 9:24:00 0.29 2.22 191.887 235 88 88 250 250 55
4-5 9:29:00 0.24 1.84 196.624 235 88 88 252 245 55
4-6 9:34:00 0.23 1.77 200.971 235 89 89 255 250 56
9:39:00 205.215
Total 2:00:00 111.808 81.9 81.9
Average 2.16 232.7 81.9
Min 1.68 230.0 77.0
Max 2.66 235.0 89.0
Volumetric Flow:
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Silica Initial Wt.
Test Length:
Nozzle Diameter:
MOISTURE DETERMINATION
Volumetric Flow:
Silica Final Wt.
Barometric Pressure:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Moisture, Bws:
Silica Difference:
Total Water Gain:
Final Impinger Content:
Meter Temp
Impinger Difference:
Start Time:
Meter Volume, Vwstd:
Source Condition:
Nitrogen:
STACK CONDITIONS
Static Pressure
Sqrt ∆P:
End Time:
Carbon Dioxide:
Run 1 - Method 5
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
7:30
6/13/24
9:39
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 155 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV 1
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 748.9 734.0 14.9
DI Water 737.8 734.9 2.9
Empty 667.9 667.2 0.7
Silica Gel 806.3 788.7 17.6
2,154.6 2,136.1 18.5
Liquid Final Liquid Initial Liquid Gain
806.3 788.7 17.6
Silica Final Silica Initial Silica Gain
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 156 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Normal
2.11 In. H2O -0.40 in. H2O
95.5 °F 25.05 in. Hg. abs.
0.521 In. H2O %
237.5 °F %
111.806 ft3 #VALUE! %
88.735 dscf 29.000 lb/lb mole
1.338 wscf 28.837 lb/lb mole
101.8 %I #VALUE! %
36.780 fps
120.00 in mins. 132,700 acfm
0.311 in inches 82,855 dscfm
25.08 in Hg 84,104 scfm
Calculated Fo:
Fo Validity: #N/A
2244.7 ml 820.5 grams
2262.9 ml 830.7 grams
18.2 ml 10.2 grams
28.4 0.015
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 9:45:00 0.34 2.62 6.491 238 92 92 253 250 62
1-2 9:50:00 0.32 2.46 11.678 238 92 92 245 252 62
1-3 9:55:00 0.29 2.23 16.681 238 92 92 250 245 62
1-4 10:00:00 0.28 2.16 21.482 238 93 93 252 250 63
1-5 10:05:00 0.23 1.77 26.189 238 93 93 255 252 63
1-6 10:10:00 0.22 1.70 30.455 238 93 93 250 252 63
10:15:00 34.627
2-1 10:18:00 0.33 2.55 34.627 238 95 95 250 245 64
2-2 10:23:00 0.31 2.40 39.765 238 95 95 250 245 64
2-3 10:28:00 0.30 2.32 44.736 237 95 95 255 250 64
2-4 10:33:00 0.26 2.01 49.629 237 95 95 253 250 65
2-5 10:38:00 0.23 1.78 54.184 238 95 95 245 252 65
2-6 10:43:00 0.21 1.63 58.445 237 96 96 240 245 65
10:48:00 62.546
3-1 10:51:00 0.31 2.41 62.546 237 96 96 250 250 64
3-2 10:56:00 0.30 2.33 67.539 237 96 96 245 250 64
3-3 11:01:00 0.27 2.09 72.441 237 96 96 250 255 64
3-4 11:06:00 0.29 2.25 77.091 237 96 96 252 253 63
3-5 11:11:00 0.24 1.86 81.911 237 97 97 255 250 63
3-6 11:16:00 0.23 1.79 86.283 237 97 97 255 252 63
11:21:00 90.583
4-1 11:24:00 0.30 2.33 90.583 238 98 98 255 253 64
4-2 11:29:00 0.29 2.25 95.489 238 98 98 253 245 64
4-3 11:34:00 0.27 2.10 100.342 237 98 98 245 250 64
4-4 11:39:00 0.25 1.94 104.989 238 98 98 250 250 65
4-5 11:44:00 0.24 1.87 109.497 237 98 98 250 255 65
4-6 11:49:00 0.24 1.87 113.877 237 98 98 253 250 65
11:54:00 118.297
Total 2:00:00 111.806 95.5 95.5
Average 2.11 237.5 95.5
Min 1.63 237.0 92.0
Max 2.62 238.0 98.0
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd: Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
6/13/24
9:45
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
11:54
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Run 2 - Method 5
Carbon Dioxide:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 157 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV 1
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 759.2 748.5 10.7
DI Water 756.9 750.2 6.7
Empty 746.8 746.0 0.8
Silica Gel 830.7 820.5 10.2
2,262.9 2,244.7 18.2
Liquid Final Liquid Initial Liquid Gain
830.7 820.5 10.2
Silica Final Silica Initial Silica Gain
250
500
750
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 158 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Normal
2.07 In. H2O -0.40 in. H2O
102.0 °F 25.05 in. Hg. abs.
0.513 In. H2O %
240.0 °F %
111.192 ft3 #VALUE! %
87.215 dscf 29.000 lb/lb mole
1.535 wscf 28.810 lb/lb mole
102.0 %I #VALUE! %
36.295 fps
120.00 in mins. 130,948 acfm
0.311 in inches 81,267 dscfm
25.08 in Hg 82,697 scfm
Calculated Fo:
Fo Validity: #N/A
2279.0 ml 836.1 grams
2299.0 ml 848.7 grams
20.0 ml 12.6 grams
32.6 0.017
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 12:10:00 0.31 2.41 19.745 240 100 100 253 245 60
1-2 12:15:00 0.30 2.33 24.743 240 100 100 245 250 60
1-3 12:20:00 0.28 2.18 29.670 240 100 100 250 250 60
1-4 12:25:00 0.27 2.10 34.449 240 100 100 250 252 61
1-5 12:30:00 0.24 1.87 39.123 240 100 100 252 245 61
1-6 12:35:00 0.23 1.79 43.509 240 100 100 250 250 61
12:40:00 47.843
2-1 12:43:00 0.30 2.34 47.843 241 101 101 245 250 62
2-2 12:48:00 0.28 2.18 52.765 241 101 101 250 245 63
2-3 12:53:00 0.27 2.10 57.549 241 101 101 250 254 63
2-4 12:58:00 0.24 1.87 62.228 241 101 101 252 250 63
2-5 13:03:00 0.25 1.95 66.639 241 101 101 255 250 64
2-6 13:08:00 0.21 1.64 71.121 241 102 102 245 245 64
13:13:00 75.255
3-1 13:16:00 0.33 2.58 75.255 239 102 102 250 250 65
3-2 13:21:00 0.30 2.35 80.434 239 102 102 252 253 64
3-3 13:26:00 0.28 2.19 85.382 239 102 102 245 245 64
3-4 13:31:00 0.27 2.12 90.162 239 103 103 250 250 64
3-5 13:36:00 0.23 1.80 94.884 239 103 103 255 250 63
3-6 13:41:00 0.21 1.65 99.224 239 103 103 255 252 63
13:46:00 103.371
4-1 13:49:00 0.31 2.42 103.371 240 103 103 253 250 64
4-2 13:54:00 0.30 2.35 108.416 240 104 104 245 252 64
4-3 13:59:00 0.27 2.12 113.370 240 104 104 250 250 64
4-4 14:04:00 0.25 1.96 118.065 240 105 105 252 245 65
4-5 14:09:00 0.22 1.73 122.602 240 105 105 245 252 65
4-6 14:14:00 0.20 1.57 126.870 240 105 105 250 250 66
14:19:00 130.937
Total 2:00:00 111.192 102.0 102.0
Average 2.07 240.0 102.0
Min 1.57 239.0 100.0
Max 2.58 241.0 105.0
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Run 3 - Method 5
6/13/24
12:10
14:19
∆H:
Stack Temperature, Ts:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 159 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Clinker Cooler Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV 1
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 768.6 755.3 13.3
DI Water 747.9 743.7 4.2
Empty 782.5 780.0 2.5
Silica Gel 848.7 836.1 12.6
2,299.0 2,279.0 20.0
Liquid Final Liquid Initial Liquid Gain
848.7 836.1 12.6
Silica Final Silica Initial Silica Gain
500
750
Impinger Weight Sheet - Run 3
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 160 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Run 1 Run 2 Run 3
Temp ID:CM18 CM18 CM18
Meter ID:CM18 CM18 CM18
Pitot ID:4039 4039 4039
Filter ID:15524 15526 14851
Filter Pre-Weight (grams):0.46178 0.46254 0.46648
Nozzle Diameter (Inches):0.313 0.313 0.313
Meter Calibration Date:6/12/2024 6/12/2024 6/12/2024
Meter Calibration Factor (Y):0.990 0.990 0.990
Meter Orifice Setting (Delta H):1.736 1.736 1.736
Nozzle Kit ID Number and Material:Quartz #14 Quartz #14 Quartz #14
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs 3
LV2
Horizontal
Circular
4
11.00
4.1
7.00
95.033
0.840
6.0
5.5
120
Anderson Box
Mill Off
Ash Grove Cememnt Company
Leamington Cement Plant
Main Kiln Stack
M242413
5/202
5.0
5.0
6
6.00
Glass
EROD
AIR
24
Flange
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 161 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
2.56 in. H2O -0.50 in. H2O
77.4 °F 24.99 in. Hg. abs.
0.712 in. H2O 13.70 %
346.2 °F 10.20 %
121.148 ft3 76.10 %
99.318 dscf 30.600 lb/lb mole
11.794 wscf 29.263 lb/lb mole
98.4 %I --- %
53.671 fps
120.00 in mins. 306,032 acfm
0.313 in inches 149,651 dscfm
25.03 in Hg 167,422 scfm
Calculated Fo: 0.78
Fo Validity: #N/A
1975.1 ml 834.2 grams
2184.6 ml 875.1 grams
209.5 ml 40.9 grams
250.4 0.106
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 5:55:00 0.63 3.22 31.489 323 71 71 244 243 64
1-2 6:00:00 0.61 3.09 37.127 331 72 72 250 244 62
1-3 6:05:00 0.57 2.90 42.650 331 74 74 246 244 60
1-4 6:10:00 0.49 2.49 48.036 334 75 75 245 245 59
1-5 6:15:00 0.45 2.28 53.012 335 75 75 250 250 60
1-6 6:20:00 0.42 2.13 57.758 335 75 75 252 249 60
6:25:00 62.382
2-1 6:28:00 0.62 3.11 62.382 345 76 76 250 253 50
2-2 6:33:00 0.60 3.01 67.961 346 77 77 246 250 51
2-3 6:38:00 0.58 2.91 73.447 346 77 77 250 250 51
2-4 6:43:00 0.51 2.56 78.840 347 78 78 245 240 52
2-5 6:48:00 0.45 2.26 83.884 348 78 78 250 245 52
2-6 6:53:00 0.40 2.00 88.657 350 78 78 250 255 53
6:58:00 93.134
3-1 7:01:00 0.61 3.04 93.134 355 79 79 250 255 55
3-2 7:06:00 0.59 2.94 98.665 355 79 79 250 250 55
3-3 7:11:00 0.55 2.74 104.095 355 79 79 250 245 56
3-4 7:16:00 0.49 2.45 109.345 353 79 79 252 249 56
3-5 7:21:00 0.44 2.20 114.312 353 79 79 251 252 56
3-6 7:26:00 0.43 2.15 118.984 352 79 79 256 252 56
7:31:00 123.645
4-1 7:33:00 0.59 2.94 123.645 354 79 79 254 247 57
4-2 7:38:00 0.54 2.69 129.112 354 79 79 252 249 58
4-3 7:43:00 0.47 2.36 134.280 351 80 80 251 251 58
4-4 7:48:00 0.43 2.15 139.176 352 80 80 252 252 59
4-5 7:53:00 0.40 2.00 143.841 352 80 80 252 251 59
4-6 7:58:00 0.37 1.85 148.299 352 80 80 251 248 59
8:03:00 152.637
Total 2:00:00 121.148 77.4 77.4
Average 2.56 346.2 77.4
Min 1.85 323.0 71.0
Max 3.22 355.0 80.0
Run 1 - Method 5/202
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
5:55
6/12/24
8:03
Start Time:
Meter Volume, Vwstd:
Source Condition:
Nitrogen:
STACK CONDITIONS
Static Pressure
Sqrt ∆P:
End Time:
Carbon Dioxide:
Moisture, Bws:
Silica Difference:
Total Water Gain:
Final Impinger Content:
Meter Temp
Impinger Difference:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
MOISTURE DETERMINATION
Volumetric Flow:
Silica Final Wt.
Barometric Pressure:
Volumetric Flow:
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Silica Initial Wt.
Test Length:
Nozzle Diameter:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 162 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5/202
Weighed/Measured By: Rods 500.1
Balance ID: LV2
750.1
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 815.3 678.7 136.6
DI Water 754.1 691.1 63.0
Empty 615.2 605.3 9.9
Silica Gel 875.1 834.2 40.9
2,184.6 1,975.1 209.5
Liquid Final Liquid Initial Liquid Gain
875.1 834.2 40.9
Silica Final Silica Initial Silica Gain
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
750
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 163 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
2.45 In. H2O -0.50 in. H2O
83.4 °F 24.99 in. Hg. abs.
0.707 In. H2O 13.60 %
380.3 °F 10.40 %
118.156 ft3 76.0 %
95.761 dscf 30.592 lb/lb mole
10.150 wscf 29.385 lb/lb mole
96.6 %I --- %
54.312 fps
120.00 in mins. 309,687 acfm
0.313 in inches 146,964 dscfm
25.03 in Hg 162,542 scfm
Calculated Fo: 0.77
Fo Validity: #N/A
1899.8 ml 854.8 grams
2072.8 ml 897.3 grams
173.0 ml 42.5 grams
215.5 0.096
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 8:20:00 0.62 3.02 53.196 378 81 81 270 252 68
1-2 8:25:00 0.58 2.82 58.715 380 82 82 265 255 64
1-3 8:30:00 0.53 2.58 64.038 380 82 82 265 252 62
1-4 8:35:00 0.49 2.38 69.145 380 82 82 260 250 61
1-5 8:40:00 0.45 2.19 74.046 380 83 83 260 245 59
1-6 8:45:00 0.40 1.98 78.732 380 83 83 260 253 54
8:50:00 83.188
2-1 8:53:00 0.59 2.87 83.188 380 83 83 254 253 55
2-2 8:58:00 0.56 2.73 88.178 380 83 83 252 250 55
2-3 9:03:00 0.54 2.63 93.835 380 83 83 251 250 55
2-4 9:08:00 0.48 2.34 98.990 380 83 83 252 240 56
2-5 9:13:00 0.42 2.05 103.850 380 83 83 252 245 56
2-6 9:18:00 0.39 1.90 108.375 380 83 83 251 255 56
9:23:00 112.766
3-1 9:26:00 0.61 2.97 112.766 381 83 83 252 252 57
3-2 9:31:00 0.59 2.87 118.241 380 83 83 251 250 57
3-3 9:36:00 0.55 2.68 123.619 380 84 83 256 246 57
3-4 9:41:00 0.51 2.49 128.846 380 84 84 254 245 57
3-5 9:46:00 0.45 2.19 133.865 382 84 84 252 250 58
3-6 9:51:00 0.40 1.95 138.553 381 84 84 251 250 58
9:56:00 143.015
4-1 9:59:00 0.61 2.98 143.015 381 85 85 245 251 58
4-2 10:04:00 0.57 2.79 148.505 380 85 85 250 252 59
4-3 10:09:00 0.49 2.40 153.836 380 85 85 250 252 59
4-4 10:14:00 0.44 2.15 158.778 382 85 85 252 245 60
4-5 10:19:00 0.41 2.00 163.447 382 85 85 254 250 60
4-6 10:24:00 0.39 1.91 167.954 381 85 85 255 252 60
10:29:00 171.352
Total 2:00:00 118.156 83.5 83.4
Average 2.45 380.3 83.4
Min 1.90 378.0 81.0
Max 3.02 382.0 85.0
Run 2 - Method 5/202
Carbon Dioxide:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
6/12/24
8:20
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
10:29
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd: Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 164 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5/202
Weighed/Measured By: Rods 500.1
Balance ID: LV2
750.1
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 769.2 628.5 140.7
DI Water 739.3 709.2 30.1
Empty 564.3 562.1 2.2
Silica Gel 897.3 854.8 42.5
2,072.8 1,899.8 173.0
Liquid Final Liquid Initial Liquid Gain
897.3 854.8 42.5
Silica Final Silica Initial Silica Gain
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
250
500
750
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 165 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
2.47 In. H2O -0.50 in. H2O
86.5 °F 24.99 in. Hg. abs.
0.708 In. H2O 13.90 %
380.7 °F 10.90 %
119.860 ft3 75.2 %
96.603 dscf 30.660 lb/lb mole
11.182 wscf 29.347 lb/lb mole
98.2 %I --- %
54.427 fps
120.00 in mins. 310,340 acfm
0.313 in inches 145,929 dscfm
25.03 in Hg 162,820 scfm
Calculated Fo: 0.72
Fo Validity: #N/A
1907.6 ml 721.7 grams
2116.0 ml 750.7 grams
208.4 ml 29.0 grams
237.4 0.104
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 10:55:00 0.60 2.93 71.621 381 85 85 254 249 60
1-2 11:00:00 0.58 2.83 77.081 381 85 85 250 245 60
1-3 11:05:00 0.51 2.49 82.450 381 85 85 250 245 60
1-4 11:10:00 0.45 2.20 87.465 380 85 85 255 250 60
1-5 11:15:00 0.40 1.96 92.167 380 85 85 253 250 61
1-6 11:20:00 0.38 1.86 96.640 380 85 85 250 252 61
11:25:00 100.960
2-1 11:28:00 0.59 2.88 100.960 380 85 85 250 250 61
2-2 11:33:00 0.56 2.74 106.378 380 85 85 250 245 61
2-3 11:38:00 0.54 2.64 111.646 381 86 86 245 252 61
2-4 11:43:00 0.48 2.35 116.826 382 86 86 252 255 62
2-5 11:48:00 0.45 2.20 121.687 380 86 86 255 250 62
2-6 11:53:00 0.40 1.96 126.439 380 86 86 255 250 62
11:58:00 130.880
3-1 12:01:00 0.62 3.04 130.880 381 87 87 252 245 61
3-2 12:06:00 0.61 2.99 136.451 381 87 87 252 250 61
3-3 12:11:00 0.57 2.79 141.966 381 87 87 250 250 60
3-4 12:16:00 0.49 2.40 147.278 382 87 87 250 253 60
3-5 12:21:00 0.45 2.21 152.218 382 88 88 255 250 60
3-6 12:26:00 0.40 1.96 156.982 382 88 88 252 250 59
12:31:00 161.433
4-1 12:34:00 0.60 2.95 161.433 380 88 88 252 255 59
4-2 12:39:00 0.58 2.85 166.926 380 88 88 250 255 59
4-3 12:44:00 0.51 2.51 172.318 380 88 88 245 250 60
4-4 12:49:00 0.48 2.37 177.352 381 88 88 250 252 60
4-5 12:54:00 0.45 2.21 182.275 380 88 88 255 245 61
4-6 12:59:00 0.40 1.97 187.004 380 88 88 250 250 61
13:04:00 191.481
Total 2:00:00 119.860 86.5 86.5
Average 2.47 380.7 86.5
Min 1.86 380.0 85.0
Max 3.04 382.0 88.0
Run 3 - Method 5/202
6/12/24
10:55
13:04
∆H:
Stack Temperature, Ts:
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 166 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5/202
Weighed/Measured By: Rods 500.1
Balance ID: LV2
750.1
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 571.5 418.2 153.3
Empty 783.1 741.7 41.4
DI 761.4 747.7 13.7
Silica Gel 750.7 721.7 29.0
2,116.0 1,907.6 208.4
Liquid Final Liquid Initial Liquid Gain
750.7 721.7 29.0
Silica Final Silica Initial Silica Gain
Impinger Weight Sheet - Run 3
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 167 of 315 ©Mostardi Platt
Project Number M242413 Source Condition:Mill OffClient:Ash Grove Cememnt Company Run No.: 1
Facility:Leamington Cement Plant Date:6/12/2024
Location:Main Kiln Stack Start Time:6:30
Pitot ID: 4039 End Time:6:50Pitot Coefficient:0.840 RM Testers:
Probe Length:6 Port Length:7.00
DP Sqrt. Temp Yaw Velocity DP Sqrt. Temp Yaw Velocity
Port Point (in. H2O) DP (oF)(o) (V) Port Point (in. H2O) DP (oF)(o) (V)
A10.60 0.7746 316.0 #VALUE!C10.61 0.7810 316.0 #VALUE!
A20.52 0.7211 316.0 #VALUE!C20.58 0.7616 316.0 #VALUE!
A30.45 0.6708 317.0 #VALUE!C30.56 0.7483 317.0 #VALUE!
A40.40 0.6325 317.0 #VALUE!C40.50 0.7071 317.0 #VALUE!
A50.37 0.6083 318.0 #VALUE!C50.42 0.6481 317.0 #VALUE!
A60.39 0.6245 318.0 #VALUE!C60.40 0.6325 319.0 #VALUE!
B10.62 0.7874 317.0 #VALUE!D10.60 0.7746 316.0 #VALUE!
B20.60 0.7746 316.0 #VALUE!D20.56 0.7483 316.0 #VALUE!
B30.58 0.7616 317.0 #VALUE!D30.50 0.7071 317.0 #VALUE!
B40.55 0.7416 318.0 #VALUE!D40.46 0.6782 318.0 #VALUE!
B50.47 0.6856 318.0 #VALUE!D50.42 0.6481 318.0 #VALUE!
B60.42 0.6481 318.0 #VALUE!D60.39 0.6245 318.0 #VALUE!
Average Yaw Angle #DIV/0!
Test Parameters
Pbar - Barometric pressure, inches Hg % CO2Pg - Stack Pressure, inches of H2O% O2
Ps - Absolute stack pressure, inches Hg % N2 100.00
ts - Average stack temperature, oF 317.1 Md - dry basis lb/lb mole
Shape of Duct: (C or R)C Ms - wet basis lb/lb mole #VALUE!
Stack Diameter, Feet Average Sqrt DP 0.7038
Bws - Moisture content fraction
Cross Sectional Area of Stack, Ft2 95.03
METHOD 2 VOLUMETRIC FLOW DATA
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 168 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)
7:45 13.70 10.10
7:46 13.70 10.10
7:47 13.60 10.20
7:48 13.60 10.20
Average 13.65 10.15
Min 13.60 10.10
Max 13.70 10.20
Client:
Facility:
Run 1
Project #:
Test Location:
Operating Condition:
Date:
Ash Grove Ceme
Leamington Cem
M242413
Main Kiln Stack
Mill OFF
6/12/24
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 169 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)
10:11 13.50 10.30
10:12 13.50 10.30
10:13 13.40 10.40
10:14 13.40 10.40
10:15 13.40 10.40
Average 13.44 10.36
Min 13.40 10.30
Max 13.50 10.40
Client:
Facility:
Project #:
Ash Grove Ceme
Leamington Cem
M242413
Run 2
Test Location:
Operating Condition:
Date:
Main Kiln Stack
Mill OFF
6/12/24
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 170 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)
11:48 13.80 10.80
11:49 13.80 10.80
11:50 13.70 10.80
11:51 13.70 10.90
11:52 13.70 10.80
Average 13.74 10.82
Min 13.70 10.80
Max 13.80 10.90
Client:
Facility:
Project #:
Run 3
Test Location:
Operating Condition:
Date:
Ash Grove Cement Company
Leamington Cement Plant
M242413
Main Kiln Stack Mill OFF
6/12/24
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 171 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Temp ID:
Meter ID:
Pitot ID:
Filter ID:
Filter Pre-Weight (grams):
Nozzle Diameter (Inches):
Meter Calibration Date:
Meter Calibration Factor (Y):
Meter Orifice Setting (Delta H):
Nozzle Kit ID Number and Material:
Pre Pitot Leak Check 0.0 @ 4.0 "H2O 0.0 @ 3.5 "H2O 0.0 @ 4.1 "H2O
Post Pitot Leak Check 0.0 @ 4.5 "H2O 0.0 @ 4.5 "H2O 0.0 @ 4.4 "H2O
Pre Nozzle Leak Check 0.0000 @ 10 "Hg 0.0000 @ 14 "Hg 0.0000 @ 11 "Hg
Post Nozzle Leak Check 0.0000 @ 14 "Hg 0.0000 @ 17 "Hg 0.0000 @ 14 "Hg
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
0.995
CM56
CM56
4034
CM56
CM56
15550
0.251
6.0
quartz
Quartz #39
Run 1
5/24/2024
0.45447
4034
15553
Run 3
Horizontal
7.00
5/24/2024
0.995
0.45781
6.00
Quartz #39
5.0
1.6691.669
0.251
24
120
Flange
Circular
11
4.1
5.5
95.033
Anderson Box
Mill On
Servomex 1440
LV2
4
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
M222606
5
AIR
Rods
Run 2
CM56
CM56
4034
15551
0.45509
0.251
5/24/2024
0.995
1.669
Quartz #39
Leak Checks
0.840
4
6
5.0
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 172 of 315 ©Mostardi Platt
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.20 3 -0.70 in. H2O
70.5 °F 25.03 in. Hg. abs.
0.723 in. H2O 15.50 %
226.7 °F 11.60 %
83.406 ft3 72.90 %
69.480 dscf 30.944 lb/lb mole
12.001 wscf 29.038 lb/lb mole
101.6 %I --- %
50.449 fps
120.00 in mins.287,657 acfm
0.251 in inches 157,765 dscfm
25.08 in Hg 185,016 scfm
1931.3 ml 821.9 grams
2167.0 ml 841.0 grams
235.7 ml 19.1 grams
254.8 0.147
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 7:30:00 0.61 1.39 84.051 226 70 70 5 255 250 52
1-2 7:35:00 0.57 1.30 87.850 226 70 70 5 253 249 52
1-3 7:40:00 0.50 1.14 91.440 226 70 70 5 252 249 52
1-4 7:45:00 0.48 1.10 94.850 226 70 70 5 252 250 52
1-5 7:50:00 0.45 1.03 98.170 226 70 70 5 251 251 52
1-6 7:55:00 0.40 0.91 101.380 226 70 70 5 251 252 52
8:00:00 104.422
2-1 8:03:00 0.64 1.46 104.422 226 70 70 5 250 251 53
2-2 8:08:00 0.61 1.39 108.290 227 70 70 5 250 250 53
2-3 8:13:00 0.57 1.30 112.120 227 70 70 5 251 250 53
2-4 8:18:00 0.54 1.23 115.650 227 70 70 5 251 249 53
2-5 8:23:00 0.49 1.12 119.170 227 70 70 5 250 248 53
2-6 8:28:00 0.42 0.96 122.540 227 70 70 5 249 249 53
8:33:00 125.641
3-1 8:36:00 0.60 1.37 125.641 227 71 71 5 250 250 53
3-2 8:41:00 0.56 1.28 129.370 227 71 71 5 251 251 53
3-3 8:46:00 0.54 1.23 132.980 227 71 71 5 250 249 53
3-4 8:51:00 0.50 1.14 136.530 227 71 71 5 248 249 53
3-5 8:56:00 0.45 1.03 139.920 227 71 71 5 249 250 54
3-6 9:01:00 0.41 0.94 143.140 227 71 71 5 250 250 54
9:06:00 146.220
4-1 9:09:00 0.65 1.48 146.220 227 71 71 5 250 250 54
4-2 9:14:00 0.63 1.44 150.110 227 71 71 5 250 251 54
4-3 9:19:00 0.57 1.30 153.940 227 71 71 5 251 251 54
4-4 9:24:00 0.50 1.14 157.550 227 71 71 5 252 251 54
4-5 9:29:00 0.47 1.07 160.950 227 71 71 5 251 250 54
4-6 9:34:00 0.44 1.00 164.270 227 71 71 5 250 249 54
9:39:00 167.457
Total 2:00:00 83.406 70.5 70.5
Average 1.20 226.7 70.5 5
Min 0.91 226.0 70.0 5
Max 1.48 227.0 71.0 5
Run 1 - Method 5 Client: Ash Grove Cement Company
Source Condition:
Nitrogen:
STACK CONDITIONS
9:39
Start Time:
Meter Volume, Vwstd:
7:30
6/13/24
Sqrt ∆P:
End Time:
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
Silica Difference:
Total Water Gain:
Final Impinger Content:Silica Final Wt.
Barometric Pressure:
Silica Initial Wt.
Volumetric Flow:
Moisture, Bws:
Static Pressure
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Test Length:
Nozzle Diameter:
Carbon Dioxide:
Volumetric Flow:
Meter Temp
Impinger Difference:
MOISTURE DETERMINATION
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 173 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M222606 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: AIR 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 752.9 603.2 149.7
DI Water 782.8 697.4 85.4
Empty 631.3 630.7 0.6
Silica Gel 841.0 821.9 19.1
2,167.0 1,931.3 235.7
Liquid Final Liquid Initial Liquid Gain
841.0 821.9 19.1
Silica Final Silica Initial Silica Gain
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 174 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.23 In. H2O -0.70 in. H2O
81.5 °F 25.03 in. Hg. abs.
0.732 In. H2O 16.10 %
225.6 °F 11.40 %
86.197 ft3 72.5 %
70.346 dscf 31.032 lb/lb mole
11.992 wscf 29.134 lb/lb mole
101.4 %I --- %
50.952 fps
120.00 in mins.290,530 acfm
0.251 in inches 159,911 dscfm
25.08 in Hg 187,170 scfm
1961.3 ml 813.8 grams
2196.9 ml 832.8 grams
235.6 ml 19.0 grams
254.6 0.146
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 9:45:00 0.65 1.48 76.593 225 81 81 5 255 253 65
1-2 9:50:00 0.61 1.39 80.550 225 81 81 5 254 252 65
1-3 9:55:00 0.58 1.32 84.380 225 81 81 5 252 252 65
1-4 10:00:00 0.55 1.26 88.120 225 81 81 5 252 251 65
1-5 10:05:00 0.47 1.07 91.750 225 81 81 5 251 251 65
1-6 10:10:00 0.45 1.03 95.120 225 81 81 5 250 250 65
10:15:00 98.410
2-1 10:18:00 0.63 1.44 98.410 225 81 81 5 250 250 65
2-2 10:23:00 0.59 1.35 102.302 225 81 81 5 252 252 65
2-3 10:28:00 0.56 1.28 106.100 225 81 81 5 252 252 65
2-4 10:33:00 0.51 1.16 109.740 225 81 81 5 251 251 65
2-5 10:38:00 0.48 1.10 113.250 226 81 81 5 250 251 65
2-6 10:43:00 0.46 1.05 116.640 226 82 82 5 252 251 65
10:48:00 119.970
3-1 10:51:00 0.64 1.46 119.970 226 82 82 5 252 252 66
3-2 10:56:00 0.58 1.32 123.900 226 82 82 5 252 252 66
3-3 11:01:00 0.53 1.21 127.640 226 82 82 5 253 253 66
3-4 11:06:00 0.49 1.12 131.220 226 82 82 5 251 251 66
3-5 11:11:00 0.47 1.07 134.650 226 82 82 5 251 250 66
3-6 11:16:00 0.44 1.00 138.020 226 82 82 5 251 251 66
11:21:00 141.280
4-1 11:24:00 0.63 1.44 141.280 226 82 82 5 250 252 66
4-2 11:29:00 0.58 1.32 145.180 226 82 82 5 250 251 66
4-3 11:34:00 0.56 1.28 148.920 226 82 82 5 253 252 66
4-4 11:39:00 0.52 1.19 152.600 226 82 82 5 252 250 66
4-5 11:44:00 0.47 1.07 156.140 226 82 82 5 253 250 66
4-6 11:49:00 0.45 1.03 159.500 226 82 82 5 252 251 66
11:54:00 162.790
Total 2:00:00 86.197 81.5 81.5
Average 1.23 225.6 81.5 5
Min 1.00 225.0 81.0 5
Max 1.48 226.0 82.0 5
Run 2 - Method 5
Carbon Dioxide:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Silica Initial Wt.
Total Water Gain:Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
6/13/24
9:45
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
11:54
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd:Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 175 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M222606 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: AIR 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 794.5 645.1 149.4
DI Water 799.6 714.2 85.4
Empty 602.8 602.0 0.8
Silica Gel 832.8 813.8 19.0
2,196.9 1,961.3 235.6
Liquid Final Liquid Initial Liquid Gain
832.8 813.8 19.0
Silica Final Silica Initial Silica Gain
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
250
500
750
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 176 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.32 In. H2O -0.70 in. H2O
85.8 °F 25.03 in. Hg. abs.
0.760 In. H2O 15.70 %
224.2 °F 11.60 %
90.332 ft3 72.7 %
73.162 dscf 30.976 lb/lb mole
12.185 wscf 29.123 lb/lb mole
101.1 %I --- %
52.881 fps
120.00 in mins.301,525 acfm
0.251 in inches 166,865 dscfm
25.08 in Hg 194,656 scfm
2016.8 ml 856.6 grams
2253.3 ml 878.8 grams
236.5 ml 22.2 grams
258.7 0.143
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 12:10:00 0.68 1.55 64.358 223 85 85 5 250 252 64
1-2 12:15:00 0.65 1.48 68.440 223 85 85 5 251 252 64
1-3 12:20:00 0.62 1.42 72.430 223 85 85 5 252 253 64
1-4 12:25:00 0.58 1.32 76.330 223 85 85 5 251 252 64
1-5 12:30:00 0.56 1.28 80.100 223 85 85 5 250 251 64
1-6 12:35:00 0.51 1.16 83.800 224 85 85 5 250 251 64
12:40:00 87.330
2-1 12:43:00 0.66 1.51 87.330 224 85 85 5 250 250 64
2-2 12:48:00 0.63 1.44 91.350 224 85 85 5 249 250 65
2-3 12:53:00 0.59 1.35 95.280 224 85 85 5 249 251 65
2-4 12:58:00 0.55 1.26 99.100 224 85 85 5 250 250 65
2-5 13:03:00 0.52 1.19 102.740 224 86 86 5 250 251 65
2-6 13:08:00 0.50 1.14 106.310 224 86 86 5 251 250 65
13:13:00 109.810
3-1 13:16:00 0.65 1.48 109.810 224 86 86 5 252 250 65
3-2 13:21:00 0.62 1.42 113.810 224 86 86 5 250 249 65
3-3 13:26:00 0.58 1.32 117.710 224 86 86 5 251 249 65
3-4 13:31:00 0.55 1.26 121.480 225 86 86 5 250 250 65
3-5 13:36:00 0.51 1.16 125.150 225 86 86 5 249 251 65
3-6 13:41:00 0.49 1.12 128.690 225 86 86 5 249 251 65
13:46:00 132.150
4-1 13:49:00 0.65 1.48 132.150 225 87 87 5 250 251 66
4-2 13:54:00 0.63 1.44 136.150 225 87 87 5 250 250 66
4-3 13:59:00 0.59 1.35 140.100 225 87 87 5 251 251 66
4-4 14:04:00 0.56 1.28 143.900 225 87 87 5 251 252 66
4-5 14:09:00 0.52 1.19 147.610 225 87 87 5 250 251 66
4-6 14:14:00 0.50 1.14 151.180 225 87 87 5 250 250 66
14:19:00 154.690
Total 2:00:00 90.332 85.8 85.8
Average 1.32 224.2 85.8 5
Min 1.12 223.0 85.0 5
Max 1.55 225.0 87.0 5
Run 3 - Method 5
6/13/24
12:10
14:19
∆H:
Stack Temperature, Ts:
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 177 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M222606 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: AIR 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 837.1 687.7 149.4
DI Water 795.3 709.0 86.3
Empty 620.9 620.1 0.8
Silica Gel 878.8 856.6 22.2
2,253.3 2,016.8 236.5
Liquid Final Liquid Initial Liquid Gain
878.8 856.6 22.2
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 178 of 315 ©Mostardi Platt
Project Number Source Condition:Mill On
Client:Run No.: 1
Facility:Date:6/13/2024
Location:Start Time:6:30
Pitot ID: End Time:6:59
Pitot Coefficient:RM Testers:AIR
Probe Length:
M222606
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4034
0.840
6 Port Length:7.00
DP Sqrt. Temp Yaw Angle DP (in. H2O) Velocity DP Sqrt. Temp Yaw Angle DP (in. H2O) Velocity
Port Point (in. H2O) DP (oF)(o) at Null Point Angle (V)Port Point (in. H2O) DP (oF)(o) at Null Point Angle (V)
A10.62 0.7874 224.0 0.00 54.95 C10.63 0.7937 224.0 0.00 55.39
A20.56 0.7483 224.0 0.00 52.22 C20.57 0.7550 225.0 0.00 52.72
A30.52 0.7211 224.0 0.00 50.32 C30.49 0.7000 225.0 0.00 48.89
A40.46 0.6782 225.0 0.00 47.37 C40.45 0.6708 225.0 0.00 46.85
A50.44 0.6633 225.0 0.00 46.32 C50.42 0.6481 225.0 0.00 45.26
A60.41 0.6403 225.0 0.00 44.72 C60.39 0.6245 225.0 0.00 43.61
B10.60 0.7746 225.0 0.00 54.09 D10.64 0.8000 224.0 0.00 55.83
B20.56 0.7483 225.0 0.00 52.26 D20.61 0.7810 225.0 0.00 54.54
B30.54 0.7348 225.0 0.00 51.32 D30.56 0.7483 225.0 0.00 52.26
B40.47 0.6856 225.0 0.00 47.88 D40.48 0.6928 224.0 0.00 48.35
B50.43 0.6557 225.0 0.00 45.79 D50.45 0.6708 224.0 0.00 46.81
B60.42 0.6481 225.0 0.00 45.26 D60.44 0.6633 224.0 0.00 46.29
Average Yaw Angle #DIV/0!o
Method 1 and 2 Cyclonic Flow Check Data
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 179 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Run 1 Run 2 Run 3
Temp ID:CM53 CM53 CM53
Meter ID:CM53 CM53 CM53
Pitot ID:1115 1115 1115
Filter ID:10486 10522 10528
Filter Pre-Weight (grams):0.45494 0.45197 0.45191
Nozzle Diameter (Inches):0.238 0.238 0.238
Meter Calibration Date:5/20/2024 5/20/2024 5/20/2024
Meter Calibration Factor (Y):0.988 0.988 0.988
Meter Orifice Setting (Delta H):1.703 1.703 1.703
Nozzle Kit ID Number and Material:SS SET #21 LV8 SS SET #21 LV8 SS SET #21 LV8
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
Glass
RB
AIR
24
Flange
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
M242413
5
5.0
5.0
12
6.00
0.840
6.0
6.3
120
Anderson Box
Mill Off
3
Servomex 1440
LV-4
Horizontal
Circular
2
2.42
1.8
7.00
4.588
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 180 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Mill Off
2.20 in. H2O -0.50 in. H2O
89.8 °F 24.99 in. Hg. abs.
0.983 in. H2O 7.60 %
157.7 °F 16.50 %
117.202 ft3 75.90 %
93.640 dscf 29.876 lb/lb mole
10.701 wscf 28.658 lb/lb mole
100.3 %I --- %
65.547 fps
120.00 in mins. 18,045 acfm
0.238 in inches 11,563 dscfm
25.03 in Hg 12,884 scfm
Calculated Fo: 0.58
Fo Validity: #N/A
1962.5 ml 845.9 grams
2148.1 ml 887.5 grams
185.6 ml 41.6 grams
227.2 0.103 0.366
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 5:55:00 1.00 2.28 47.135 157 86 86 240 250 67
1-2 6:00:00 1.00 2.28 52.060 157 87 87 243 251 67
1-3 6:05:00 0.99 2.26 57.010 157 87 87 244 251 67
1-4 6:10:00 0.98 2.24 61.930 157 88 88 244 250 66
1-5 6:15:00 0.98 2.24 66.840 158 88 88 245 255 66
1-6 6:20:00 0.96 2.19 71.740 158 89 89 249 255 66
1-7 6:25:00 0.96 2.19 76.600 159 89 89 250 256 66
1-8 6:30:00 0.95 2.17 81.460 159 90 90 250 254 65
1-9 6:35:00 0.93 2.12 86.300 159 90 90 248 252 65
1-10 6:40:00 0.93 2.12 91.090 158 91 91 247 250 65
1-11 6:45:00 0.92 2.10 95.890 158 91 91 250 250 64
1-12 6:50:00 0.91 2.08 100.660 158 92 92 251 251 64
6:55:00 105.428
2-1 6:58:00 1.10 2.51 105.428 158 91 91 255 250 63
2-2 7:03:00 1.10 2.51 110.640 158 91 91 255 249 63
2-3 7:08:00 0.99 2.26 115.860 158 91 91 254 248 63
2-4 7:13:00 0.98 2.24 120.810 158 91 91 252 249 63
2-5 7:18:00 0.98 2.24 125.740 158 91 91 250 252 62
2-6 7:23:00 0.96 2.19 130.670 158 91 91 248 250 62
2-7 7:28:00 0.95 2.17 135.550 157 90 90 249 250 62
2-8 7:33:00 0.95 2.17 140.400 157 90 90 252 255 61
2-9 7:38:00 0.93 2.12 145.250 157 90 90 255 257 61
2-10 7:43:00 0.92 2.10 150.040 157 90 90 256 255 61
2-11 7:48:00 0.92 2.10 154.820 157 90 90 258 254 61
2-12 7:53:00 0.91 2.08 159.590 157 90 90 255 250 60
7:58:00 164.337
Total 2:00:00 117.202 89.8 89.8
Average 2.20 157.7 89.8
Min 2.08 157.0 86.0
Max 2.51 159.0 92.0
Volumetric Flow:
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Silica Initial Wt.
Test Length:
Nozzle Diameter:
MOISTURE DETERMINATION
Volumetric Flow:
Supersaturation Value, Bws:
Silica Final Wt.
Barometric Pressure:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Moisture, Bws:
Silica Difference:
Total Water Gain:
Final Impinger Content:
Meter Temp
Impinger Difference:
Start Time:
Meter Volume, Vwstd:
Source Condition:
Nitrogen:
STACK CONDITIONS
Static Pressure
Sqrt ∆P:
End Time:
Carbon Dioxide:
Run 1 - Method 5
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
5:55
6/12/24
7:58
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 181 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 757.0 632.7 124.3
DI Water 725.6 677.7 47.9
Empty 665.5 652.1 13.4
Silica Gel 887.5 845.9 41.6
2,148.1 1,962.5 185.6
Liquid Final Liquid Initial Liquid Gain
887.5 845.9 41.6
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 182 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Mill Off
2.24 In. H2O -0.50 in. H2O
91.7 °F 24.99 in. Hg. abs.
0.990 In. H2O 6.70 %
163.1 °F 16.90 %
117.983 ft3 76.4 %
93.945 dscf 29.748 lb/lb mole
10.800 wscf 28.537 lb/lb mole
100.2 %I --- %
66.420 fps
120.00 in mins. 18,285 acfm
0.238 in inches 11,609 dscfm
25.03 in Hg 12,943 scfm
Calculated Fo: 0.60
Fo Validity: #N/A
2148.1 ml 887.5 grams
2339.7 ml 925.2 grams
191.6 ml 37.7 grams
229.3 0.103 0.415
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 8:20:00 1.10 2.51 65.215 163 89 89 252 254 54
1-2 8:25:00 1.00 2.28 70.420 163 89 89 251 254 54
1-3 8:30:00 1.00 2.28 75.350 163 90 90 250 251 56
1-4 8:35:00 1.00 2.28 80.310 163 90 90 247 252 57
1-5 8:40:00 0.99 2.26 85.240 163 90 90 250 253 58
1-6 8:45:00 0.97 2.21 90.180 163 91 91 251 253 58
1-7 8:50:00 0.97 2.21 95.110 163 91 91 254 251 59
1-8 8:55:00 0.95 2.17 99.950 164 91 91 253 254 62
1-9 9:00:00 0.95 2.17 104.770 164 92 92 251 251 60
1-10 9:05:00 0.94 2.14 109.620 164 92 92 250 248 60
1-11 9:10:00 0.92 2.10 114.450 164 92 92 252 248 59
1-12 9:15:00 0.92 2.10 119.200 164 92 92 252 249 59
9:20:00 123.974
2-1 9:23:00 1.00 2.28 123.974 164 91 91 251 252 57
2-2 9:28:00 1.10 2.51 128.940 164 92 92 252 252 57
2-3 9:33:00 1.10 2.51 134.150 164 92 92 256 251 58
2-4 9:38:00 1.00 2.28 139.370 163 92 92 256 250 58
2-5 9:43:00 1.00 2.28 144.350 163 93 93 253 250 59
2-6 9:48:00 0.99 2.26 149.280 163 93 93 254 247 59
2-7 9:53:00 0.97 2.21 154.250 162 93 93 251 249 59
2-8 9:58:00 0.97 2.21 159.160 162 93 93 252 251 60
2-9 10:03:00 0.95 2.17 164.140 162 93 93 253 251 61
2-10 10:08:00 0.94 2.14 168.990 162 93 93 256 256 62
2-11 10:13:00 0.90 2.05 173.780 162 93 93 251 255 62
2-12 10:18:00 0.89 2.03 178.470 162 93 93 250 251 62
10:23:00 183.198
Total 2:00:00 117.983 91.7 91.7
Average 2.24 163.1 91.7
Min 2.03 162.0 89.0
Max 2.51 164.0 93.0
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd: Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
6/12/24
8:20
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
10:23
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Run 2 - Method 5
Supersaturation Value, Bws:
Carbon Dioxide:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 183 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 887.4 757.0 130.4
DI Water 777.0 725.6 51.4
Empty 675.3 665.5 9.8
Silica Gel 925.2 887.5 37.7
2,339.7 2,148.1 191.6
Liquid Final Liquid Initial Liquid Gain
925.2 887.5 37.7
Silica Final Silica Initial Silica Gain
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
250
500
750
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 184 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Mill Off
2.22 In. H2O -0.50 in. H2O
108.8 °F 24.99 in. Hg. abs.
0.987 In. H2O 6.70 %
163.6 °F 16.90 %
121.170 ft3 76.4 %
93.581 dscf 29.748 lb/lb mole
12.660 wscf 28.348 lb/lb mole
101.6 %I --- %
66.484 fps
120.00 in mins. 18,303 acfm
0.238 in inches 11,403 dscfm
25.03 in Hg 12,945 scfm
Calculated Fo: 0.60
Fo Validity: #N/A
1911.5 ml 800.0 grams
2055.3 ml 925.0 grams
143.8 ml 125.0 grams
268.8 0.119 0.420
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 10:55:00 1.00 2.28 85.019 164 111 111 244 254 62
1-2 11:00:00 1.10 2.51 90.140 164 111 111 250 256 62
1-3 11:05:00 0.99 2.26 95.530 164 111 111 251 254 62
1-4 11:10:00 0.99 2.26 100.640 164 111 111 251 252 62
1-5 11:15:00 0.97 2.21 105.750 164 111 111 250 250 63
1-6 11:20:00 0.96 2.19 110.800 163 110 110 255 250 63
1-7 11:25:00 0.97 2.21 115.830 163 110 110 250 256 63
1-8 11:30:00 0.96 2.19 120.880 163 110 110 251 254 64
1-9 11:35:00 0.95 2.17 125.910 163 109 109 251 252 64
1-10 11:40:00 0.93 2.12 130.900 163 109 109 250 250 64
1-11 11:45:00 0.91 2.08 135.840 162 109 109 255 250 65
1-12 11:50:00 0.91 2.08 140.760 162 109 109 255 251 65
11:55:00 145.623
2-1 11:58:00 1.10 2.51 145.623 163 108 108 252 251 65
2-2 12:03:00 1.10 2.51 150.970 163 108 108 251 251 66
2-3 12:08:00 1.00 2.28 156.330 163 108 108 252 250 66
2-4 12:13:00 0.98 2.24 161.340 163 108 108 251 250 64
2-5 12:18:00 0.98 2.24 166.510 164 108 108 250 247 64
2-6 12:23:00 0.96 2.19 171.560 164 107 107 252 249 64
2-7 12:28:00 0.96 2.19 176.560 164 107 107 251 251 64
2-8 12:33:00 0.95 2.17 181.560 164 107 107 250 251 63
2-9 12:38:00 0.94 2.14 186.530 164 107 107 247 249 63
2-10 12:43:00 0.94 2.14 191.470 165 107 107 250 251 62
2-11 12:48:00 0.92 2.10 196.410 165 107 107 251 251 62
2-12 12:53:00 0.92 2.10 201.300 165 107 107 252 256 62
12:58:00 206.189
Total 2:00:00 121.170 108.8 108.8
Average 2.22 163.6 108.8
Min 2.08 162.0 107.0
Max 2.51 165.0 111.0
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
Supersaturation Value, Bws:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Run 3 - Method 5
6/12/24
10:55
13:55
∆H:
Stack Temperature, Ts:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 185 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
EMPTY 660.4 517.9 142.5
EMPTY 644.5 643.2 1.3
DI 750.4 750.4 0.0
Silica Gel 925.0 800.0 125.0
2,055.3 1,911.5 143.8
Liquid Final Liquid Initial Liquid Gain
925.0 800.0 125.0
Silica Final Silica Initial Silica Gain
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 186 of 315 ©Mostardi Platt
Date: 6/12/2024 Date: 6/12/2024 Date: 6/12/2024
Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)
8:36 16.50 7.60 10:19 16.80 6.80 11:53 16.90 6.70
8:37 16.40 7.50 10:20 16.80 6.70 11:54 16.90 6.70
8:38 16.50 7.40 10:21 16.90 6.60 11:55 16.90 6.60Average 16.47 7.50 Average 16.83 6.70 Average 16.90 6.67
Min 16.40 7.40 Min 16.80 6.60 Min 16.90 6.60Max16.50 7.60 Max 16.90 6.80 Max 16.90 6.70
Run 1 Run 2 Run 3
M242413Project #:
Client:Ash Grove Cement CompanyFacility:Leamington Cement Plant
Coal Mill StackTest Location:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 187 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Run 1 Run 2 Run 3
Temp ID:CM53 CM53 CM53
Meter ID:CM53 CM53 CM53
Pitot ID:1115 1115 1115
Filter ID:15535 14843 9258
Filter Pre-Weight (grams):0.46251 0.46322 0.45206
Nozzle Diameter (Inches):0.238 0.238 0.238
Meter Calibration Date:5/20/2024 5/20/2024 5/20/2024
Meter Calibration Factor (Y):0.988 0.988 0.988
Meter Orifice Setting (Delta H):1.703 1.703 1.703
Nozzle Kit ID Number and Material:SS SET #21 LV8 SS SET #21 LV8 SS SET #21 LV8
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
Glass
RB
RODS
24
Flange
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
M242413
5
5.0
5.0
12
6.00
0.840
6.0
6.3
120
Anderson Box
Mill ON
4
Servomex 1440
LV-4
Horizontal
Circular
2
2.42
1.8
7.00
4.588
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 188 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
MILL ON
2.26 in. H2O -0.50 in. H2O
98.7 °F 25.04 in. Hg. abs.
0.981 in. H2O 7.60 %
163.3 °F 16.50 %
118.184 ft3 75.90 %
93.118 dscf 29.876 lb/lb mole
9.321 wscf 28.795 lb/lb mole
99.3 %I --- %
65.469 fps
120.00 in mins. 18,023 acfm
0.238 in inches 11,617 dscfm
25.08 in Hg 12,780 scfm
Calculated Fo: 0.58
Fo Validity: #N/A
1823.0 ml 906.5 grams
1986.5 ml 940.9 grams
163.5 ml 34.4 grams
197.9 0.091 0.416
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 7:30:00 1.00 2.35 6.419 162 97 97 247 251 61
1-2 7:35:00 0.99 2.33 11.420 162 97 97 245 252 61
1-3 7:40:00 1.00 2.35 16.400 162 97 97 244 250 61
1-4 7:45:00 0.99 2.33 21.420 162 97 97 245 249 61
1-5 7:50:00 0.98 2.31 26.400 163 97 97 246 253 62
1-6 7:55:00 0.97 2.28 31.360 163 97 97 249 257 62
1-7 8:00:00 0.96 2.26 36.300 163 98 98 250 256 63
1-8 8:05:00 0.96 2.26 41.210 163 98 98 250 255 63
1-9 8:10:00 0.94 2.21 46.130 164 98 98 251 255 63
1-10 8:15:00 0.93 2.19 51.010 164 98 98 251 253 64
1-11 8:20:00 0.92 2.16 55.820 164 98 98 250 250 65
1-12 8:25:00 0.92 2.16 60.630 164 98 98 249 250 65
8:30:00 65.445
2-1 8:33:00 1.10 2.59 65.445 164 99 99 250 249 66
2-2 8:38:00 0.99 2.33 70.700 164 99 99 251 251 66
2-3 8:43:00 0.99 2.33 75.700 164 99 99 251 252 65
2-4 8:48:00 0.97 2.28 80.690 164 99 99 252 251 65
2-5 8:53:00 0.96 2.26 85.640 164 100 100 255 249 65
2-6 8:58:00 0.96 2.26 90.570 164 100 100 256 247 64
2-7 9:03:00 0.94 2.21 95.500 163 100 100 253 250 64
2-8 9:08:00 0.94 2.21 100.380 163 100 100 249 253 64
2-9 9:13:00 0.93 2.19 105.260 163 100 100 248 255 63
2-10 9:18:00 0.92 2.16 110.120 163 100 100 247 252 62
2-11 9:23:00 0.92 2.16 114.950 163 101 101 244 251 62
2-12 9:28:00 0.91 2.14 119.790 163 101 101 242 249 60
9:33:00 124.603
Total 2:00:00 118.184 98.7 98.7
Average 2.26 163.3 98.7
Min 2.14 162.0 97.0
Max 2.59 164.0 101.0
Volumetric Flow:
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Silica Initial Wt.
Test Length:
Nozzle Diameter:
MOISTURE DETERMINATION
Volumetric Flow:
Supersaturation Value, Bws:
Silica Final Wt.
Barometric Pressure:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Moisture, Bws:
Silica Difference:
Total Water Gain:
Final Impinger Content:
Meter Temp
Impinger Difference:
Start Time:
Meter Volume, Vwstd:
Source Condition:
Nitrogen:
STACK CONDITIONS
Static Pressure
Sqrt ∆P:
End Time:
Carbon Dioxide:
Run 1 - Method 5
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
7:30
6/13/24
9:33
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 189 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 468.5 399.7 68.8
Empty 739.0 677.7 61.3
DI Water 779.0 745.6 33.4
Silica Gel 940.9 906.5 34.4
1,986.5 1,823.0 163.5
Liquid Final Liquid Initial Liquid Gain
940.9 906.5 34.4
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 190 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
MILL ON
2.36 In. H2O -0.50 in. H2O
105.1 °F 25.04 in. Hg. abs.
0.982 In. H2O 6.70 %
163.0 °F 16.90 %
121.989 ft3 76.4 %
95.050 dscf 29.748 lb/lb mole
8.897 wscf 28.742 lb/lb mole
100.4 %I --- %
65.635 fps
120.00 in mins. 18,069 acfm
0.238 in inches 11,721 dscfm
25.08 in Hg 12,818 scfm
Calculated Fo: 0.60
Fo Validity: #N/A
2088.1 ml 867.5 grams
2243.4 ml 901.1 grams
155.3 ml 33.6 grams
188.9 0.086 0.413
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 9:45:00 1.10 2.68 31.934 163 104 104 255 250 63
1-2 9:50:00 1.10 2.68 37.340 163 104 104 255 249 63
1-3 9:55:00 0.99 2.42 42.750 163 104 104 254 250 63
1-4 10:00:00 0.98 2.39 47.890 163 104 104 254 251 63
1-5 10:05:00 0.97 2.37 53.020 163 104 104 251 254 64
1-6 10:10:00 0.97 2.37 58.090 162 104 104 249 255 64
1-7 10:15:00 0.96 2.34 63.180 162 105 105 250 254 65
1-8 10:20:00 0.94 2.29 68.250 162 105 105 250 253 65
1-9 10:25:00 0.94 2.29 73.270 162 105 105 248 249 65
1-10 10:30:00 0.92 2.24 78.290 162 105 105 247 248 64
1-11 10:35:00 0.91 2.22 83.150 162 105 105 251 250 64
1-12 10:40:00 0.91 2.22 88.200 162 106 106 253 251 63
10:45:00 93.151
2-1 10:48:00 1.00 2.44 93.151 163 106 106 254 250 61
2-2 10:53:00 0.99 2.42 98.320 163 106 106 253 250 61
2-3 10:58:00 0.99 2.42 103.480 163 106 106 249 248 61
2-4 11:03:00 0.98 2.39 108.630 163 106 106 248 247 60
2-5 11:08:00 0.97 2.37 113.760 163 106 106 250 251 60
2-6 11:13:00 0.97 2.37 118.870 163 106 106 251 253 60
2-7 11:18:00 0.95 2.32 123.970 164 106 106 255 250 59
2-8 11:23:00 0.95 2.32 129.020 164 105 105 255 249 59
2-9 11:28:00 0.94 2.29 134.060 164 105 105 254 250 59
2-10 11:33:00 0.92 2.24 139.070 164 105 105 254 251 58
2-11 11:38:00 0.92 2.24 144.030 164 105 105 251 254 58
2-12 11:43:00 0.91 2.22 149.010 164 105 105 249 255 59
11:48:00 153.923
Total 2:00:00 121.989 105.1 105.1
Average 2.36 163.0 105.1
Min 2.22 162.0 104.0
Max 2.68 164.0 106.0
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd: Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
6/13/24
9:45
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
11:48
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Run 2 - Method 5
Supersaturation Value, Bws:
Carbon Dioxide:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 191 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 801.8 737.0 64.8
DI Water 766.3 705.6 60.7
Empty 675.3 645.5 29.8
Silica Gel 901.1 867.5 33.6
2,243.4 2,088.1 155.3
Liquid Final Liquid Initial Liquid Gain
901.1 867.5 33.6
Silica Final Silica Initial Silica Gain
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
250
500
750
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 192 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
MILL ON
2.34 In. H2O -0.50 in. H2O
99.1 °F 25.04 in. Hg. abs.
0.980 In. H2O 6.70 %
164.0 °F 16.90 %
120.245 ft3 76.4 %
94.693 dscf 29.748 lb/lb mole
8.845 wscf 28.744 lb/lb mole
100.4 %I --- %
65.493 fps
120.00 in mins. 18,030 acfm
0.238 in inches 11,679 dscfm
25.08 in Hg 12,770 scfm
Calculated Fo: 0.60
Fo Validity: #N/A
2105.4 ml 871.1 grams
2261.3 ml 903.0 grams
155.9 ml 31.9 grams
187.8 0.085 0.423
Velocity Orifice Actual Stack Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F oF oF oF
1-1 12:10:00 1.00 2.44 55.062 164 100 100 245 251 65
1-2 12:15:00 1.00 2.44 60.170 165 100 100 244 252 65
1-3 12:20:00 0.98 2.39 65.290 165 100 100 243 251 65
1-4 12:25:00 0.98 2.39 70.360 165 100 100 244 249 65
1-5 12:30:00 0.97 2.37 75.430 165 100 100 250 247 65
1-6 12:35:00 0.97 2.37 80.470 165 100 100 251 245 66
1-7 12:40:00 0.95 2.32 85.510 165 100 100 258 248 66
1-8 12:45:00 0.95 2.32 90.500 165 99 99 256 256 66
1-9 12:50:00 0.93 2.27 95.480 165 99 99 252 258 67
1-10 12:55:00 0.93 2.27 100.410 164 99 99 249 254 67
1-11 13:00:00 0.91 2.22 105.340 164 99 99 247 251 66
1-12 13:05:00 0.91 2.22 110.220 164 99 99 249 250 66
13:10:00 115.105
2-1 13:13:00 1.10 2.68 115.105 164 99 99 252 252 65
2-2 13:18:00 1.00 2.44 120.450 164 99 99 252 256 65
2-3 13:23:00 0.98 2.39 125.570 164 98 98 251 254 65
2-4 13:28:00 0.97 2.37 130.620 164 98 98 248 258 64
2-5 13:33:00 0.97 2.37 135.650 163 98 98 249 253 64
2-6 13:38:00 0.96 2.34 140.680 163 98 98 250 250 64
2-7 13:43:00 0.94 2.29 145.690 163 98 98 255 249 64
2-8 13:48:00 0.94 2.29 150.640 163 99 99 256 248 64
2-9 13:53:00 0.93 2.27 155.610 163 99 99 254 248 64
2-10 13:58:00 0.93 2.27 160.540 163 99 99 250 246 63
2-11 14:03:00 0.92 2.24 165.480 163 99 99 250 249 63
2-12 14:08:00 0.92 2.24 170.390 162 99 99 248 252 62
14:13:00 175.307
Total 2:00:00 120.245 99.1 99.1
Average 2.34 164.0 99.1
Min 2.22 162.0 98.0
Max 2.68 165.0 100.0
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
Supersaturation Value, Bws:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Run 3 - Method 5
6/13/24
12:10
13:55
∆H:
Stack Temperature, Ts:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 193 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/13/2024
Facility: Leamington Cement Plant
Test Location: Coal Mill Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/13/2024 250.0
Test Method: 5
Weighed/Measured By: RICHS 500.0
Balance ID: LV-4
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
DI Water 823.8 758.8 65.0
DI Water 770.8 711.3 59.5
Empty 666.7 635.3 31.4
Silica Gel 903.0 871.1 31.9
2,261.3 2,105.4 155.9
Liquid Final Liquid Initial Liquid Gain
903.0 871.1 31.9
Silica Final Silica Initial Silica Gain
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 194 of 315 ©Mostardi Platt
Date: 6/13/2024 Date: 6/13/2024 Date: 6/13/2024
Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)
8:36 16.50 7.60 10:19 16.80 6.80 11:53 16.90 6.70
8:37 16.40 7.50 10:20 16.80 6.70 11:54 16.90 6.70
8:38 16.50 7.40 10:21 16.90 6.60 11:55 16.90 6.60Average 16.47 7.50 Average 16.83 6.70 Average 16.90 6.67
Min 16.40 7.40 Min 16.80 6.60 Min 16.90 6.60Max16.50 7.60 Max 16.90 6.80 Max 16.90 6.70
Run 1 Run 2 Run 3
M242413Project #:
Client:Ash Grove Cement CompanyFacility:Leamington Cement Plant
Coal Mill StackTest Location:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 195 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
p,
Temp ID:
Meter ID:
Pitot ID:
Filter ID:
Filter Pre-Weight (grams):
Nozzle Diameter (Inches):
Meter Calibration Date:
Meter Calibration Factor (Y):
Meter Orifice Setting (Delta H):
Nozzle Kit ID Number and Material:
Pre Pitot Leak Check 0.0 @ 3.5 "H2O 0.0 @ 5.5 "H2O 0.0 @ 4.0 "H2O
Post Pitot Leak Check 0.0 @ 4.5 "H2O 0.0 @ 3.0 "H2O 0.0 @ 3.0 "H2O
Pre Nozzle Leak Check 0.0000 @ 10 "Hg 0.0000 @ 15 "Hg 0.0000 @ 13 "Hg
Post Nozzle Leak Check 0.0000 @ 14 "Hg 0.0000 @ 16 "Hg 0.0000 @ 12 "Hg
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
Anderson Box
Mill On
Servomex 1440
LV2
3
Leak Checks
0.840
4
6
7.5
24
180
Flange
Circular
11
4.1
5.5
95.033
6.00
Quartz
7.5
1.6691.669
0.275
Horizontal
7.00
5/24/2024
Quartz
0.995
0.462540.46178
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
M242413
23
AIR
RODS
Run 2 Run 3
0.46648
4034
14851
CM56
CM56
Quartz
0.275
5/24/2024
Run 1
4034
5/24/2024
1552615524
1.669
0.275
6.0
quartz
0.995 0.995
CM56
CM56
4034
CM56
CM56
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 196 of 315 ©Mostardi Platt
Client: Ash Grove Cememnt Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
MILL ON
1.67 in. H2O -0.70 in. H2O
72.4 °F 24.98 in. Hg. abs.
0.702 in. H2O 14.00 %
344.1 °F 12.00 %
137.489 ft3 74.00 %
114.060 dscf 30.720 lb/lb mole
19.433 wscf 28.868 lb/lb mole
102.7 %I --- %
53.262 fps
180.00 in mins.303,699 acfm
0.275 in inches 142,243 dscfm
25.03 in Hg 166,478 scfm
2796.9 ml 831.4 grams
3189.0 ml 851.9 grams
392.1 ml 20.5 grams
412.6 0.146
Velocity Orifice Actual Stack Pump Probe Filter Impinger XAD TRAP
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF °F
1-1 5:55:00 0.61 2.06 81.571 340 71 71 5 251 250 50 50
1-2 6:02:30 0.57 1.92 88.010 340 71 71 5 250 250 50 50
1-3 6:10:00 0.54 1.82 94.230 341 71 71 5 250 249 50 50
1-4 6:17:30 0.48 1.62 100.290 341 71 71 5 249 249 50 50
1-5 6:25:00 0.42 1.42 106.000 341 71 71 5 248 250 50 50
1-6 6:32:30 0.39 1.31 111.340 341 71 71 5 249 251 50 50
6:40:00 116.480
2-1 6:43:00 0.59 1.99 16.480 342 72 72 5 250 250 50 50
2-2 6:50:30 0.52 1.75 22.730 342 72 72 5 251 251 50 50
2-3 6:58:00 0.48 1.62 28.590 342 72 72 5 250 250 51 50
2-4 7:05:30 0.45 1.52 34.230 343 72 72 5 249 249 51 50
2-5 7:13:00 0.41 1.38 39.680 343 72 72 5 250 249 51 51
2-6 7:20:30 0.38 1.28 44.880 343 72 72 5 251 250 51 51
7:28:00 49.890
3-1 7:31:00 0.60 2.02 49.890 345 72 72 5 252 253 51 52
3-2 7:38:30 0.58 1.95 56.180 345 72 72 5 250 251 51 52
3-3 7:46:00 0.53 1.79 62.360 345 73 73 5 250 250 52 52
3-4 7:53:30 0.49 1.65 68.280 345 73 73 5 251 251 52 52
3-5 8:01:00 0.46 1.55 73.980 346 73 73 5 249 250 52 53
3-6 8:08:30 0.41 1.38 79.490 346 73 73 5 250 249 52 53
8:16:00 84.690
4-1 8:19:00 0.61 2.06 84.690 347 73 73 5 253 251 53 53
4-2 8:26:30 0.58 1.95 91.040 347 74 74 5 253 250 53 53
4-3 8:34:00 0.54 1.82 97.240 347 74 74 5 251 252 54 54
4-4 8:41:30 0.47 1.58 103.210 349 74 74 5 250 250 54 54
4-5 8:49:00 0.41 1.38 108.790 349 74 74 5 251 250 54 54
4-6 8:56:30 0.39 1.31 113.990 349 74 74 5 250 251 54 54
9:04:00 119.060
MOISTURE DETERMINATION
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Volumetric Flow:
Meter Temp
Impinger Difference:
Static Pressure
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Test Length:
Nozzle Diameter:
Carbon Dioxide:
Silica Difference:
Total Water Gain:
Final Impinger Content: Silica Final Wt.
Barometric Pressure:
Silica Initial Wt.
Volumetric Flow:
Moisture, Bws:
6/12/24
Sqrt ∆P:
End Time:
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
Run 1 - Method 23
Source Condition:
Nitrogen:
STACK CONDITIONS
9:04
Start Time:
Meter Volume, Vwstd:
5:55
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 197 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 948.0 679.1 268.9
DI Water 845.2 735.6 109.6
DI Water 725.7 719.0 6.7
Empty 670.1 663.2 6.9
Silica Gel 851.9 831.4 20.5
3,189.0 2,796.9 392.1
Liquid Final Liquid Initial Liquid Gain
851.9 831.4 20.5
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 198 of 315 ©Mostardi Platt
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.23 In. H2O -0.70 in. H2O
84.8 °F 24.79 in. Hg. abs.
0.662 In. H2O %
382.8 °F %
129.017 ft3 #VALUE! %
103.668 dscf #VALUE! lb/lb mole
17.663 wscf #VALUE! lb/lb mole
#VALUE! %I #VALUE! %
#VALUE! fps
180.00 in mins.#VALUE! acfm
0.275 in inches #VALUE! dscfm
24.84 in Hg #VALUE! scfm
2764.7 ml 825.1 grams
3118.9 ml 845.9 grams
354.2 ml 20.8 grams
375.0 0.146
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 9:20:00 0.52 1.46 21.513 381 84 84 5 255 254 53
1-2 9:27:30 0.49 1.37 27.370 381 84 84 5 253 254 53
1-3 9:35:00 0.45 1.26 33.060 381 84 84 5 253 252 53
1-4 9:42:30 0.39 1.09 38.500 381 84 84 5 254 251 53
1-5 9:50:00 0.36 1.01 43.580 381 84 84 5 255 250 53
1-6 9:57:30 0.35 0.98 48.450 382 84 84 5 253 251 53
10:05:00 53.250
2-1 10:08:00 0.55 1.54 53.250 382 84 84 5 252 250 53
2-2 10:15:30 0.49 1.37 59.270 382 84 84 5 253 252 53
2-3 10:23:00 0.46 1.29 64.950 382 85 85 5 252 251 53
2-4 10:30:30 0.41 1.15 70.470 382 85 85 5 252 250 53
2-5 10:38:00 0.39 1.09 75.670 382 85 85 5 253 251 53
2-6 10:45:30 0.37 1.04 80.750 383 85 85 5 250 251 54
10:53:00 85.690
3-1 10:56:00 0.54 1.51 85.690 383 85 85 5 252 250 54
3-2 11:03:30 0.51 1.43 91.670 383 85 85 5 252 250 54
3-3 11:11:00 0.47 1.32 97.470 383 85 85 5 253 251 54
3-4 11:18:30 0.43 1.20 103.040 383 85 85 5 254 252 54
3-5 11:26:00 0.38 1.06 108.370 383 85 85 5 251 251 54
3-6 11:33:30 0.36 1.01 113.380 383 85 85 5 251 250 54
11:41:00 118.250
4-1 11:44:00 0.52 1.46 18.250 383 85 85 5 250 250 55
4-2 11:51:30 0.49 1.37 24.110 385 85 85 5 253 249 55
4-3 11:59:00 0.45 1.26 29.800 385 85 85 5 252 250 56
4-4 12:06:30 0.42 1.18 35.240 385 86 86 5 251 252 56
4-5 12:14:00 0.39 1.09 40.510 385 86 86 5 250 251 56
4-6 12:21:30 0.37 1.04 45.590 385 86 86 5 250 250 56
12:29:00 50.530
Total 3:00:00 129.017 84.8 84.8
Average 1.23 382.8 84.8 5
Min 0.98 381.0 84.0 5
Max 1.54 385.0 86.0 5
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd:Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
6/12/24
9:20
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
12:29
Silica Initial Wt.
Total Water Gain:Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
Carbon Dioxide:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Run 2 - Method 23
Client: Ash Grove Cement Company
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 199 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 794.0 565.6 228.4
DI Water 875.4 764.5 110.9
DI Water 729.1 722.2 6.9
Empty 720.4 712.4 8.0
Silica Gel 845.9 825.1 20.8
3,118.9 2,764.7 354.2
Liquid Final Liquid Initial Liquid Gain
845.9 825.1 20.8
Silica Final Silica Initial Silica Gain
250
500
750
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 200 of 315 ©Mostardi Platt
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.26 In. H2O -0.70 in. H2O
89.5 °F 24.79 in. Hg. abs.
0.669 In. H2O %
385.4 °F %
131.305 ft3 #VALUE! %
104.610 dscf #VALUE! lb/lb mole
17.691 wscf #VALUE! lb/lb mole
#VALUE! %I #VALUE! %
#VALUE! fps
180.00 in mins.#VALUE! acfm
0.275 in inches #VALUE! dscfm
24.84 in Hg #VALUE! scfm
2632.4 ml 804.5 grams
2986.1 ml 826.4 grams
353.7 ml 21.9 grams
375.6 0.145
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 12:45:00 0.54 1.51 52.355 386 89 89 5 253 252 63
1-2 12:52:30 0.50 1.40 58.360 386 89 89 5 253 252 63
1-3 13:00:00 0.48 1.34 64.140 386 89 89 5 252 253 63
1-4 13:07:30 0.45 1.26 69.800 386 89 89 5 252 252 63
1-5 13:15:00 0.39 1.09 75.280 386 89 89 5 252 251 63
1-6 13:22:30 0.37 1.04 80.380 386 89 89 5 250 251 63
13:30:00 85.350
2-1 13:33:00 0.52 1.46 85.350 386 89 89 5 250 251 63
2-2 13:40:30 0.49 1.37 91.250 386 89 89 5 251 251 63
2-3 13:48:00 0.47 1.32 96.970 386 89 89 5 251 252 63
2-4 13:55:30 0.44 1.23 102.570 386 89 89 5 250 252 63
2-5 14:03:00 0.41 1.15 107.990 385 89 89 5 252 251 63
2-6 14:10:30 0.38 1.06 113.220 385 89 89 5 251 250 63
14:18:00 118.260
3-1 14:21:00 0.52 1.46 118.260 385 90 90 5 251 251 64
3-2 14:28:30 0.50 1.40 124.170 385 90 90 5 251 252 64
3-3 14:36:00 0.47 1.32 129.960 385 90 90 5 252 252 64
3-4 14:43:30 0.43 1.20 135.580 385 90 90 5 252 250 64
3-5 14:51:00 0.40 1.12 140.950 385 90 90 5 251 250 64
3-6 14:58:30 0.37 1.04 146.130 385 90 90 5 250 252 64
15:06:00 151.110
4-1 15:09:00 0.51 1.43 151.110 385 90 90 5 252 251 64
4-2 15:16:30 0.49 1.37 156.960 385 90 90 5 252 251 64
4-3 15:24:00 0.46 1.29 162.700 385 90 90 5 251 250 64
4-4 15:31:30 0.41 1.15 168.250 385 90 90 5 251 250 64
4-5 15:39:00 0.39 1.09 173.500 385 90 90 5 251 251 64
4-6 15:46:30 0.38 1.06 178.610 385 90 90 5 252 251 64
15:54:00 183.660
Total 3:00:00 131.305 89.5 89.5
Average 1.26 385.4 89.5 5
Min 1.04 385.0 89.0 5
Max 1.51 386.0 90.0 5
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
Stack Temperature, Ts:
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Run 3 - Method 23
Client: Ash Grove Cement Company 6/12/24
12:45
15:54
∆H:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 201 of 315 ©Mostardi Platt
Client:Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 719.9 487.3 232.6
DI Water 848.3 741.1 107.2
DI Water 791.4 785.0 6.4
Empty 626.5 619.0 7.5
Silica Gel 826.4 804.5 21.9
2,986.1 2,632.4 353.7
Liquid Final Liquid Initial Liquid Gain
826.4 804.5 21.9
Silica Final Silica Initial Silica Gain
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 202 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
p,
Temp ID:
Meter ID:
Pitot ID:
Filter ID:
Filter Pre-Weight (grams):
Nozzle Diameter (Inches):
Meter Calibration Date:
Meter Calibration Factor (Y):
Meter Orifice Setting (Delta H):
Nozzle Kit ID Number and Material:
Pre Pitot Leak Check 0.0 @ 3.5 "H2O 0.0 @ 5.5 "H2O 0.0 @ 4.0 "H2O
Post Pitot Leak Check 0.0 @ 4.5 "H2O 0.0 @ 3.0 "H2O 0.0 @ 3.0 "H2O
Pre Nozzle Leak Check 0.0000 @ 10 "Hg 0.0000 @ 15 "Hg 0.0000 @ 13 "Hg
Post Nozzle Leak Check 0.0000 @ 14 "Hg 0.0000 @ 16 "Hg 0.0000 @ 12 "Hg
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Diameter (Feet):
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
Anderson Box
Mill Off
Servomex 1440
LV2
3
Leak Checks
0.840
4
6
7.5
24
180
Flange
Circular
11
4.1
5.5
95.033
6.00
Quartz
Run 2
7.5
1.6691.669
0.275
Horizontal
7.00
5/24/2024
Quartz
0.995
0.462540.46178
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
M242413
23
AIR
RODS
Run 3
0.46648
4034
14851
CM56
CM56
Quartz
0.275
5/24/2024
Run 1
4034
5/24/2024
1552615524
1.669
0.275
6.0
quartz
0.995 0.995
CM56
CM56
4034
CM56
CM56
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 203 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
1.67 in. H2O -0.70 in. H2O
72.4 °F 24.98 in. Hg. abs.
0.702 in. H2O 13.70 %
344.1 °F 10.20 %
137.489 ft3 76.10 %
114.060 dscf 30.600 lb/lb mole
19.433 wscf 28.766 lb/lb mole
102.5 %I --- %
53.357 fps
180.00 in mins.304,240 acfm
0.275 in inches 142,496 dscfm
25.03 in Hg 166,775 scfm
2796.9 ml 831.4 grams
3189.0 ml 851.9 grams
392.1 ml 20.5 grams
412.6 0.146
Velocity Orifice Actual Stack Pump Probe Filter Impinger XAD TRAP
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF °F
1-1 5:55:00 0.61 2.06 81.571 340 71 71 5 251 250 50 50
1-2 6:02:30 0.57 1.92 88.010 340 71 71 5 250 250 50 50
1-3 6:10:00 0.54 1.82 94.230 341 71 71 5 250 249 50 50
1-4 6:17:30 0.48 1.62 100.290 341 71 71 5 249 249 50 50
1-5 6:25:00 0.42 1.42 106.000 341 71 71 5 248 250 50 50
1-6 6:32:30 0.39 1.31 111.340 341 71 71 5 249 251 50 50
6:40:00 116.480
2-1 6:43:00 0.59 1.99 16.480 342 72 72 5 250 250 50 50
2-2 6:50:30 0.52 1.75 22.730 342 72 72 5 251 251 50 50
2-3 6:58:00 0.48 1.62 28.590 342 72 72 5 250 250 51 50
2-4 7:05:30 0.45 1.52 34.230 343 72 72 5 249 249 51 50
2-5 7:13:00 0.41 1.38 39.680 343 72 72 5 250 249 51 51
2-6 7:20:30 0.38 1.28 44.880 343 72 72 5 251 250 51 51
7:28:00 49.890
3-1 7:31:00 0.60 2.02 49.890 345 72 72 5 252 253 51 52
3-2 7:38:30 0.58 1.95 56.180 345 72 72 5 250 251 51 52
3-3 7:46:00 0.53 1.79 62.360 345 73 73 5 250 250 52 52
3-4 7:53:30 0.49 1.65 68.280 345 73 73 5 251 251 52 52
3-5 8:01:00 0.46 1.55 73.980 346 73 73 5 249 250 52 53
3-6 8:08:30 0.41 1.38 79.490 346 73 73 5 250 249 52 53
8:16:00 84.690
4-1 8:19:00 0.61 2.06 84.690 347 73 73 5 253 251 53 53
4-2 8:26:30 0.58 1.95 91.040 347 74 74 5 253 250 53 53
4-3 8:34:00 0.54 1.82 97.240 347 74 74 5 251 252 54 54
4-4 8:41:30 0.47 1.58 103.210 349 74 74 5 250 250 54 54
4-5 8:49:00 0.41 1.38 108.790 349 74 74 5 251 250 54 54
4-6 8:56:30 0.39 1.31 113.990 349 74 74 5 250 251 54 54
9:04:00 119.060
MOISTURE DETERMINATION
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
Volumetric Flow:
Meter Temp
Impinger Difference:
Static Pressure
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Test Length:
Nozzle Diameter:
Carbon Dioxide:
Silica Difference:
Total Water Gain:
Final Impinger Content: Silica Final Wt.
Barometric Pressure:
Silica Initial Wt.
Volumetric Flow:
Moisture, Bws:
6/12/24
Sqrt ∆P:
End Time:
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
Run 1 - Method 23
Source Condition:
Nitrogen:
STACK CONDITIONS
9:04
Start Time:
Meter Volume, Vwstd:
5:55
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 204 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 948.0 679.1 268.9
DI Water 845.2 735.6 109.6
DI Water 725.7 719.0 6.7
Empty 670.1 663.2 6.9
Silica Gel 851.9 831.4 20.5
3,189.0 2,796.9 392.1
Liquid Final Liquid Initial Liquid Gain
851.9 831.4 20.5
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 205 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
1.23 In. H2O -0.70 in. H2O
84.8 °F 24.79 in. Hg. abs.
0.662 In. H2O 13.60 %
382.8 °F 10.40 %
129.017 ft3 76.0 %
103.668 dscf 30.592 lb/lb mole
17.663 wscf 28.759 lb/lb mole
101.6 %I --- %
51.664 fps
180.00 in mins.294,586 acfm
0.275 in inches 130,650 dscfm
24.84 in Hg 152,910 scfm
2764.7 ml 825.1 grams
3118.9 ml 845.9 grams
354.2 ml 20.8 grams
375.0 0.146
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 9:20:00 0.52 1.46 21.513 381 84 84 5 255 254 53
1-2 9:27:30 0.49 1.37 27.370 381 84 84 5 253 254 53
1-3 9:35:00 0.45 1.26 33.060 381 84 84 5 253 252 53
1-4 9:42:30 0.39 1.09 38.500 381 84 84 5 254 251 53
1-5 9:50:00 0.36 1.01 43.580 381 84 84 5 255 250 53
1-6 9:57:30 0.35 0.98 48.450 382 84 84 5 253 251 53
10:05:00 53.250
2-1 10:08:00 0.55 1.54 53.250 382 84 84 5 252 250 53
2-2 10:15:30 0.49 1.37 59.270 382 84 84 5 253 252 53
2-3 10:23:00 0.46 1.29 64.950 382 85 85 5 252 251 53
2-4 10:30:30 0.41 1.15 70.470 382 85 85 5 252 250 53
2-5 10:38:00 0.39 1.09 75.670 382 85 85 5 253 251 53
2-6 10:45:30 0.37 1.04 80.750 383 85 85 5 250 251 54
10:53:00 85.690
3-1 10:56:00 0.54 1.51 85.690 383 85 85 5 252 250 54
3-2 11:03:30 0.51 1.43 91.670 383 85 85 5 252 250 54
3-3 11:11:00 0.47 1.32 97.470 383 85 85 5 253 251 54
3-4 11:18:30 0.43 1.20 103.040 383 85 85 5 254 252 54
3-5 11:26:00 0.38 1.06 108.370 383 85 85 5 251 251 54
3-6 11:33:30 0.36 1.01 113.380 383 85 85 5 251 250 54
11:41:00 118.250
4-1 11:44:00 0.52 1.46 18.250 383 85 85 5 250 250 55
4-2 11:51:30 0.49 1.37 24.110 385 85 85 5 253 249 55
4-3 11:59:00 0.45 1.26 29.800 385 85 85 5 252 250 56
4-4 12:06:30 0.42 1.18 35.240 385 86 86 5 251 252 56
4-5 12:14:00 0.39 1.09 40.510 385 86 86 5 250 251 56
4-6 12:21:30 0.37 1.04 45.590 385 86 86 5 250 250 56
12:29:00 50.530
Total 3:00:00 129.017 84.8 84.8
Average 1.23 382.8 84.8 5
Min 0.98 381.0 84.0 5
Max 1.54 385.0 86.0 5
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd:Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
6/12/24
9:20
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
12:29
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
Carbon Dioxide:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Run 2 - Method 23
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 206 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 794.0 565.6 228.4
DI Water 875.4 764.5 110.9
DI Water 729.1 722.2 6.9
Empty 720.4 712.4 8.0
Silica Gel 845.9 825.1 20.8
3,118.9 2,764.7 354.2
Liquid Final Liquid Initial Liquid Gain
845.9 825.1 20.8
Silica Final Silica Initial Silica Gain
250
500
750
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 207 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill Off
1.26 In. H2O -0.70 in. H2O
89.5 °F 24.79 in. Hg. abs.
0.669 In. H2O 13.90 %
385.4 °F 10.90 %
131.305 ft3 75.2 %
104.610 dscf 30.660 lb/lb mole
17.691 wscf 28.829 lb/lb mole
101.6 %I --- %
52.231 fps
180.00 in mins.297,821 acfm
0.275 in inches 131,811 dscfm
24.84 in Hg 154,101 scfm
2632.4 ml 804.5 grams
2986.1 ml 826.4 grams
353.7 ml 21.9 grams
375.6 0.145
Velocity Orifice Actual Stack Pump Probe Filter Impinger
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg oF oF oF
1-1 12:45:00 0.54 1.51 52.355 386 89 89 5 253 252 63
1-2 12:52:30 0.50 1.40 58.360 386 89 89 5 253 252 63
1-3 13:00:00 0.48 1.34 64.140 386 89 89 5 252 253 63
1-4 13:07:30 0.45 1.26 69.800 386 89 89 5 252 252 63
1-5 13:15:00 0.39 1.09 75.280 386 89 89 5 252 251 63
1-6 13:22:30 0.37 1.04 80.380 386 89 89 5 250 251 63
13:30:00 85.350
2-1 13:33:00 0.52 1.46 85.350 386 89 89 5 250 251 63
2-2 13:40:30 0.49 1.37 91.250 386 89 89 5 251 251 63
2-3 13:48:00 0.47 1.32 96.970 386 89 89 5 251 252 63
2-4 13:55:30 0.44 1.23 102.570 386 89 89 5 250 252 63
2-5 14:03:00 0.41 1.15 107.990 385 89 89 5 252 251 63
2-6 14:10:30 0.38 1.06 113.220 385 89 89 5 251 250 63
14:18:00 118.260
3-1 14:21:00 0.52 1.46 118.260 385 90 90 5 251 251 64
3-2 14:28:30 0.50 1.40 124.170 385 90 90 5 251 252 64
3-3 14:36:00 0.47 1.32 129.960 385 90 90 5 252 252 64
3-4 14:43:30 0.43 1.20 135.580 385 90 90 5 252 250 64
3-5 14:51:00 0.40 1.12 140.950 385 90 90 5 251 250 64
3-6 14:58:30 0.37 1.04 146.130 385 90 90 5 250 252 64
15:06:00 151.110
4-1 15:09:00 0.51 1.43 151.110 385 90 90 5 252 251 64
4-2 15:16:30 0.49 1.37 156.960 385 90 90 5 252 251 64
4-3 15:24:00 0.46 1.29 162.700 385 90 90 5 251 250 64
4-4 15:31:30 0.41 1.15 168.250 385 90 90 5 251 250 64
4-5 15:39:00 0.39 1.09 173.500 385 90 90 5 251 251 64
4-6 15:46:30 0.38 1.06 178.610 385 90 90 5 252 251 64
15:54:00 183.660
Total 3:00:00 131.305 89.5 89.5
Average 1.26 385.4 89.5 5
Min 1.04 385.0 89.0 5
Max 1.51 386.0 90.0 5
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
Stack Temperature, Ts:
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Run 3 - Method 23
6/12/24
12:45
15:54
∆H:
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 208 of 315 ©Mostardi Platt
Client: Ash Grove Cement Company 6/12/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/12/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 719.9 487.3 232.6
DI Water 848.3 741.1 107.2
DI Water 791.4 785.0 6.4
Empty 626.5 619.0 7.5
Silica Gel 826.4 804.5 21.9
2,986.1 2,632.4 353.7
Liquid Final Liquid Initial Liquid Gain
826.4 804.5 21.9
Silica Final Silica Initial Silica Gain
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 209 of 315 ©Mostardi Platt
Project Number M242413 Source Condition:Mill Off
Client:Ash Grove Cement Company Run No.: 1
Facility:Leamington Cement Plant Date:6/12/2024
Location:Main Kiln Stack Start Time:5:15
Pitot ID: 4034 End Time:5:35
Pitot Coefficient:0.840 RM Testers:AIR
Probe Length:6 Port Length:7.00
DP Sqrt. Temp Yaw Angle DP (in. H2O) Velocity DP Sqrt. Temp Yaw Angle DP (in. H2O) Velocity
Port Point (in. H2O) DP (oF)(o) at Null Point Angle (V) Port Point (in. H2O) DP (oF)(o) at Null Point Angle (V)
A10.61 0.7810 233.0 2.0 0.00 55.08 C10.61 0.7810 232.0 4.0 0.00 55.04
A20.60 0.7746 233.0 5.0 0.00 54.63 C20.58 0.7616 232.0 2.0 0.00 53.67
A30.58 0.7616 232.0 7.0 0.00 53.67 C30.56 0.7483 231.0 6.0 0.00 52.70
A40.55 0.7416 232.0 4.0 0.00 52.26 C40.52 0.7211 231.0 4.0 0.00 50.78
A50.51 0.7141 232.0 1.0 0.00 50.33 C50.50 0.7071 231.0 3.0 0.00 49.80
A60.49 0.7000 232.0 8.0 0.00 49.33 C60.49 0.7000 231.0 7.0 0.00 49.30
B10.60 0.7746 232.0 5.0 0.00 54.59 D10.60 0.7746 231.0 1.0 0.00 54.55
B20.59 0.7681 232.0 3.0 0.00 54.13 D20.59 0.7681 230.0 5.0 0.00 54.05
B30.57 0.7550 232.0 9.0 0.00 53.21 D30.55 0.7416 230.0 7.0 0.00 52.19
B40.54 0.7348 231.0 5.0 0.00 51.75 D40.51 0.7141 230.0 3.0 0.00 50.26
B50.51 0.7141 231.0 1.0 0.00 50.29 D50.50 0.7071 230.0 8.0 0.00 49.76
B60.50 0.7071 231.0 3.0 0.00 49.80 D60.48 0.6928 230.0 4.0 0.00 48.75
Average Yaw Angle 4.5o
Method 1 and 2 Cyclonic Flow Check Data
AET-014 ISO Template V26.7 5/7/24Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 210 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)THC ppmvw
7:30 5.80 17.40 3.20
7:31 5.80 17.40 3.20
7:32 5.80 17.40 3.20
7:33 5.80 17.40 3.10
7:34 5.80 17.40 3.10
7:35 5.80 17.40 3.10
7:36 5.80 17.40 3.10
7:37 5.90 17.40 3.10
7:38 5.90 17.40 3.10
7:39 5.90 17.40 3.10
7:40 6.00 17.40 3.10
7:41 6.00 17.30 3.10
7:42 6.00 17.30 3.10
7:43 6.00 17.30 3.20
7:44 6.10 17.20 3.20
7:45 6.00 17.30 3.20
7:46 6.00 17.30 3.20
7:47 6.00 17.30 3.10
7:48 6.00 17.30 3.20
7:49 6.00 17.30 3.10
7:50 6.00 17.40 3.10
7:51 5.70 17.40 3.10
7:52 5.80 17.30 3.10
7:53 5.80 17.40 3.10
7:54 5.90 17.40 3.10
7:55 5.90 17.40 3.10
7:56 5.90 17.40 2.90
7:57 5.90 17.30 2.90
7:58 5.90 17.30 2.90
7:59 5.90 17.40 2.90
8:00 5.80 17.40 2.90
8:01 5.80 17.40 3.00
8:02 5.90 17.40 2.90
8:03 5.90 17.40 2.90
8:04 5.90 17.40 2.90
8:05 5.90 17.30 3.00
8:06 5.90 17.30 3.00
8:07 5.90 17.40 2.90
8:08 5.90 17.40 2.90
8:09 6.00 17.40 2.90
8:10 6.00 17.40 3.00
8:11 6.00 17.40 3.00
8:12 6.00 17.50 2.90
8:13 5.90 17.50 2.90
8:14 5.90 17.20 17.40
8:15 5.90 17.20 6.10
8:16 5.90 17.40 3.10
8:17 5.90 17.40 3.00
8:18 5.80 17.30 3.00
8:19 5.80 17.30 3.00
8:20 5.80 17.30 3.00
8:21 5.90 17.20 3.00
8:22 5.90 17.20 3.00
8:23 5.90 17.20 3.00
8:24 5.90 17.10 3.00
8:25 5.90 17.10 3.00
8:26 5.80 17.10 3.10
8:27 5.80 17.20 3.00
8:28 5.70 17.10 3.00
8:29 5.80 17.10 3.10
Average 5.89 17.33 3.30
Min 5.70 17.10 2.90
Max 6.10 17.50 17.40
M242413
Coal Mill
Mill On
6/13/24
Client:
Facility:
Run 1
Project #:
Test Location:
Operating Condition:
Date:
Ash Grove Cement Company
Leamington Plant
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 211 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)THC ppmvw
9:45 5.90 17.00 3.60
9:46 5.90 17.00 3.60
9:47 5.90 16.90 3.70
9:48 5.90 16.90 3.70
9:49 6.00 17.00 3.60
9:50 6.00 17.00 3.60
9:51 6.00 17.00 3.60
9:52 6.00 17.00 3.60
9:53 6.10 16.90 3.60
9:54 6.10 16.90 3.60
9:55 6.20 16.90 3.60
9:56 6.20 16.90 3.60
9:57 6.20 16.90 3.70
9:58 6.10 16.90 3.70
9:59 6.20 16.90 3.60
10:00 6.20 16.90 3.60
10:01 6.10 16.90 3.60
10:02 6.20 16.80 3.70
10:03 6.20 16.80 3.70
10:04 6.10 16.80 3.70
10:05 6.10 16.80 3.70
10:06 6.00 16.80 3.70
10:07 6.00 16.70 3.70
10:08 6.00 16.70 3.70
10:09 6.10 16.70 3.70
10:10 6.10 16.70 3.70
10:11 6.10 16.80 3.80
10:12 6.00 16.80 3.70
10:13 5.90 16.80 3.60
10:14 5.90 16.80 3.60
10:15 5.90 16.80 3.60
10:16 5.90 16.80 3.80
10:17 6.00 16.70 3.80
10:18 6.00 16.80 3.80
10:19 6.10 16.80 3.70
10:20 6.10 16.80 3.70
10:21 6.00 16.80 3.70
10:22 6.10 16.80 3.70
10:23 6.10 16.80 3.70
10:24 6.10 16.90 3.70
10:25 6.20 16.80 3.70
10:26 6.20 16.80 3.70
10:27 6.10 16.80 3.70
10:28 6.10 16.80 3.70
10:29 6.20 16.80 3.70
10:30 6.20 16.90 3.70
10:31 6.10 16.80 3.70
10:32 6.10 16.80 3.80
10:33 6.00 16.80 3.70
10:34 6.00 16.90 3.60
10:35 6.00 16.90 3.60
10:36 6.00 16.80 3.60
10:37 6.10 16.80 3.60
10:38 6.10 16.80 3.70
10:39 6.20 16.70 3.80
10:40 6.20 16.80 3.70
10:41 6.10 16.80 3.70
10:42 6.20 16.80 3.70
10:43 6.20 16.70 3.80
10:44 6.10 16.70 3.80
Average 6.07 16.83 3.70
Min 5.90 16.70 3.60
Max 6.20 17.00 3.80
Client:
Facility:
Project #:
Run 2
Test Location:
Operating Condition:
Date:
Ash Grove Cement Company
Leamington Plant
M242413
Coal Mill
Mill On
6/13/24
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 212 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)THC ppmvw
12:10 6.10 16.80 4.20
12:11 6.10 16.80 4.20
12:12 6.10 17.10 3.90
12:13 6.20 17.00 4.00
12:14 6.20 17.10 4.00
12:15 6.20 16.80 4.10
12:16 6.10 16.80 4.10
12:17 6.20 16.70 4.10
12:18 6.20 16.70 4.20
12:19 6.30 16.70 4.10
12:20 6.20 16.80 4.10
12:21 6.20 16.70 4.10
12:22 6.20 16.80 4.10
12:23 6.10 16.70 4.10
12:24 6.10 16.70 4.10
12:25 6.00 16.70 4.20
12:26 6.00 16.70 4.20
12:27 6.00 16.80 4.20
12:28 6.00 16.80 4.10
12:29 6.00 16.80 4.10
12:30 6.10 16.70 4.10
12:31 6.10 16.70 4.10
12:32 6.10 16.70 4.20
12:33 6.10 16.60 4.20
12:34 6.20 16.70 4.10
12:35 6.20 16.80 4.00
12:36 6.20 16.80 4.00
12:37 6.20 16.80 4.00
12:38 6.20 16.70 4.10
12:39 6.20 16.70 4.10
12:40 6.10 16.80 4.00
12:41 6.20 16.80 4.00
12:42 6.10 16.90 4.00
12:43 6.20 16.80 4.00
12:44 6.20 16.70 4.10
12:45 6.20 16.80 4.00
12:46 6.20 16.70 4.00
12:47 6.20 16.70 4.10
12:48 6.30 16.70 4.10
12:49 6.30 16.70 4.10
12:50 6.10 16.70 4.10
12:51 6.10 16.80 4.00
12:52 6.10 16.80 4.00
12:53 6.10 16.80 4.00
12:54 6.10 16.70 4.10
12:55 6.10 16.70 4.10
12:56 6.20 16.70 4.00
12:57 6.20 16.70 4.10
12:58 6.20 16.70 4.10
12:59 6.20 16.60 4.10
13:00 6.10 16.70 4.10
13:01 6.20 16.70 4.10
13:02 6.20 16.70 4.10
13:03 6.00 16.80 4.10
13:04 6.00 16.70 4.20
13:05 6.10 16.70 4.20
13:06 6.20 16.70 4.30
13:07 6.20 16.70 4.30
13:08 6.10 16.70 4.40
13:09 6.20 16.70 4.50
Average 6.15 16.75 4.10
Min 6.00 16.60 3.90
Max 6.30 17.10 4.50
Client:
Facility:
Project #:
Run 3
Test Location:
Operating Condition:
Date:
Ash Grove Cement Company
Leamington Plant
M242413
Coal Mill
Mill On
6/13/24
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Test No. Date Start Time End Time
Vm (standard
L)ng detected ppb ug/dscm ug/wscm
lb/MM tons
of clinker
1A 48.921 43.9 0.108 0.897 0.816 0.331
1B 47.310 38.4 0.097 0.812 0.738 0.300
41.2 0.102 0.855 0.777 0.316
2A 48.647 43.0 0.106 0.884 0.808 0.337
2B 49.850 33.3 0.080 0.668 0.611 0.255
38.2 0.093 0.776 0.709 0.296
3A 48.349 48.3 0.120 0.999 0.914 0.378
3B 46.726 39.4 0.101 0.843 0.772 0.319
43.9 0.110 0.921 0.843 0.348
41.05 0.10 0.85 0.78 0.320
Method 30B (Sorbent Trap) Mercury Test Results Summary
Ash Grove Cement Company
Leamington Plant
6/12/2024 7:30 8:30
Coal Mill Stack
Average
6/12/2024 9:45 10:45
Average
6/12/2024 12:10 13:10
Average
Overall Average
FT-008 Hg Template V5.0 10/31/17
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Project #:Location:
Client:Condition:
Facility:Data Taken By:
Analyzer ID:
Date:6/12/2024 1A Trap ID:OLC189974 1B Trap ID:OL701370
Start Time:7:30 Hg (ng):43.9 Hg (ng):38.4
End Time:8:30 Meter Temperature (oF):87.00 Meter Temperature (oF):88.00
25.080 Meter ID:MM22A Meter ID:MM2B
0.091 Meter Calibration (Y):1.007 Meter Calibration (Y):0.976
CO2 % (dry):5.90 Initial Volume (liters):0 Initial Volume (liters):0
O2 % (dry):17.00 Final Volume (liters):60.042 Final Volume (liters):60.018
770,520 Meter Volume (Standard liters):48.921 Meter Volume (Standard liters):47.310
Tons of Clinker Produced:118.4 Hg (ppb):0.108 Hg (ppb):0.097
Hg (ug/dscm):0.897 Hg (ug/dscm):0.812
Hg (ug/wscm):0.816 Hg (ug/wscm):0.738
Hg (lb/hr):3.92E-05 Hg (lb/hr):3.55E-05
Hg (lb/MM ton):0.331 Hg (lb/MM ton):0.300
Spike Concentration:Y
Spike Concentration:100
Date:6/12/2024 2A Trap ID:OL607250 2B Trap ID:OL701470
Start Time:9:45 Hg (ng):43.0 Hg (ng):33.3
End Time:10:45 Meter Temperature (oF):90.00 Meter Temperature (oF):60.01
25.080 Meter ID:MM22A Meter ID:MM2B
0.086 Meter Calibration (Y):1.007 Meter Calibration (Y):0.976
CO2 % (dry):6.10 Initial Volume (liters):0 Initial Volume (liters):0
O2 % (dry):15.90 Final Volume (liters):60.033 Final Volume (liters):60.011
770,760 Meter Volume (Standard liters):48.647 Meter Volume (Standard liters):49.850
Tons of Clinker Produced:115.3 Hg (ppb):0.106 Hg (ppb):0.080
Hg (ug/dscm):0.884 Hg (ug/dscm):0.668
Hg (ug/wscm):0.808 Hg (ug/wscm):0.611
Hg (lb/hr):3.89E-05 Hg (lb/hr):2.94E-05
Hg (lb/MM ton):0.337 Hg (lb/MM ton):0.255
Spiked Trap Run:Y
Spike Concentration:100
Date:6/12/2024 3A Trap ID:OL667965 3B Trap ID:OL701305
Start Time:12:10 Hg (ng):48.3 Hg (ng):39.4
End Time:13:10 Meter Temperature (oF):94.00 Meter Temperature (oF):95.00
25.080 Meter ID:MM22A Meter ID:MM2B
0.085 Meter Calibration (Y):1.007 Meter Calibration (Y):0.976
CO2 % (dry):6.20 Initial Volume (liters):0 Initial Volume (liters):0
O2 % (dry):16.90 Final Volume (liters):60.099 Final Volume (liters):60.035
767,160 Meter Volume (Standard liters):48.349 Meter Volume (Standard liters):46.726
Tons of Clinker Produced:115.9 Hg (ppb):0.120 Hg (ppb):0.101
Hg (ug/dscm):0.999 Hg (ug/dscm):0.843
Hg (ug/wscm):0.914 Hg (ug/wscm):0.772
Hg (lb/hr):4.38E-05 Hg (lb/hr):3.70E-05
Hg (lb/MM ton):0.378 Hg (lb/MM ton):0.319
Spiked Trap Run:Y
Spike Concentration:100
1455
Coal Mill Stack
Mill On
MLIPLeamington Plant
3A Trap Data
Run 2 Source Data 2A Trap Data
Run 3
3B Trap Data
2B Trap Data
METHOD 30B TEST RESULTS
Water Vapor in Flue Gas (Bws):
1A Trap DataRun 1 Source Data
Run 2
1B Trap Data
Ash Grove Cement Company
M242413
Run 1
Flowrate (SCFH):
Pressure, Barometric(Hg"):
Flowrate (SCFH):
Pressure, Barometric(Hg"):
Water Vapor in Flue Gas (Bws):
Flowrate (SCFH):
Pressure, Barometric(Hg"):
Water Vapor in Flue Gas (Bws):
Run 3 Source Data
FT-008 Hg Template V5.0 10/31/17
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Appendix G - Field Data Sheets
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Appendix H - Calibration Data
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CN&F-002 Cal Procedures M5 & flow Rev. 2.2 1/1/2021
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.
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ATD-090 Dry Gas Meter Calibration Rev. 1.2 1/1/2021
Dry Gas Meter/Control Module Calibration Diagram
Standard Dry Gas Meter
Dry Gas Meter
Stack Temperature Calibrator
Air-Tight
Pump
Orifice Incline Gauge
Temperature Sensors
Temperature Sensors
Air Inlet
Temperature Display
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Meter Box Calibration
Dry Gas Meter No.CM18 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. Fo Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 50.294 73.866 79 79 79
Initial 45.244 68.814 79 79 79
Difference 1 0.20 5.050 5.052 79 79 79 79 18 0.996 1.562
Final 55.314 78.947 80 80 80
Initial 50.294 73.866 79 79 79
Difference 2 0.50 5.020 5.081 80 80 80 80 12 0.984 1.758
Final 60.354 84.035 80 81 81
Initial 55.314 78.947 80 80 80
Difference 3 0.70 5.040 5.089 80 81 81 81 10 0.987 1.695
Final 65.367 89.072 80 81 81
Initial 60.354 84.035 80 81 81
Difference 4 0.90 5.013 5.037 80 81 81 81 9 0.992 1.783
Final 70.379 94.136 81 82 82
Initial 65.367 89.072 80 81 81
Difference 5 1.20 5.012 5.064 81 82 82 82 8 0.986 1.881
Final 45.244 68.814 79 79 79
Initial 40.201 63.791 79 79 79
Difference 6 2.00 5.043 5.023 79 79 79 79 6 0.996 1.740
Average 0.990 1.736
Run Number
Dry Gas Meter Calibration Data
28.09
Erod
May 21, 2024
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Temperature ID :Name : Erod
Ambient Temperature, oF :Date : May 21, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Stack Temperature Sensor Calibration
CL940A
526
100770
79.1
Test Thermometer
Temperature (oF)Reference Source Temperature (o F)
Temperature Calibrator
February 1, 2025
Model # :
597
1199
Temperature Difference %
0.2
0.3
0.3
0.1
Serial # :Expiration Date:
Certification Date: February 1, 2024
-1
248
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Meter Box Calibration
Dry Gas Meter No.CM18 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. F o Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 97.444 13.934 85 87 87
Initial 92.045 8.473 85 86 87
Difference 1 0.20 5.399 5.461 85 87 87 87 18 0.989 1.379
Final 92.045 8.473 85 86 86
Initial 86.534 2.895 85 86 86
Difference 2 0.50 5.511 5.578 85 86 86 86 12 7 0.986 1.501
Final 86.534 102.895 85 87 87
Initial 81.004 97.347 85 87 87
Difference 3 0.70 5.530 5.548 85 87 87 87 10 13 0.996 1.481
Final 81.004 97.347 85 85 85
Initial 75.519 91.838 85 85 85
Difference 4 0.90 5.485 5.509 85 85 85 85 9 7 0.991 1.547
Final 75.519 91.838 85 85 85
Initial 70.038 86.356 85 85 85
Difference 5 1.20 5.481 5.482 85 85 85 85 8 3 0.994 1.611
Final 70.038 86.356 85 85 85
Initial 64.889 81.246 84 84 84
Difference 6 2.00 5.149 5.110 85 85 85 85 6 3 1.000 1.717
Average 0.992 1.539
Run Number
Dry Gas Meter Calibration Data
28.05
AIR
July 2, 2024
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Temperature ID :Name :AIR
Ambient Temperature, o F :Date :July 2, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Serial # :Expiration Date:
Certification Date:February 1, 2024
-3
246
595
1197
Temperature Difference %
0.7
0.6
0.5
0.2
Stack Temperature Sensor Calibration
CL940A
526
100770
90.7
Test Thermometer
Temperature (o F)Reference Source Temperature (o F)
Temperature Calibrator
February 1, 2025
Model # :
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Meter Box Calibration
Dry Gas Meter No.CM53 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. Fo Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 40.341 97.289 68 69 69
Initial 35.320 92.201 68 69 69
Difference 1 0.20 5.021 5.088 68 69 69 69 18 15 0.986 1.582
Final 45.368 102.378 69 70 70
Initial 40.341 97.289 68 69 69
Difference 2 0.50 5.027 5.089 69 70 70 70 12 0 0.986 1.708
Final 50.371 107.402 70 71 71
Initial 45.368 102.378 69 70 70
Difference 3 0.70 5.003 5.024 70 71 71 71 10 0 0.993 1.679
Final 55.529 112.623 70 72 72
Initial 50.371 107.402 70 71 71
Difference 4 0.90 5.158 5.221 70 72 72 72 9 5 0.986 1.676
Final 60.534 117.716 70 72 72
Initial 55.529 112.623 70 72 72
Difference 5 1.20 5.005 5.093 70 72 72 72 8 0 0.981 1.839
Final 65.585 122.779 70 73 73
Initial 60.534 117.716 70 73 73
Difference 6 2.00 5.051 5.063 70 73 73 73 6 5 0.995 1.737
Average 0.988 1.703
Run Number
Dry Gas Meter Calibration Data
28.19
FCT
March 22, 2024
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Temperature ID :Name : FCT
Ambient Temperature, oF :Date : March 22, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Serial # :Expiration Date:
Certification Date: February 1, 2024
1
252
601
1205
Temperature Difference %
0.2
0.3
0.1
0.3
Stack Temperature Sensor Calibration
CL940A
526
100770
68.9
Test Thermometer
Temperature (oF)Reference Source Temperature (oF)
Temperature Calibrator
February 1, 2025
Model # :
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Meter Box Calibration
Dry Gas Meter No.CM53 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. Fo Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 18.338 5.544 91 90 90
Initial 13.330 0.488 91 89 89
Difference 1 0.20 5.008 5.056 91 90 90 90 18 5 0.985 1.648
Final 23.407 10.636 91 91 91
Initial 18.338 5.544 91 90 90
Difference 2 0.50 5.069 5.092 91 91 91 91 11 55 0.991 1.743
Final 28.436 15.682 92 92 92
Initial 23.407 10.636 91 91 91
Difference 3 0.70 5.029 5.046 92 92 92 92 10 0 0.992 1.746
Final 33.467 20.749 93 92 92
Initial 28.436 15.682 92 92 92
Difference 4 0.90 5.031 5.067 93 92 92 92 8 55 0.987 1.788
Final 38.540 25.851 92 93 93
Initial 33.467 20.749 92 93 93
Difference 5 1.20 5.073 5.102 92 93 93 93 7 55 0.990 1.842
Final 43.574 30.924 92 92 92
Initial 38.540 25.851 92 93 93
Difference 6 2.00 5.034 5.073 92 93 93 93 6 0 0.985 1.792
Average 0.988 1.760
Run Number
Dry Gas Meter Calibration Data
28.00
JSC
June 24, 2024
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Temperature ID :Name : JSC
Ambient Temperature, oF :Date : June 24, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Stack Temperature Sensor Calibration
CL940A
526
100770
93.9
Test Thermometer
Temperature (oF)Reference Source Temperature (o F)
Temperature Calibrator
February 1, 2025
Model # :
600
1204
Temperature Difference %
0.0
0.0
0.0
0.2
Serial # :Expiration Date:
Certification Date: February 1, 2024
0
250
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Meter Box Calibration
Dry Gas Meter No.CM56 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. Fo Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 22.164 12.052 59 60 60
Initial 17.159 7.046 59 58 58
Difference 1 0.20 5.005 5.006 59 59 59 59 18 0 0.997 1.528
Final 27.164 17.065 60 61 61
Initial 22.164 12.052 59 60 60
Difference 2 0.50 5.000 5.013 60 61 61 61 12 0 0.995 1.700
Final 32.203 22.123 60 61 61
Initial 27.164 17.065 60 61 61
Difference 3 0.70 5.039 5.058 60 61 61 61 10 0 0.994 1.628
Final 37.207 27.142 60 63 63
Initial 32.203 22.123 60 61 61
Difference 4 0.90 5.004 5.019 60 62 62 62 9 5 0.996 1.748
Final 42.382 32.367 60 62 62
Initial 37.207 27.142 60 63 63
Difference 5 1.20 5.175 5.225 60 63 63 63 8 0 0.989 1.689
Final 17.159 7.046 59 58 58
Initial 12.124 2.046 56 58 58
Difference 6 2.00 5.035 5.000 58 58 58 58 6 5 1.000 1.718
Average 0.995 1.669
Run Number
Dry Gas Meter Calibration Data
28.14
ER
March 4, 2024
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Temperature ID :Name :ER
Ambient Temperature, oF :Date : March 4, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Serial # :Expiration Date:
Certification Date: February 1, 2024
0
250
600
1204
Temperature Difference %
0.0
0.0
0.0
0.2
Stack Temperature Sensor Calibration
CL940A
526
100770
60
Test Thermometer
Temperature (oF)Reference Source Temperature (o F)
Temperature Calibrator
February 1, 2025
Model # :
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Meter Box Calibration
Dry Gas Meter No.CM56 Date:
Standard Meter No.18654530 Calibrated By:
Standard Meter (Y)0.99730 Barometric Pressure:
Orifice Standard Meter Dry Gas Meter Standard Meter Dry Gas Meter Dry Gas Meter Dry Gas Meter
Setting in H 2O Gas Volume Gas Volume Temp. Fo Inlet Temp. Fo Outlet Temp. Fo Avg. Temp. Fo Time Time
Chg (H)vr vd tr tdi tdo td Min Sec Y Chg (H)
Final 326.609 521.775 90 88 88
Initial 321.595 516.715 89 87 87
Difference 1 0.20 5.014 5.060 90 88 88 88 18 50 0.984 1.777
Final 331.643 526.805 91 90 90
Initial 326.609 521.775 90 88 88
Difference 2 0.50 5.034 5.030 91 89 89 89 12 20 0.994 1.892
Final 336.679 531.853 91 91 91
Initial 331.643 526.805 91 90 90
Difference 3 0.70 5.036 5.048 91 91 91 91 10 30 0.992 1.916
Final 341.782 536.875 91 91 91
Initial 336.679 531.853 91 91 91
Difference 4 0.90 5.103 5.022 91 91 91 91 9 30 1.011 1.962
Final 346.822 541.905 92 92 92
Initial 341.782 536.875 91 91 91
Difference 5 1.20 5.040 5.030 92 92 92 92 8 20 0.996 2.066
Final 351.880 546.925 92 93 93
Initial 346.822 541.905 91 92 92
Difference 6 2.00 5.058 5.020 92 93 93 93 6 20 1.001 1.971
Average 0.996 1.931
Run Number
Dry Gas Meter Calibration Data
28.05
DSN1
July 26, 2024
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 270 of 315 ©Mostardi Platt
Temperature ID :Name : DSN1
Ambient Temperature, oF :Date : July 26, 2024
Primary Standards Directly Traceable National Institute of Standards and Technology (NIST)
0
250
600
1200
(Ref. Temp., oF + 460) - (Test Therm. Temp., oF + 460)* 100 <= 1.5 %
Ref. Temp., oF + 460
Stack Temperature Sensor Calibration
CL940A
526
100770
86.8
Test Thermometer
Temperature (oF)Reference Source Temperature (oF)
Temperature Calibrator
February 1, 2025
Model # :
598
1203
Temperature Difference %
0.4
0.3
0.2
0.2
Serial # :Expiration Date:
Certification Date: February 1, 2024
-2
248
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 271 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (circle one) M5 Probe Length: 5 ft.
γ
Pitot tube assembly level? X yes no
Pitot tube openings damaged? yes (explain below) X no
a1 =1 o (≤10o)a2 =1 o (≤10o)z = A sin γ =0.016 (in.); (≤0.125 in.)
b1 =1 o (≤5o)b2 =1 o (≤5o)w = A sin θ =0.01632 (in.); (≤0.03125 in.)
γ1 θ =1 o A =0.935 (in.)PA =0.468 (in.), PB =0.468 (in.), Dt =0.375 (in.)
Calibration required? yes X no

4039 10/6/2023 IMB
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 272 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (circle one) M5 Probe Length: 5 ft.
γ
Pitot tube assembly level? X yes no
Pitot tube openings damaged? yes (explain below) X no
a1 =1 o (≤10o)a2 =1 o (≤10o)z = A sin γ =0.016 (in.); (≤0.125 in.)
b1 =1 o (≤5o)b2 =1 o (≤5o)w = A sin θ =0.01632 (in.); (≤0.03125 in.)
γ1 θ =1 o A =0.935 (in.)PA =0.468 (in.), PB =0.468 (in.), Dt =0.375 (in.)
Calibration required? yes X no

4039 7/26/2024 DV
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 273 of 315 ©Mostardi Platt
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (mark one) M2 M5 M17 Probe Length:6 ft.
X
Pitot tube assembly level?X yes no
Pitot tube openings damaged?yes (explain below)X no
a1 =3 o (≤10o)a2 =3 o (≤10o)z = A sin γ =0.016 (in.); (≤0.125 in.)
b1 =0 o (≤5o)b2 =1 o (≤5o)w = A sin θ =0.00819 (in.); (≤0.03125 in.)
γ =1 ο θ =0.5 o A =0.938 (in.)PA =0.469 (in.), PB =0.469 (in.), Dt =0.375 (in.)
Calibration required?yes x no
4034 11/13/2023 PJC1/BRD1
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 274 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (mark one) M2 M5 M17 Probe Length: 6 ft.
X
Pitot tube assembly level?X yes no
Pitot tube openings damaged?yes (explain below)X no
a1 =3 o (≤10o)a2 =3 o (≤10o)z = A sin γ =0.016 (in.); (≤0.125 in.)
b1 =0 o (≤5o)b2 =1 o (≤5o)w = A sin θ =0.00819 (in.); (≤0.03125 in.)
γ1 θ =0.5 o A =0.938 (in.)PA =0.469 (in.), PB =0.469 (in.), Dt =0.375 (in.)
Calibration required? yes x no
4034 7/26/2024 DV
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 275 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (circle one) M2 M5 M17 Probe Length:7 ft.
X
Pitot tube assembly level?x yes no
Pitot tube openings damaged?yes (explain below)x no
a1 =1 o (≤10o)a2 =1.5 o (≤10o)z = A sin γ =0.025 (in.); (≤0.125 in.)
b1 =1 o (≤5o)b2 =3 o (≤5o)w = A sin θ =0.00000 (in.); (≤0.03125 in.)
γ =1.5 o θ =0 o A =0.955 (in.)PA =0.478 (in.), PB =0.478 (in.), Dt =0.375 (in.)
Calibration required?yes X no
1115 12/29/2023 AGR
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 276 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (circle one) M2 M5 M17 Probe Length: 7 ft.
X
γ
Pitot tube assembly level?x yes no
Pitot tube openings damaged? yes (explain below)x no
a1 =1 o (≤10o)a2 =1.5 o (≤10o)z = A sin γ =0.025 (in.); (≤0.125 in.)
b1 =1 o (≤5o)b2 =3 o (≤5o)w = A sin θ =0.00000 (in.); (≤0.03125 in.)
γ1.5 θ =0 o A =0.955 (in.)PA =0.478 (in.), PB =0.478 (in.), Dt =0.375 (in.)
Calibration required? yes X no

1115 7/26/2024 DV
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 277 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (mark one) M2 M5 M17 Probe Length:4 ft.
X
Pitot tube assembly level?X yes no
Pitot tube openings damaged?yes (explain below)X no
a1 =3 o (≤10o)a2 =0 o (≤10o)z = A sin γ =0.024 (in.); (≤0.125 in.)
b1 =3.5 o (≤5o)b2 =0 o (≤5o)w = A sin θ =0.02421 (in.); (≤0.03125 in.)
γ =1.5 o θ =1.5 o A =0.925 (in.)PA =0.463 (in.), PB =0.463 (in.), Dt =0.375 (in.)
Calibration required?yes no
569 7/18/2023 JAM
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 278 of 315 ©Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No:Date:Inspectors Name:
Type of Probe: (mark one) M2 M5 M17 Probe Length: 4 ft.
X
Pitot tube assembly level?X yes no
Pitot tube openings damaged?yes (explain below)X no
a1 =3 o (≤10o)a2 =0 o (≤10o)z = A sin γ =0.024 (in.); (≤0.125 in.)
b1 =3.5 o (≤5o)b2 =0 o (≤5o)w = A sin θ =0.02421 (in.); (≤0.03125 in.)
γ1.5 θ =1.5 o A =0.925 (in.)PA =0.463 (in.), PB =0.463 (in.), Dt =0.375 (in.)
Calibration required? yes no
569 7/26/2024 DV
PIS-001 S Type Pitot Tube Inspection Form Rev. 1.0 2/17/2020
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 279 of 315 ©Mostardi Platt
Nozzle Calibration
Date:2/27/2015 Nozzle ID No.:269
Analyst:SC Material/Type: Quartz
0.311 1

0.311 2
0.312 3
0.311 4
Valid Data
Average
0.311
CAT-01 Rev. 0.0 9/13/2013
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 280 of 315 ©Mostardi Platt
Nozzle Calibration
Date:Nozzle ID No.:320
Analyst:Material/Type: Quartz
0.313 1
0.313 2
0.313 3
0.314 4
Valid Data
Average
0.313
7/14/2023
RB
CAT-01 Rev. 0.0 9/13/2013
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 281 of 315 ©Mostardi Platt
Nozzle Calibration
Date:10/13/2023 Nozzle ID No.:Q-2525
Analyst:RMF Material/Type: Quartz
0.252 1
0.250 2
0.251 3
0.251 4
Valid Data
Average
0.251
CAT-01 Rev. 0.0 9/13/2013
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 282 of 315 ©Mostardi Platt
Nozzle Calibration
Date:Nozzle ID No.:864
Analyst:Material/Type: Quartz
0.275 1
0.274 2
0.274 3
0.275 4
Average
0.275
10/27/2021
KLJ
CAT-01 Rev. 0.0 9/13/2013
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 283 of 315 ©Mostardi Platt
Nozzle Calibration
Date:Nozzle ID No.:LV-8
Analyst:Material/Type: SS
0.238 1
0.239 2
0.238 3
0.237 4
Valid Data
Average
0.238
2/27/2021
JJC
CAT-01 Rev. 0.0 9/13/2013
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 284 of 315 ©Mostardi Platt
Client:Location:
Facility:Date:
Fuel Type:Operator:
Fuel Factor:Project #:
Diluent:Fuel Factor: by
Run # Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
1 11.26 11.30 11.10 0.00 0.00 0.00 11.20 13.65 13.7 0.89 -0.89 0.00 0.00
2 11.26 11.10 11.10 0.00 0.00 0.00 11.10 13.44 13.6 0.89 0.00 0.00 0.00
3 11.26 11.10 11.20 0.00 0.00 0.00 11.15 13.74 13.9 0.44 0.44 0.00 0.00
Run # Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
1 11.24 11.20 11.10 0.00 0.10 0.05 11.15 10.15 10.2 0.45 -0.45 -0.45 0.45
2 11.24 11.10 11.20 0.10 0.00 0.05 11.15 10.36 10.4 0.00 0.45 0.00 -0.45
3 11.24 11.20 11.10 0.00 0.00 0.00 11.15 10.82 10.9 0.45 -0.45 0.00 0.00
1 6/12/24 7:45 7:48 13.7 10.2
2 6/12/24 10:11 10:15 13.6 10.4
3 6/12/24 11:48 11:52 13.9 10.9
O2 % (dry)
Calibration Corrected Data
Run #Run
Date Start Time End
Time
CO2 %
(dry)
Ash Grove Cement Company Main Kiln Stack
Leamington Cement Plant 6/12/24
O2 %
O2 % (dry)
Coal, Bituminous
9780
MLIP
M242413
Standard
CO2 % (dry) Correction Data
Correction Data
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 285 of 315 ©Mostardi Platt
Client:Test Location:
Facility:Date:
Project #:Operator:
Operating Condition:
ft
in.
in.
ft
Sq. Ft.
Zero N/A >500
Mid 3/26/2032 >500
High 5/25/2031 >500
Zero N/A >500
Mid 3/26/2032 >500
High 5/25/2031 >500
CO2 % (dry)
Response Time Data
Start
RM Gas SpanRM Analyzer Make/Model
Servomex 1440
Servomex 1440
0.5
Time (min)
25
22.12
95% Response
25
Mill OFF
11.26
22.58
22.1022.12 0.09%
CC308342 22.58
CC308342
Horizontal
11.24
Port Length:7.00
6/12/24
0.00
MLIP
0.35%
11.30
Zero Nitrogen 0
Probe Length:
Zero NitrogenSG9160210
Main Kiln Stack
Analyzer Span
Ash Grove Cement Company
Leamington Cement Plant
Type
Difference, %
of Span
CO2 % (dry)
M242413
Expiration
Date
11.20
Type Setting
-0.18%
Analyzer
Response
0 0.00
22.50
0.00%
Downscale
O2 % (dry)
Upscale
0.18%
0.00%
RM Analyzer s/n
Cylinder ID Cylinder Value
O2 % (dry)SG9160210
Final Bottle
Pressure, PSI
O2/CO2 Samples taken by :Multi-point, integrated continuous sample
Sample Plane:
8.0
Port Size (diameter):8
Port Type:Flange
Duct Shape:Circular
Diameter:11
Duct Area:95.03
Upstream Diameters:4.090
Downstream Diameters:5.450
Number of Ports Sampled:1
Number of Points per Port:3
Total Number of Traverse Points:3
0.5
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 286 of 315 ©Mostardi Platt
Ash Grove Cement Company
Leamington Cement Plant
M242413
Main Kiln Stack
Mill OFF
6/12/24
Time CO2 % (dry)O2 % (dry)
5:32 22.50 22.10
5:33 22.50 ih 22.10 ih
5:34 22.40 22.20
5:35 22.40 22.10
5:36 12.10 13.50
5:37 0.10 0.00
5:38 0.00 iz 0.00 iz
5:39 0.00 z 0.00 z
5:40 0.00 0.00
5:41 0.00 18.80
5:42 0.00 20.70
5:43 9.10 11.60
5:44 11.30 11.20
5:45 11.30 im 11.20 im
5:46 11.30 m 11.20 m
Facility:
Client:
Linearity Cal/Pre 1 Cal
Project #:
Test Location:
Operating Condition:
Date:
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 287 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)Time CO2 % (dry)O2 % (dry)
8:10 0.00 0.10 10:26 0.00 0.00
8:11 0.00 z 0.10 z 10:27 0.00 0.00
8:12 0.00 0.10 10:28 0.00 z 0.00 z
8:13 7.90 6.90 10:29 0.00 0.00
8:14 11.10 11.20 10:30 2.90 6.80
8:15 11.10 m 11.10 m 10:31 11.00 11.10
10:32 11.10 m 11.20 m
Time CO2 % (dry)O2 % (dry)
13:48 0.00 0.00
13:49 0.00 z 0.00 z
13:40 3.60 8.50
13:41 11.20 11.10
13:42 11.20 m 11.10 m
Main Kiln Stack
Mill OFF
6/12/24
Ash Grove Cement Company
Leamington Cement Plant
M242413
Post 1/Pre 2
Post 3
Post 2/Pre 3
Test Location:
Operating Condition:
Date:
Client:
Facility:
Project #:
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 288 of 315 ©Mostardi Platt
Client:Test Location:
Facility:Operator:
Project #:Test Methods:
O2/CO2 Samples taken by :
Zero N/A
Mid 5/11/2031
High 3/8/2029
Zero N/A
Mid 5/11/2031
High 3/8/2029
Source Condition Start Time End Time Date Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero DriftRun 1 Mill Off 5:55 7:58 6/12/2024 11.18 11.00 11.10 0.00 0.00 0.00 11.05 7.50 7.6 0.52 0.52 0.00 0.00
Run 2 Mill Off 8:20 10:23 6/12/2024 11.18 11.10 11.10 0.00 0.00 0.00 11.10 6.70 6.7 0.52 0.00 0.00 0.00
Run 3 Mill Off 10:55 13:55 6/12/2024 11.18 11.10 11.10 0.00 0.00 0.00 11.10 6.67 6.7 0.52 0.00 0.00 0.00
Source Condition Start Time End Time Date Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
Run 1 Mill Off 5:55 7:58 6/12/2024 11.07 11.10 11.00 0.00 0.10 0.05 11.05 16.47 16.5 0.91 -0.45 -0.45 0.45
Run 2 Mill Off 8:20 10:23 6/12/2024 11.07 11.00 11.10 0.10 0.00 0.05 11.05 16.83 16.9 0.45 0.45 0.00 -0.45
Run 3 Mill Off 10:55 13:55 6/12/2024 11.07 11.10 11.10 0.00 0.00 0.00 11.10 16.90 16.9 0.45 0.00 0.00 0.00
Multi-point, integrated bag sample
11.20
0.09%22.00
Analyzer Data
Setting Expiration
Date
CC440199 11.18
O2 %
CO2 %
Servomex 1440Model/Serial #
O2 %Servomex 1440
CO2 %Type
22.02
-0.59%
0.00%O2%CC62689
0.00
11.07
19.2 19.30
CC62689
0
Type Analyzer Response
CC440199
CO2%
Zero Nitrogen
Cylinder ID
0.00
Cylinder Value
Zero Nitrogen
11.20 58.23%
0.00%
50.27%
-0.52%
-0.10%
Ash Grove Cement Company
Leamington Cement Plant
M242413
Coal Mill Stack
RB
0
3A,5
Mid cylinder % of high
cylinder
Difference, % of
Span
Correction Data
Correction Data
Calibration Gases - Linearity
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 289 of 315 ©Mostardi Platt
Client:
Facility:
Project #:
Test Location:
Date:6/12/2024
Time O2 % (dry)CO2 % (dry)
6:44 22.00 19.30
6:45 22.00 ih 19.30 ih
6:46 22.00 19.30
6:47 1.10 1.70
6:48 0.00 0.00
6:49 0.00 0.00
6:50 0.00 0.00
6:51 0.00 iz 0.00 iz
6:52 0.00 z 0.00 z
6:53 0.00 0.00
6:54 0.00 0.00
6:55 19.70 5.50
6:56 21.00 0.00
6:57 21.00 0.00
6:58 18.90 2.10
6:59 11.10 11.10
7:00 11.20 im 11.20 im
7:01 11.10 m 11.00 m
Linearity Cal/Pre Run 1 Cal
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
M242413
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 290 of 315 ©Mostardi Platt
Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)
8:50 0.10 0.00 10:30 0.00 0.10 12:05 0.00 0.00
8:51 0.10 z 0.00 z 10:31 0.00 z 0.00 z 12:06 0.00 z 0.00 z
8:52 4.30 2.30 10:32 5.10 4.90 12:07 0.50 0.208:53 10.90 11.00 10:33 11.00 11.00 12:08 9.20 8.80
8:54 11.00 11.10 10:34 11.10 11.10 12:09 11.10 11.10
8:55 11.00 m 11.10 m 10:35 11.10 m 11.10 m 12:10 11.10 m 11.10 m
Post 1/Pre 2 Post 2/Pre 3 Post 3
Client:Ash Grove Cement Company Test Location:Coal Mill StackFacility:Leamington Cement Plant M242413Project #:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 291 of 315 ©Mostardi Platt
Client:Test Location:
Facility:Operator:
Project #:Test Methods:
O2/CO2 Samples taken by :
Zero N/A
Mid 5/11/2031
High 3/8/2029
Zero N/A
Mid 5/11/2031
High 3/8/2029
Source Condition Start Time End Time Date Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero DriftRun 1 MILL ON 7:30 9:33 6/13/2024 11.18 11.00 11.10 0.00 0.00 0.00 11.05 7.50 7.6 0.52 0.52 0.00 0.00
Run 2 MILL ON 9:45 11:48 6/13/2024 11.18 11.10 11.10 0.00 0.00 0.00 11.10 6.70 6.7 0.52 0.00 0.00 0.00
Run 3 MILL ON 12:10 13:55 6/13/2024 11.18 11.10 11.10 0.00 0.00 0.00 11.10 6.67 6.7 0.52 0.00 0.00 0.00
Source Condition Start Time End Time Date Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
Run 1 MILL ON 7:30 9:33 6/13/2024 11.07 11.10 11.00 0.00 0.10 0.05 11.05 16.47 16.5 0.91 -0.45 -0.45 0.45
Run 2 MILL ON 9:45 11:48 6/13/2024 11.07 11.00 11.10 0.10 0.00 0.05 11.05 16.83 16.9 0.45 0.45 0.00 -0.45
Run 3 MILL ON 12:10 13:55 6/13/2024 11.07 11.10 11.10 0.00 0.00 0.00 11.10 16.90 16.9 0.45 0.00 0.00 0.00
Multi-point, integrated bag sample
11.20
0.09%22.00
Analyzer Data
Setting Expiration
Date
CC440199 11.18
O2 %
CO2 %
Servomex 1440Model/Serial #
O2 %Servomex 1440
CO2 %Type
22.02
-0.59%
0.00%O2%CC62689
0.00
11.07
19.2 19.30
CC62689
0
Type Analyzer Response
CC440199
CO2%
Zero Nitrogen
Cylinder ID
0.00
Cylinder Value
Zero Nitrogen
11.20 58.23%
0.00%
50.27%
-0.52%
-0.10%
Ash Grove Cement Company
Leamington Cement Plant
M242413
Coal Mill Stack
RB
0
3A,5
Mid cylinder % of high
cylinder
Difference, % of
Span
Correction Data
Correction Data
Calibration Gases - Linearity
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 292 of 315 ©Mostardi Platt
Client:
Facility:
Project #:
Test Location:
Date:6/13/2024
Time O2 % (dry)CO2 % (dry)
6:44 22.00 19.30
6:45 22.00 ih 19.30 ih
6:46 22.00 19.30
6:47 1.10 1.70
6:48 0.00 0.00
6:49 0.00 0.00
6:50 0.00 0.00
6:51 0.00 iz 0.00 iz
6:52 0.00 z 0.00 z
6:53 0.00 0.00
6:54 0.00 0.00
6:55 19.70 5.50
6:56 21.00 0.00
6:57 21.00 0.00
6:58 18.90 2.10
6:59 11.10 11.10
7:00 11.20 im 11.20 im
7:01 11.10 m 11.00 m
Linearity Cal/Pre Run 1 Cal
Ash Grove Cement Company
Leamington Cement Plant
Coal Mill Stack
M242413
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 293 of 315 ©Mostardi Platt
Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)Time O2 % (dry)CO2 % (dry)
8:50 0.10 0.00 10:30 0.00 0.10 12:05 0.00 0.00
8:51 0.10 z 0.00 z 10:31 0.00 z 0.00 z 12:06 0.00 z 0.00 z
8:52 4.30 2.30 10:32 5.10 4.90 12:07 0.50 0.208:53 10.90 11.00 10:33 11.00 11.00 12:08 9.20 8.80
8:54 11.00 11.10 10:34 11.10 11.10 12:09 11.10 11.10
8:55 11.00 m 11.10 m 10:35 11.10 m 11.10 m 12:10 11.10 m 11.10 m
Post 1/Pre 2 Post 2/Pre 3 Post 3
Client:Ash Grove Cement Company Test Location:Coal Mill StackFacility:Leamington Cement Plant M242413Project #:
AET-014 ISO Template V24.4 4/6/2022
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 294 of 315 ©Mostardi Platt
Client:Test Location:
Facility:Date:
Project #:Operator:
Operating Condition:
ft
ft
Sq. Ft.
Zero N/A >500
Mid 3/26/2032 >500
High 5/25/2031 >500
Zero N/A >500
Mid 3/26/2032 >500
High 5/25/2031 >500
Zero Zero Nitrogen 0 -0.66% N/A >500
Low AAL071292 10.08 -1.19% 6/6/2031 >500
Mid CC582200 19.82 -0.91% 6/30/2031 >500
High CC45760 30.17 -0.10% 6/12/2031 >500
TECO 51i 100
Predicted Value
20.00
N/A
01440D1/3791
CO2 % (dry)
Response Time Data
N/A
01440D1/3791
Cylinder
ValueType
Start
RM Gas SpanRM Analyzer Make/Model
Servomex 1440
Servomex 1440
0.5
Time (min)
25
22.12
95% Response
25
Mill On
10.20
30.20
11.26
Setting Predicted Value
Difference, %
0.20
22.58
N/A
THC ppmvw
N/A
10.22
Cylinder ID
19.91
22.1022.12
-0.46%
11.24
Zero Nitrogen
SG9160210
0.09%
CC308342 22.58
CC308342
6/13/24
0.00
MLIP
0.80%
11.20
Zero Nitrogen 0.0
Probe Length:
22.40
0.00%
Coal Mill
Analyzer Span
Ash Grove Cement Company
Leamington Plant
Type
Difference, %
of Span
CO2 % (dry)
M242413
Expiration
Date
11.20
Type Setting
0.27%
Analyzer
Response
0 0.00
Downscale
O2 % (dry)
Upscale
0.23%
Expiration
Date
Final Bottle
Pressure, PSI
0.18%
0.00%
Difference, %
of Cylinder
Analyzer
Response
110161896
RM Analyzer s/n
THC ppmvw
Cylinder ID Cylinder Value
O2 % (dry)SG9160210
Final Bottle
Pressure, PSI
Probe Type:Extractive
Sample Plane:
3.0
Horizontal
Duct Shape:Circular
Diameter:2.417
Duct Area:4.59
Upstream Diameters:1.800
Downstream Diameters:6.300
Number of Ports Sampled:1
Number of Points per Port:3
Total Number of Traverse Points:3
37
0.5
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 295 of 315 ©Mostardi Platt
Client:Location:
Facility:Date:
Fuel Type:Operator:
Fuel Factor:Project #:
Diluent:Fuel Factor: by
Run # Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
1 11.26 11.30 11.10 0.00 0.00 0.00 11.20 5.89 5.9 0.44 -0.89 0.00 0.00
2 11.26 11.10 11.20 0.00 0.10 0.05 11.15 6.07 6.1 0.00 0.44 -0.44 0.44
3 11.26 11.20 11.00 0.10 0.00 0.05 11.10 6.15 6.2 0.89 -0.89 0.00 -0.44
4 11.26 11.00 11.20 0.00 0.00 0.00 11.10 6.09 6.2 0.00 0.89 0.00 0.00
Run # Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift
1 11.24 11.70 11.30 0.00 0.20 0.10 11.50 17.33 17.0 -0.45 -1.81 -0.90 0.90
2 11.24 11.30 11.20 0.20 0.20 0.20 11.25 16.83 16.9 0.00 -0.45 -0.90 0.00
3 11.24 11.20 11.20 0.20 0.20 0.20 11.20 16.75 16.9 0.00 0.00 -0.90 0.00
4 11.24 11.20 11.30 0.20 0.20 0.20 11.25 16.80 16.9 -0.45 0.45 -0.90 0.00
Run # Cma Precal Postcal Pre zero Post zero Co Cm C Cgas Span Bias Span Drift Zero Bias Zero Drift1 19.82 20.00 20.20 0.20 0.40 0.30 20.10 3.30 3.3 -1.92 0.54 -1.08 0.54
2 19.82 20.20 20.20 0.40 0.50 0.45 20.20 3.70 3.7 -1.92 0.00 -1.35 0.27
3 19.82 20.20 20.20 0.50 0.20 0.35 20.20 4.10 4.1 -1.92 0.00 -0.54 -0.81
4 19.82 20.20 20.20 0.20 0.40 0.30 20.20 4.20 4.2 -1.92 0.00 -1.08 0.54
1 6/13/24 7:30 8:29 5.9 17.0 3.3 12.9 3.6 0.091
2 6/13/24 9:45 10:44 6.1 16.9 3.7 14.1 4.0 0.086
3 6/13/24 12:10 13:09 6.2 16.9 4.1 15.6 4.5 0.085
O2 % (dry) MoistureTHC ppmvd
O2 %
CH4 ppmv
THC ppmvw
THC @ 7% O2
Ash Grove Cement Company Coal Mill
Leamington Plant 6/13/24
Calibration Corrected Data
O2 % (dry)
Coal, Bituminous
9780
MLIP
M242413
Standard
Calibration Data
Run
Date
End
TimeRun # Start Time
CO2 %
(dry)
Calibration Data
THC
ppmvw
CO2 % (dry) Correction Data
Correction Data
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 296 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)THC ppmvw
7:55 0.00 0.00 -0.20
7:56 0.00 iz 0.00 iz 0.20 z
7:57 5.20 4.90 0.60
7:58 22.30 22.00 0.40
7:59 22.40 ih 22.10 ih 0.40
8:00 19.30 21.20 0.90
8:01 11.10 11.30 0.20
8:02 11.20 im 11.20 im 0.20
8:03 6.80 13.70 0.60
8:04 0.00 0.60 0.20
8:05 0.00 z 0.00 z 0.10
8:06 0.00 14.60 1.20
8:07 4.90 14.10 0.30
8:08 11.30 11.20 0.10
8:09 11.30 m 11.70 m 0.70
8:10 0.00 20.70 31.10
8:11 0.00 21.10 30.60
8:12 0.00 21.10 30.20 h
8:13 0.00 21.00 6.00
8:14 0.00 21.10 10.20 l
8:15 0.00 21.10 10.20
8:16 0.00 21.00 6.60
8:17 0.00 21.00 20.00
8:18 0.00 21.00 20.00 m
Facility:
Mill On
6/13/24
Linearity Cal/Pre 1 Cal
Project #:
Ash Grove Cement Company
Leamington Plant
M242413
Coal MillTest Location:
Operating Condition:
Date:
Client:
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 297 of 315 ©Mostardi Platt
Time CO2 % (dry)O2 % (dry)THC ppmvw Time CO2 % (dry)O2 % (dry)THC ppmvw
9:56 0.00 20.90 20.20 M 11:48 0.10 0.20 0.60
9:57 4.30 18.50 13.20 11:49 0.10 0.20 Z 0.50 Z
9:58 11.10 11.30 0.50 11:50 4.70 5.50 1.50
9:59 11.10 M 11.30 M 0.40 11:51 11.10 11.20 0.20
10:00 11.20 11.30 0.40 11:52 11.20 M 11.20 M 0.20
10:01 6.30 10.70 1.80 11:53 8.60 15.70 9.50
10:02 0.10 0.30 0.40 11:54 0.10 20.80 20.20 M
10:03 0.00 Z 0.20 Z 0.40 Z 11:55 0.10 Z 20.80 20.30
Time CO2 % (dry)O2 % (dry)THC ppmvw Time CO2 % (dry)O2 % (dry)THC ppmvw
13:17 0.00 20.60 20.00 15:36 0.10 0.30 0.30
13:18 0.00 20.70 20.20 m 15:37 0.00 z 0.20 z 0.40 z
13:19 4.80 15.20 5.20 15:38 10.90 11.30 1.70
13:20 11.00 m 11.20 m 0.30 15:39 11.10 11.10 0.40
13:21 11.10 11.20 0.40 15:40 11.20 m 11.30 m 1.00
13:22 4.70 5.60 1.70 15:41 3.20 19.70 18.50
13:23 0.00 z 0.20 z 0.20 z 15:42 0.00 20.60 20.20 m
13:24 0.10 0.20 0.20
Post 1/Pre 2
Post 3/Pre 4
Coal Mill
Mill On
6/13/24
Post 2/Pre 3
Post 4
Test Location:
Operating Condition:
Date:
Client:
Facility:
Project #:
Ash Grove Cement Company
Leamington Plant
M242413
Mostardi Platt Template Rev. 3/20/13
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 298 of 315 ©Mostardi Platt

Appendix I - Gas Cylinder Calibrations

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Page 300 of 315 ©Mostardi Platt
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
Customer:MOSTARDI PLATT,
Part Number: E02AI99E15A01H9 Reference Number: 163-402780762-1
Cylinder Number: CC58220 Cylinder Volume: 146.0 CF
Laboratory: 124 - Pasadena (SG06) - TX Cylinder Pressure: 2015 PSIG
PGVP Number: A32023 Valve Outlet: 590
Gas Code:PPN,BALA Certification Date: Jun 30, 2023
Expiration Date:Jun 30, 2031
Certification performed in accordance with “EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)” document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder below 100 psig, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
PROPANE 20.00 PPM 19.82 PPM G1 +/- 1.4% NIST Traceable 06/30/2023
AIR Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NTRM 180603-12 6162676Y 29.99 PPM PROPANE/AIR +/-0.4%Jun 14, 2025
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
C3H8-XL-NICOLET iS50 AUP2010248 FTIR Jun 17, 2023
Triad Data Available Upon Request
Airgas Specialty Gases
Airgas USA LLC
9810 BAY AREA BLVD
Pasadena, TX 77507
Airgas.com
Signature on file
Approved for Release Page 1 of 1Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 301 of 315 ©Mostardi Platt
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
Part Number: E02AI99E15A0705 Reference Number: 48-402750150-1
Cylinder Number: CC45760 Cylinder Volume: 146.0 CF
Laboratory: 124 - Los Angeles (SAP) - CA Cylinder Pressure: 2015 PSIG
PGVP Number: B32023 Valve Outlet: 590
Gas Code:PPN,BALA Certification Date: Jun 12, 2023
Expiration Date:Jun 12, 2031
Certification performed in accordance with “EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)” document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder below 100 psig, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
PROPANE 30.00 PPM 30.17 PPM G1 +/- 0.6% NIST Traceable 06/12/2023
AIR Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NTRM 16061117 EB0081910 50.06 PPM PROPANE/AIR +/- 0.5%Mar 22, 2028
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
Nicolet iS50 AUP2010243 C3H8 FTIR May 22, 2023
Triad Data Available Upon Request
Airgas Specialty Gases
Airgas USA LLC
11711 S. Alameda Street
Los Angeles, CA 90059
Airgas.com
Signature on file
Approved for Release Page 1 of 1Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 302 of 315 ©Mostardi Platt
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
Part Number: E03NI78E15A0225 Reference Number: 48-403001716-1
Cylinder Number: SG9160210 Cylinder Volume: 152.0 CF
Laboratory: 124 - Los Angeles (SAP) - CA Cylinder Pressure: 2015 PSIG
PGVP Number: B32024 Valve Outlet: 590
Gas Code:CO2,O2,BALN Certification Date: Mar 26, 2024
Expiration Date:Mar 26, 2032
Certification performed in accordance with “EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)” document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this 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 Cylinder below 100 psig, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
CARBON DIOXIDE 11.00 %11.26 %G1 +/- 0.6% NIST Traceable 03/26/2024
OXYGEN 11.00 %11.24 %G1 +/- 1.4% NIST Traceable 03/26/2024
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NTRM 08010611 K005428 13.94 % CARBON DIOXIDE/NITROGEN +/- 0.6%Aug 31, 2029
NTRM 98051113 SG9163010BAL 9.507 % OXYGEN/NITROGEN +/- 0.7%Mar 22, 2030
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
SIEMENS 6E CO2 NDIR Feb 26, 2024
SIEMENS OXYMAT 6 PARAMAGNETIC Mar 25, 2024
Triad Data Available Upon Request
Airgas Specialty Gases
Airgas USA LLC
11711 S. Alameda Street
Los Angeles, CA 90059
Airgas.com
Signature on file
Approved for Release Page 1 of 1Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 303 of 315 ©Mostardi Platt
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Appendix J - Mercury QA/QC Data
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 307 of 315 ©Mostardi Platt
METHOD 30B CALIBRATION SUMMARY
Project #: Location:
Client: Condition:
Facility: Data Taken By:
Analyzer ID:
Calibration ID: CAL-01
Standard Mass
(ng)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (%)
25 3300 26.27 5.08%
50 6400 50.95 1.90%
100 12000 95.53 4.47%
250 33600 267.49 7.00%
500 61700 491.19 1.76%
Slope: 0.007961 0.00760
R-Squared: 0.997487
Standard Mass
(ng)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (%)
25 3300 25.08 0.32%
Standard Mass
(ng)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (%)
100 12200 97.12 2.88%
Standard Mass
(ng)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (%)
100 13100 104.29 4.29%
100 13100 104.29 4.29%
100 13400 106.68 6.68%
M242413 Coal Mill Stack
Ash Grove Cement Company Mill On
Leamington Plant MLIP
Continuing Calibration Verification
Enter Lowest Calibration Point
Independent Calibration Verification
1455
FT-008 Hg Template V5.0 10/31/17
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 308 of 315 ©Mostardi Platt
Project #:Location:
Client:Condition:
Facility:Data Taken By:
Analyzer ID:
Cal Curve Run ID Trap ID Section
Ohio Lumex
Response
(Area)
Hg Mass
(ng)*
1-Sample 5300 42.2
2-Breakthrough 208 1.7
1-Sample 17200 136.9
2-Breakthrough 190 1.5
1-Sample 5030 40.0
2-Breakthrough 380 3.0
1-Sample 16400 130.6
2-Breakthrough 343 2.7
1-Sample 5900 47.0
2-Breakthrough 158 1.3
1-Sample 17100 136.1
2-Breakthrough 410 3.3
METHOD 30B TEST RESULTS
M242413 Coal Mill Stack
Ash Grove Cement Company Mill On
Leamington Plant MLIP
1455
3A OL667965
3B OL701305
2B OL701470
CAL-01
CAL-01
CAL-01
CAL-01
1A OLC189974
1B OL701370
2A OL607250
CAL-01
CAL-01
FT-008 Hg Template V5.0 10/31/17
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1A 43.9 N/A 48.921
1B 138.4 100 47.310
2A 43.0 N/A 48.647
2B 133.3 100 49.850
3A 48.3 N/A 48.349
3B 139.4 100 46.726
92.63
92.72
8:30
10:45
13:10
95.957:30
9:45 89.24
6/12/2024
6/12/2024
6/12/2024
Method 30B Spike Recovery Summary
Leamington Plant
Coal Mill Stack
Test Run
Sample Volume,
standard liters Recovery %
Expected Spike
Concentration, ng
Actual
Concentration, ngDate End TimeStart Time
12:10
Spike Recovery Average, %
FT-008 Hg Template V5.0 10/31/17
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Certificate of Analysis
1490 Lammers Pike
Batesville, IN 47006
http://www.riccachemical.com
1-888-GO-RICCA
[e-mail]
Mercury ICP Standard, 1000 ppm Hg in 3% HNO₃
Manufacture Date: FEB 07, 2024
Expiration Date: JUL 2025Lot Number: 4402F45 Product Number: PHG1KN
The certified value for this product is confirmed in independent testing by a second qualified chemist. The uncertainty associated with the certified value is ± 0.5% relative, which is the sum of the estimated errors due to the purity of the raw material, the volumetric preparation of the solution, and
transpiration of the solution through the container wall.
The final solution concentration is confirmed by AA, ICP, or ICP-MS, and is traceable to NIST Standard Reference Material 3133. All trace level
elements were determined by ICP or ICP-MS.
Name CAS#Grade
7732-18-5Water
7697-37-2Nitric Acid
7439-97-6Mercury
Test ResultSpecification NIST SRM#
Appearance Passed Colorless liquid
Assay (vs. Potassium Thiocyanate/Volhard's
Indicator)
1000 ppm Hg 995-1005 ppm Hg 999
Trace Elements by ICP or ICP - MS
All values reported in mg/L (ppm)
I=Spectral Interference N=Not Tested
Aluminum (Al) < 0.0009 ppm
Antimony (Sb) < 0.0001 ppm
Arsenic (As) < 0.0007 ppm
Barium (Ba) < 0.0001 ppm
Beryllium (Be) < 0.0001 ppm
Bismuth (Bi) 0.0058 ppm
Boron (B)< 0.00005 ppm
Cadmium (Cd)< 0.00007 ppm
Calcium (Ca) < 0.004 ppm
Cerium (Ce)< 0.00003 ppm
Cesium (Cs) 0.0221 ppm
Chromium (Cr) 0.1452 ppm
Cobalt (Co)< 0.00002 ppm
Copper (Cu)< 0.00005 ppm
Dysprosium (Dy) < 0.0001 ppm
Erbium (Er)< 0.00007 ppm
Europium (Eu)< 0.00008 ppm
Gadolinium (Gd) 0.0010 ppm
Gallium (Ga) < 0.0006 ppm
Germanium (Ge) 0.0009 ppm
Gold (Au) I
Hafnium (Hf) 0.0024 ppm
Holmium (Ho) < 0.0001 ppm
Indium (In)< 0.00003 ppm
Iridium (Ir)< 0.00007 ppm
Iron (Fe)N
Lanthanum (La)< 0.00004 ppm
Lead (Pb) 0.4326 ppm
Lithium (Li) < 0.03 ppm
Lutetium (Lu) < 0.0003 ppm
Magnesium (Mg) < 0.0007 ppm
Manganese (Mn) 0.0141 ppm
Molybdenum (Mo) 0.0874 ppm
Neodymium (Nd) < 0.0002 ppm
Nickel (Ni) < 0.0001 ppm
Niobium (Nb) 0.0013 ppm
Osmium (Os) 0.0357 ppm
Palladium (Pd) 0.0386 ppm
Phosphorus (P) I
Platinum (Pt)< 0.00003 ppm
Potassium (K) I
Praseodymium (Pr)< 0.00003 ppm
Rhenium (Re)< 0.00003 ppm
Rhodium (Rh) 0.0047 ppm
Rubidium (Rb)< 0.00004 ppm
Ruthenium (Ru) 0.0011 ppm
Samarium (Sm) < 0.002 ppm
Scandium (Sc) 0.0003 ppm
Selenium (Se) < 0.004 ppm
Silicon (Si) I
Silver (Ag) I
Sodium (Na) I
Strontium (Sr)< 0.00006 ppm
Sulfur (S) 0.7628 ppm
Tantalum (Ta) 0.2642 ppm
Tellurium (Te) I
Terbium (Tb)< 0.00003 ppm
Thallium (Tl) 0.0505 ppm
Thorium (Th) 0.0012 ppm
Thulium (Tm)< 0.00002 ppm
Tin (Sn)0.0007 ppm
Titanium (Ti) < 0.001 ppm
Tungsten (W) < 0.0001 ppm
Uranium (U)< 0.00007 ppm
Vanadium (V)< 0.00004 ppm
Ytterbium (Yb) < 0.001 ppm
Yttrium (Y) 0.0016 ppm
Zinc (Zn)I
Zirconium (Zr) < 0.002 ppm
Version: 1.5 Product Number: PHG1KNLot Number: 4402F45 Page 1 of 2
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ReferenceSpecification
Mercury ICP Standard, 1 mL = 1 mg Hg (1,000 ppm Hg) Hg in 3%
HNO3
EPA (200.7)
This standard is guaranteed to be stable and accurate provided the product is kept tightly capped and stored under normal laboratory conditions. Balances are calibrated using NIST traceable weights whose verification of maintenance and recalibration is documented per in-house Standard
Operating Procedures. Class A glassware is also calibrated and routinely rechecked per in-house Standard Operating Procedures. Trace metal analyzed acids and Trace Metals Analyzed Water are used in the manufacture of this product. Triple cleaned containers are used in the manufacture of
this product.
Part Number Shelf Life (Unopened Container)Size / Package Type
PHG1KN-100 18 months100 mL natural LDPE
Recommended Storage: 15°C - 30°C (59°F - 86°F)
This document is designed to comply with ISO Guide 31 "Reference Materials --
Contents of Certificates and Labels."
Production Manager
Paul Brandon (02/07/2024)
This test report shall not be reproduced, except in full, without the written approval of Ricca Chemical Company.
Version: 1.5 Product Number: PHG1KNLot Number: 4402F45 Page 2 of 2
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Page 314 of 315 ©Mostardi Platt

END OF THE REPORT
Project No. M242413B Clinker Cooler Stack, Coal Mill Stack, and Main Kiln Stack
Page 315 of 315 ©Mostardi Platt
Client:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Temp ID:
Meter ID:
Pitot ID:
Nozzle Diameter (Inches):
Meter Calibration Date:
Meter Calibration Factor (Y):
Meter Orifice Setting (Delta H):
Nozzle Kit ID Number and Material:
Pre Pitot Leak Check 0.0 @ 4.0 "H2O 0.0 @ 3.0 "H2O 0.0 @ 6.0 "H2O
Post Pitot Leak Check 0.0 @ 5.0 "H2O 0.0 @ 6.0 "H2O 0.0 @ 4.0 "H2O
Pre Nozzle Leak Check 0.0010 @ 14 "Hg 0.0020 @ 17 "Hg 0.0030 @ 13 "Hg
Post Nozzle Leak Check 0.0010 @ 15 "Hg 0.0030 @ 16 "Hg 0.0010 @ 14 "Hg
Pitot Tube Coefficient:
Probe Length (Feet):
Probe Liner Material:
Sample Plane:
Port Length (Inches):
Port Size (Diameter, Inches):
Port Type:
Duct Shape:
Duct Area (Square Feet):
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Minutes per Point:
Minutes per Reading:
Total Number of Traverse Points:
Test Length (Minutes):
Train Type:
Source Condition:
Diluent Model/Serial Number:
Moisture Balance ID:
# of Runs
0.995 0.995
CM56
CM56
569
CM56
CM56
1.669
0.276
6.0
quartz
GLASS SET #39 446
0.276
5/24/2024
Run 1
569
5/24/2024
569
CM56
CM56
AIR
Run 3
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
M242413
23
RB
Horizontal
7.00
5/24/2024
GLASS SET #39 446
0.995
6.00
GLASS SET #39 446
Run 2
7.5
1.6691.669
0.276
24
180
Flange
Circular
4.1
5.5
95.033
Anderson Box
Mill On
Servomex 1440 01440D1/3791
LV2
3
Leak Checks
0.840
4
6
7.5
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.98 in. H2O -0.60 in. H2O
76.4 °F 25.05 in. Hg. abs.
0.767 in. H2O 14.60 %
231.3 °F 12.00 %
162.246 ft3 73.40 %
134.034 dscf 30.816 lb/lb mole
21.854 wscf 29.019 lb/lb mole
101.2 %I --- %
53.703 fps
180.00 in mins.306,214 acfm
0.276 in inches 168,324 dscfm
25.09 in Hg 195,769 scfm
2667.3 ml 821.5 grams
3110.6 ml 842.2 grams
443.3 ml 20.7 grams
464.0 0.140
Velocity Orifice Actual Stack Pump Probe Filter Impinger XAD TRAP
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg
oF oF oF °F
1-1 8:10:00 0.55 1.85 80.155 232 74 74 5 246 249 38 40
1-2 8:17:30 0.57 1.92 86.650 232 74 74 5 250 249 38 40
1-3 8:25:00 0.59 1.99 93.270 232 74 74 5 250 248 39 42
1-4 8:32:30 0.60 2.02 100.010 232 75 75 5 251 250 39 42
1-5 8:40:00 0.62 2.09 106.820 233 75 75 5 250 255 40 42
1-6 8:47:30 0.63 2.12 113.740 233 75 75 5 245 252 40 43
8:55:00 120.719
2-1 8:58:00 0.54 1.82 120.719 233 75 75 5 242 252 42 45
2-2 9:05:30 0.55 1.85 127.160 233 75 75 5 243 252 42 45
2-3 9:13:00 0.57 1.92 133.680 233 75 75 5 245 251 43 46
2-4 9:20:30 0.59 1.99 140.310 232 75 75 5 244 251 43 46
2-5 9:28:00 0.61 2.06 147.060 232 75 75 5 244 250 45 48
2-6 9:35:30 0.63 2.12 153.930 232 75 75 5 242 248 46 49
9:43:00 160.910
3-1 9:46:00 0.55 1.85 160.910 231 76 76 5 252 250 48 50
3-2 9:53:30 0.56 1.89 167.430 231 76 76 5 250 240 50 50
3-3 10:01:00 0.58 1.95 174.030 231 76 76 5 251 250 50 52
3-4 10:08:30 0.60 2.02 180.740 230 77 77 5 253 250 51 52
3-5 10:16:00 0.61 2.06 187.590 230 77 77 5 250 250 51 53
3-6 10:23:30 0.62 2.09 194.490 230 77 77 5 249 247 51 53
10:31:00 201.450
4-1 10:34:00 0.54 1.82 201.450 230 79 79 5 252 246 53 54
4-2 10:41:30 0.56 1.89 207.950 230 79 79 5 252 250 54 54
4-3 10:49:00 0.59 1.99 214.590 230 79 79 5 251 250 54 55
4-4 10:56:30 0.61 2.06 221.400 230 80 80 5 251 251 55 57
4-5 11:04:00 0.62 2.09 228.350 230 80 80 5 250 250 55 57
4-6 11:11:30 0.63 2.12 235.340 230 80 80 5 248 245 56 58
11:19:00 242.401
Total 3:00:00 162.246 76.4 76.4
Average 1.98 231.3 76.4 5
Min 1.82 230.0 74.0 5
Max 2.12 233.0 80.0 5
Run 1 - Method 23
Source Condition:
Nitrogen:
STACK CONDITIONS
11:19
Start Time:
Meter Volume, Vwstd:
8:10
6/11/24
Sqrt ∆P:
End Time:
Date:
Meter Volume, Vm:
Meter Volume, Vmstd:
Gas Weight wet, Ms:
Gas Weight dry, Md:
∆H:
Silica Difference:
Total Water Gain:
Final Impinger Content: Silica Final Wt.
Barometric Pressure:
Silica Initial Wt.
Volumetric Flow:
Moisture, Bws:
Static Pressure
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Meter Temperature, Tm:
Oxygen:
Flue Pressure (Ps):
Test Length:
Nozzle Diameter:
Carbon Dioxide:
Volumetric Flow:
Meter Temp
Impinger Difference:
MOISTURE DETERMINATION
Isokinetic Variance:
Gas Velocity, Vs:
Initial Impinger Content:
Excess Air:
Volumetric Flow:
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company 6/11/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/11/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 732.1 413.2 318.9
DI Water 835.2 724.7 110.5
DI Water 749.3 743.1 6.2
Empty 794.0 786.3 7.7
Silica Gel 842.2 821.5 20.7
3,110.6 2,667.3 443.3
Liquid Final Liquid Initial Liquid Gain
842.2 821.5 20.7
Silica Final Silica Initial Silica Gain
250
500
750
Impinger Weight Sheet - Run 1
Scale Calibration Check Date:
Scale Calibration Check (see QS-6.05C for procedure)
must be within ± 0.5g of certified mass
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.98 In. H2O -0.60 in. H2O
86.1 °F 25.05 in. Hg. abs.
0.767 In. H2O 16.10 %
233.5 °F 11.70 %
164.955 ft3 72.2 %
133.850 dscf 31.044 lb/lb mole
21.826 wscf 29.215 lb/lb mole
101.6 %I --- %
53.607 fps
180.00 in mins.305,666 acfm
0.276 in inches 167,496 dscfm
25.09 in Hg 194,808 scfm
2671.8 ml 773.7 grams
3115.3 ml 793.6 grams
443.5 ml 19.9 grams
463.4 0.140
Velocity Orifice Actual Stack Pump Probe Filter Impinger XAD TRAP
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg
oF oF oF °F
1-1 11:35:00 0.54 1.82 44.214 233 84 84 5 249 254 51 55
1-2 11:42:30 0.55 1.85 50.760 233 85 85 5 250 254 50 55
1-3 11:50:00 0.58 1.95 57.400 233 85 85 5 250 253 50 55
1-4 11:57:30 0.59 1.99 64.220 233 85 85 5 251 250 51 56
1-5 12:05:00 0.61 2.06 71.090 233 85 85 5 251 250 51 56
1-6 12:12:30 0.63 2.12 78.080 233 86 86 5 252 249 51 57
12:20:00 85.202
2-1 12:23:00 0.54 1.82 85.202 233 86 86 5 250 249 53 58
2-2 12:30:30 0.56 1.89 91.780 234 86 86 5 250 250 53 58
2-3 12:38:00 0.59 1.99 98.480 234 86 86 5 249 251 53 58
2-4 12:45:30 0.61 2.06 105.360 234 86 86 5 254 251 54 57
2-5 12:53:00 0.62 2.09 112.360 233 86 86 5 254 252 55 57
2-6 13:00:30 0.63 2.12 119.420 233 86 86 5 253 255 55 56
13:08:00 126.554
3-1 13:11:00 0.55 1.85 126.554 234 86 86 5 249 250 57 57
3-2 13:18:30 0.57 1.92 133.180 234 86 86 5 244 252 57 58
3-3 13:26:00 0.58 1.95 139.950 234 86 86 5 244 252 58 58
3-4 13:33:30 0.60 2.02 146.770 234 86 86 5 247 251 59 59
3-5 13:41:00 0.62 2.09 153.710 234 87 87 5 250 251 59 59
3-6 13:48:30 0.62 2.09 160.790 234 87 87 5 250 249 60 59
13:56:00 167.866
4-1 13:59:00 0.54 1.82 167.866 234 87 87 5 250 249 61 60
4-2 14:06:30 0.57 1.92 174.450 234 87 87 5 255 250 61 60
4-3 14:14:00 0.59 1.99 181.220 234 87 87 5 255 251 61 59
4-4 14:21:30 0.60 2.02 188.120 233 87 87 5 251 252 60 59
4-5 14:29:00 0.61 2.06 195.080 233 87 87 5 248 255 60 59
4-6 14:36:30 0.62 2.09 202.090 233 87 87 5 246 253 59 58
14:44:00 209.169
Total 3:00:00 164.955 86.1 86.1
Average 1.98 233.5 86.1 5
Min 1.82 233.0 84.0 5
Max 2.12 234.0 87.0 5
Run 2 - Method 23
Carbon Dioxide:
Silica Final Wt.
Meter Temp
Volumetric Flow:
Test Length:
Barometric Pressure:
Volumetric Flow:Nozzle Diameter:
Volumetric Flow:
Silica Initial Wt.
Total Water Gain: Moisture, Bws:
Final Impinger Content:
Silica Difference:
Initial Impinger Content:
MOISTURE DETERMINATION
Impinger Difference:
6/11/24
11:35
Meter Volume, Vmstd:
Static Pressure∆H:
Sqrt ∆P:
Gas Weight dry, Md:
Oxygen:
STACK CONDITIONS
14:44
Gas Velocity, Vs:
Date:
Start Time:
End Time:
Meter Temperature, Tm:Flue Pressure (Ps):
Source Condition:
DRY GAS METER CONDITIONS
Stack Temperature, Ts:
Isokinetic Variance:
Meter Volume, Vwstd:Gas Weight wet, Ms:
Meter Volume, Vm:Nitrogen:
Excess Air:
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company 6/11/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/11/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 737.8 419.0 318.8
DI Water 856.9 746.3 110.6
DI Water 751.8 744.9 6.9
Empty 768.8 761.6 7.2
Silica Gel 793.6 773.7 19.9
3,115.3 2,671.8 443.5
Liquid Final Liquid Initial Liquid Gain
793.6 773.7 19.9
Silica Final Silica Initial Silica Gain
must be within ± 0.5g of certified mass
Scale Calibration Check (see QS-6.05C for procedure)
Impinger Weight Sheet - Run 2
Scale Calibration Check Date:
250
500
750
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Mill On
1.98 In. H2O -0.60 in. H2O
87.9 °F 25.05 in. Hg. abs.
0.766 In. H2O 16.30 %
234.8 °F 11.60 %
165.082 ft3 72.1 %
133.512 dscf 31.072 lb/lb mole
21.845 wscf 29.234 lb/lb mole
101.7 %I --- %
53.562 fps
180.00 in mins.305,411 acfm
0.276 in inches 166,976 dscfm
25.09 in Hg 194,296 scfm
2506.3 ml 817.2 grams
2949.3 ml 838.0 grams
443.0 ml 20.8 grams
463.8 0.141
Velocity Orifice Actual Stack Pump Probe Filter Impinger XAD TRAP
Port- Clock Head ∆p ∆H Meter Vol. Temp Inlet Outlet Vacuum Temp Exit Temp Exit Temp Temp
Point No. Time in. H2O in. H2O ft3 °F °F °F "Hg
oF oF oF °F
1-1 15:00:00 0.54 1.82 11.645 235 87 87 5 249 246 57 44
1-2 15:07:30 0.56 1.89 18.220 235 87 87 5 244 250 57 44
1-3 15:15:00 0.58 1.95 24.930 235 87 87 5 245 250 56 45
1-4 15:22:30 0.59 1.99 31.760 235 87 87 5 247 251 56 45
1-5 15:30:00 0.60 2.02 38.650 235 87 87 5 254 250 55 46
1-6 15:37:30 0.62 2.09 45.600 235 88 88 5 254 245 55 47
15:45:00 52.682
2-1 15:48:00 0.54 1.82 52.682 235 88 88 5 250 248 55 47
2-2 15:55:30 0.55 1.85 59.270 236 88 88 5 255 246 55 48
2-3 16:03:00 0.58 1.95 65.930 236 88 88 5 255 245 54 48
2-4 16:10:30 0.60 2.02 72.770 236 88 88 5 251 244 54 49
2-5 16:18:00 0.61 2.06 79.720 236 88 88 5 248 244 55 50
2-6 16:25:30 0.63 2.12 86.740 236 88 88 5 246 249 55 50
16:33:00 93.868
3-1 16:36:00 0.55 1.85 93.868 235 89 89 5 254 250 56 52
3-2 16:43:30 0.57 1.92 100.530 235 89 89 5 254 249 56 52
3-3 16:51:00 0.58 1.95 107.330 235 89 89 5 253 250 56 53
3-4 16:58:30 0.60 2.02 114.180 234 89 89 5 250 250 57 54
3-5 17:06:00 0.61 2.06 121.160 234 89 89 5 250 250 57 54
3-6 17:13:30 0.62 2.09 128.200 234 89 89 5 249 252 58 55
17:21:00 135.294
4-1 17:24:00 0.54 1.82 135.294 233 89 89 5 249 254 58 56
4-2 17:31:30 0.56 1.89 141.900 233 87 87 5 250 250 59 56
4-3 17:39:00 0.59 1.99 148.630 234 87 87 5 251 250 59 57
4-4 17:46:30 0.61 2.06 155.520 234 87 87 5 251 251 60 57
4-5 17:54:00 0.62 2.09 162.530 234 87 87 5 252 250 60 57
4-6 18:01:30 0.63 2.12 169.600 234 87 87 5 255 245 61 56
18:09:00 176.727
Total 3:00:00 165.082 87.9 87.9
Average 1.98 234.8 87.9 5
Min 1.82 233.0 87.0 5
Max 2.12 236.0 89.0 5
Run 3 - Method 23
6/11/24
15:00
18:09
∆H:
Stack Temperature, Ts:
Meter Volume, Vm:
Test Length:
Meter Volume, Vwstd:
Gas Weight dry, Md:
Gas Weight wet, Ms:
Gas Velocity, Vs:
Meter Temperature, Tm:
DRY GAS METER CONDITIONS
Date:
Start Time:
Source Condition:
Meter Volume, Vmstd:
End Time:
Static Pressure
Flue Pressure (Ps):
STACK CONDITIONS
Silica Final Wt.
Silica Difference:
Silica Initial Wt.
Excess Air:
Volumetric Flow:
Nitrogen:
Sqrt ∆P:
Nozzle Diameter:
Isokinetic Variance:
Initial Impinger Content:
Volumetric Flow:
Volumetric Flow:
Oxygen:
Carbon Dioxide:
Meter Temp
Barometric Pressure:
MOISTURE DETERMINATION
Moisture, Bws:Total Water Gain:
Final Impinger Content:
Impinger Difference:
AET-014 ISO Template V26.7 5/7/24
Client: Ash Grove Cement Company 6/11/2024
Facility: Leamington Cement Plant
Test Location: Main Kiln Stack
Project #: M242413 Certified Weight, grams Result, grams
Date: 6/11/2024 250.0
Test Method: 23
Weighed/Measured By: RB 500.0
Balance ID: LV2
750.0
IMPINGER FINAL INITIAL GAIN
CONTENTS MLS / GRAMS MLS / GRAMS MLS / GRAMS
Empty 734.1 416.5 317.6
DI Water 792.9 682.0 110.9
DI Water 742.2 736.8 5.4
Empty 680.1 671.0 9.1
Silica Gel 838.0 817.2 20.8
2,949.3 2,506.3 443.0
Liquid Final Liquid Initial Liquid Gain
838.0 817.2 20.8
Silica Final Silica Initial Silica Gain
Scale Calibration Check (see QS-6.05C for procedure)
250
500
750
Impinger Weight Sheet - Run 3
Scale Calibration Check Date:
must be within ± 0.5g of certified mass
AET-014 ISO Template V26.7 5/7/24
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name Ash Grove - Main Kiln/Raw Mill Off
Company Contact:Cody Watkins
Contact Phone No.[phone]
Source Designation:Main Kiln/Raw Mill Off
Test & Review Dates
Test Date: 6/13/2024
Review Date: 8/25/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/Ton Clinker lbs/hr gr/dscf
0.070
Emission Rates - "Front Half"
lbs/Ton Clinker lbs/hr gr/dscf
0.013 1.4249 0.0010
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
132.00 95.033 0.9950 1.669 0.84 25.08 -0.7 0.251
Contractor Information
Contracting Company: Alliance Source Testing
Contact: Austin Keough
Phone No.: 385-722-6712
Project No.:
1800
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
Ash Grove - Main Kiln/Raw Mill Off
Testing Results Lab Data - grams collected
Test Date 6/13/2024 6/13/2024 6/13/2024 6/13/2024 Lab Data Probe Filter Back 9.8
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.00195 0.00166 0
As ft^2 95.03 95.03 95.03 95.03 Run 2 0.00149 0.00185 0
Pbar 25.08 25.08 25.08 25.08 Run 3 0.00025 0.0018 0
Pq (static)-0.70 -0.70 -0.70 -0.70 Run 4 0 0.00988
Ps 25.03 25.03 25.03 25.03
Avg. Ts F 226.71 225.58 224.13 224.50 Front Half Emissions Summary
CO2 - FCO2 15.50 16.10 15.70 15.70 Run 1 Run 2 Run 3 Run 4 Avg.
O2 11.60 11.40 11.60 11.40 gr./dscf 0.0008 0.0007 0.0004 0.0021 0.001
N2+C 72.90 72.50 72.70 72.90 lbs/hr 1.0850 1.0054 0.6184 2.9909 1.425
Md 30.94 31.03 30.98 30.97 lbs/Ton of Clinke 0.0100 0.0093 0.0057 0.0275 0.013
Ms 29.04 29.13 29.12 29.15
Y 1.00 1.00 1.00 1.00
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 83.41 86.16 90.33 90.06 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 254.80 254.60 258.70 251.60 gr./dscf 0.0008 0.0007 0.0004 0.0021 0.0010
AVG. Tm F 70.50 81.58 85.83 86.58 lbs/hr 1.0850 1.0054 0.6184 2.9909 1.4249
Vm std 69.45 70.28 73.13 72.81 lbs/MMBtu #DIV/0!
Vw std 11.99 11.98 12.18 11.84
Bws 0.15 0.15 0.14 0.14
S Bws 1.00 1.00 1.00 1.00
Avg. Sqrt
Dlp 0.72 0.73 0.76 0.76
Vs 50.45 50.95 52.84 52.64 F factor used
scfm wet 185015.72 187173.10 194525.06 193686.93 1800
acfm 287655.22 290532.69 301302.22 300168.49
Qsd dscfh 9466245 9594376 10005526 9995348.2
# Sample
Points 24.00 24.00 24.00 24.00
Dn 0.251 0.251 0.251 0.251
An 3.44E-04 3.44E-04 3.44E-04 3.44E-04
Start Time
End Time
Total Test
time 120.00 120.00 120.00 120.00
Time @ point 5.00 5.00 5.00 5.00
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
Page 1
Run 1
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.08 -0.70 25.03 226.7 15.50 11.60 72.90 30.94 29.038
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.5955
0.9950 0.84 83.406 254.80 70.50 69.452 11.993 0.1473 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.723 50.448 185,016 287,655 9.47E+06 24 0.251 120 5.00 1.197917
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 84.051 0.61 1.39 226.0 70.0 70.0 Wt. (Final) Wt. (Initial) lc
2 87.850 0.57 1.30 226.0 70.0 70.0 752.90 603.20 149.7
3 91.440 0.50 1.14 226.0 70.0 70.0 782.80 697.40 85.4
4 94.850 0.48 1.10 226.0 70.0 70.0 631.30 630.70 0.6
5 98.170 0.45 1.03 226.0 70.0 70.0 841.00 821.90 19.1
6 101.380 0.40 0.91 226.0 70.0 70.0 0.0
7 104.422 0.64 1.46 226.0 70.0 70.0
8 108.290 0.61 1.39 227.0 70.0 70.0 Isokinetics 101.5
9 112.120 0.57 1.30 227.0 70.0 70.0 Test Date 6/13/2024
10 115.650 0.54 1.23 227.0 70.0 70.0 Start Time enter enter
11 119.170 0.49 1.12 227.0 70.0 70.0 End Time enter
12 122.540 0.42 0.96 227.0 70.0 70.0
13 125.641 0.60 1.37 227.0 71.0 71.0
14 129.370 0.56 1.28 227.0 71.0 71.0
15 132.980 0.54 1.23 227.0 71.0 71.0
16 136.530 0.50 1.14 227.0 71.0 71.0
17 139.920 0.45 1.03 227.0 71.0 71.0
18 143.140 0.41 0.94 227.0 71.0 71.0
19 146.220 0.65 1.48 227.0 71.0 71.0
20 150.110 0.63 1.44 227.0 71.0 71.0
21 153.940 0.57 1.30 227.0 71.0 71.0
22 157.550 0.50 1.14 227.0 71.0 71.0
23 160.950 0.47 1.07 227.0 71.0 71.0
24 164.270 0.44 1.00 227.0 71.0 71.0
25 167.457
26
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Page 1
Run 2
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.08 -0.70 25.03 226 16.10 11.40 72.50 31.03 29.13

Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.5617
0.9950 0.84 86.157 254.60 82 70.280 11.984 0.1457 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.732 50.95 187,173 290,533 9.59E+06 24 0.251 120 5.00 1.23
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 76.593 0.65 1.48 225.0 81.0 81.0 Wt. (Final) Wt. (Initial) lc
2 80.550 0.61 1.39 225.0 81.0 81.0 794.50 645.10 149.4
3 84.380 0.58 1.32 225.0 81.0 81.0 799.60 714.20 85.4
4 88.120 0.55 1.26 225.0 81.0 81.0 602.80 602.00 0.8
5 91.780 0.47 1.07 225.0 81.0 81.0 832.80 813.80 19.0
6 95.120 0.45 1.03 225.0 81.0 81.0 0.0
7 98.410 0.63 1.44 225.0 81.0 81.0
8 102.302 0.59 1.35 225.0 81.0 81.0 Isokinetics 101.3
9 106.100 0.56 1.28 225.0 81.0 81.0 Test Date 6/13/2024
10 109.740 0.51 1.16 225.0 81.0 81.0 Start Time enter
11 113.250 0.48 1.10 226.0 82.0 82.0 End Time enter
12 116.640 0.46 1.05 226.0 82.0 82.0
13 119.970 0.64 1.46 226.0 82.0 82.0
14 123.900 0.58 1.32 226.0 82.0 82.0
15 127.640 0.53 1.21 226.0 82.0 82.0
16 131.22 0.49 1.12 226.0 82.0 82.0
17 134.650 0.47 1.07 226.0 82.0 82.0
18 138.020 0.44 1.00 226.0 82.0 82.0
19 141.280 0.63 1.44 226.0 82.0 82.0
20 145.180 0.58 1.32 226.0 82.0 82.0
21 148.920 0.56 1.28 226.0 82.0 82.0
22 152.600 0.52 1.19 226.0 82.0 82.0
23 156.140 0.47 1.07 226.0 82.0 82.0
24 159.500 0.45 1.03 226.0 82.0 82.0
25 162.790
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Page 1
Run 3
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.08 -0.70 25.03 224 15.70 11.60 72.70 30.98 29.12
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.5188
0.9950 0.84 90.332 258.70 86 73.133 12.177 0.1427 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.760 52.84 194,525 301,302 1.00E+07 24 0.251 120 5.00 1.32
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 64.358 0.68 1.55 223.0 85.0 85.0 Wt. (Final) Wt. (Initial) lc
2 68.440 0.65 1.48 223.0 85.0 85.0 837.1 687.7 149.4
3 72.430 0.62 1.42 223.0 85.0 85.0 795.3 709.0 86.3
4 76.330 0.58 1.32 223.0 85.0 85.0 620.9 620.1 0.8
5 80.100 0.56 1.28 223.0 85.0 85.0 878.8 856.6 22.2
6 83.800 0.51 1.16 224.0 85.0 85.0
7 87.330 0.66 1.51 224.0 85.0 85.0
8 91.350 0.63 1.44 224.0 85.0 85.0 Isokinetics 101.1
9 95.280 0.59 1.35 224.0 85.0 85.0 Test Date 6/13/2024
10 99.100 0.55 1.26 224.0 85.0 85.0 Start Time enter
11 102.740 0.52 1.19 224.0 86.0 86.0 End Time enter
12 106.310 0.50 1.14 224.0 86.0 86.0
13 109.810 0.65 1.48 224.0 86.0 86.0
14 113.810 0.60 1.42 224.0 86.0 86.0
15 117.710 0.58 1.32 224.0 86.0 86.0
16 121.480 0.55 1.26 224.0 86.0 86.0
17 125.150 0.51 1.16 225.0 86.0 86.0
18 128.690 0.49 1.12 225.0 86.0 86.0
19 132.150 0.65 1.48 225.0 87.0 87.0
20 136.150 0.63 1.44 225.0 87.0 87.0
21 140.100 0.59 1.35 225.0 87.0 87.0
22 143.900 0.56 1.28 225.0 87.0 87.0
23 147.610 0.52 1.19 225.0 87.0 87.0
24 151.180 0.50 1.14 225.0 87.0 87.0
25 154.690
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Page 1
Run 4
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.08 -0.70 25.03 225 15.70 11.40 72.90 30.97 29.15
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.5298
0.9950 0.84 90.055 251.60 87 72.806 11.843 0.1399 0.9990 0.999
Avg. Sqrt Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.757 52.64 193,687 300,168 1.00E+07 24 0.251 120 5.00 1.31
TRUE
Mv@ Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 56.465 0.66 1.51 225.0 86.0 86.0 Wt. (Final) Wt. (Initial) lc
4.025 2 60.490 0.62 1.42 225.0 86.0 86.0 834.5 688.4 146.1
3.900 3 64.390 0.61 1.39 225.0 86.0 86.0 794.2 712.2 82.0
3.860 4 68.250 0.59 1.35 225.0 86.0 86.0 610.8 610.0 0.8
3.810 5 72.060 0.56 1.28 225.0 86.0 86.0 831.9 809.2 22.7
3.700 6 75.760 0.52 1.19 225.0 86.0 86.0 0.0
3.570 7 79.330 0.64 1.46 225.0 86.0 86.0
3.960 8 83.290 0.60 1.37 225.0 86.0 86.0 Isokinetics 100.8
3.840 9 87.130 0.59 1.35 225.0 86.0 86.0 Test Date 6/13/2024
3.800 10 90.930 0.57 1.30 225.0 86.0 86.0 Start Time enter
3.740 11 94.670 0.55 1.26 225.0 87.0 87.0 End Time enter
3.670 12 98.340 0.53 1.21 225.0 87.0 87.0
3.610 13 101.950 0.62 1.42 224.0 87.0 87.0
3.910 14 105.860 0.60 1.37 224.0 87.0 87.0
3.850 15 109.710 0.57 1.30 224.0 87.0 87.0
3.740 16 113.450 0.55 1.26 224.0 87.0 87.0
3.680 17 117.130 0.52 1.19 224.0 87.0 87.0
3.580 18 120.710 0.48 1.10 224.0 87.0 87.0
3.440 19 124.150 0.62 1.42 224.0 87.0 87.0
3.910 20 128.060 0.60 1.37 224.0 87.0 87.0
3.850 21 131.910 0.59 1.35 224.0 87.0 87.0
3.810 22 135.720 0.56 1.28 224.0 87.0 87.0
3.710 23 139.430 0.52 1.19 224.0 87.0 87.0
3.580 24 143.010 0.50 1.14 224.0 87.0 87.0
3.510 25 146.520
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name Ash Grove - Main Kiln/Raw Mill Off
Company Contact:Cody Watkins
Contact Phone No.[phone]
Source Designation:Main Kiln/Raw Mill Off
Test & Review Dates
Test Date: 6/12/2024
Review Date: 8/21/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/Ton Clinker lbs/hr gr/dscf
0.070
Emission Rates - "Front Half"
lbs/Ton Clinker lbs/hr gr/dscf
0.007 0.7158 0.0006
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
132.00 95.033 0.9990 1.736 0.84 25.03 -0.5 0.313
Contractor Information
Contracting Company: Alliance Source Testing
Contact: Austin Keough
Phone No.: 385-722-6712
Project No.:
1800
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
Ash Grove - Main Kiln/Raw Mill Off
Testing Results Lab Data - grams collected
Test Date 6/12/2024 6/12/2024 6/12/2024 6/12/2024 Lab Data Probe Filter Back 9.8
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.00032 0.00441 0
As ft^2 95.03 95.03 95.03 Run 2 0.00163 0.0025 0
Pbar 25.03 25.03 25.03 Run 3 0.00148 0.00042 0
Pq (static)-0.50 -0.50 -0.50 Run 4
Ps 24.99 24.99 24.99
Avg. Ts F 346.21 380.33 380.67 Front Half Emissions Summary
CO2 - FCO2 13.70 13.60 13.90 Run 1 Run 2 Run 3 Run 4 Avg.
O2 10.20 10.40 10.90 gr./dscf 0.0007 0.0007 0.0003 0.001
N2+C 76.10 76.00 75.20 lbs/hr 0.9355 0.8352 0.3767 0.716
Md 30.60 30.59 30.66 lbs/Ton of Clinke 0.0085 0.0076 0.0034 #VALUE! 0.007
Ms 29.27 29.39 29.36
Y 1.00 1.00 1.00
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 121.15 117.66 119.86 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 250.40 215.50 237.40 gr./dscf 0.0007 0.0007 0.0003 0.0006
AVG. Tm F 77.42 83.46 86.50 lbs/hr 0.9355 0.8352 0.3767 0.7158
Vm std 100.18 96.19 97.44 lbs/MMBtu #DIV/0!
Vw std 11.79 10.14 11.17
Bws 0.11 0.10 0.10
S Bws 1.00 1.00 1.00
Avg. Sqrt
Dlp 0.71 0.71 0.71
Vs 53.66 54.31 54.42 F factor used
scfm wet 167391.51 162527.40 162790.60 1800
acfm 305974.25 309658.03 310282.53
Qsd dscfh 8986255 8821363 8762572
# Sample
Points 24.00 24.00 24.00
Dn 0.313 0.313 0.313
An 5.34E-04 5.34E-04 5.34E-04
Start Time
End Time
Total Test
time 120.00 120.00 120.00
Time @ point 5.00 5.00 5.00
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
Page 1
Run 1
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 6/12/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.03 -0.50 24.99 346.2 13.70 10.20 76.10 30.60 29.274
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 10.6792
0.9990 0.84 121.148 250.40 77.42 100.181 11.786 0.1053 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.712 53.661 167,392 305,974 8.99E+06 24 0.313 120 5.00 2.561250
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 31.489 0.63 3.22 323.0 71.0 71.0 Wt. (Final) Wt. (Initial) lc
2 37.127 0.61 3.09 331.0 72.0 72.0 815.30 678.70 136.6
3 42.650 0.57 2.90 331.0 74.0 74.0 754.10 691.10 63.0
4 48.036 0.49 2.49 334.0 75.0 75.0 615.20 605.30 9.9
5 53.012 0.45 2.28 335.0 75.0 75.0 875.10 834.20 40.9
6 57.758 0.42 2.13 335.0 75.0 75.0 0.0
7 62.382 0.62 3.11 345.0 76.0 76.0
8 67.961 0.60 3.01 346.0 77.0 77.0 Isokinetics 99.2
9 73.447 0.58 2.91 346.0 77.0 77.0 Test Date 6/12/2024
10 78.840 0.51 2.56 347.0 78.0 78.0 Start Time enter enter
11 83.884 0.45 2.26 348.0 78.0 78.0 End Time enter
12 88.657 0.40 2.00 350.0 78.0 78.0
13 93.134 0.61 3.04 355.0 79.0 79.0
14 98.665 0.59 2.94 355.0 79.0 79.0
15 104.095 0.55 2.74 355.0 79.0 79.0
16 109.345 0.49 2.45 353.0 79.0 79.0
17 114.312 0.44 2.20 353.0 79.0 79.0
18 118.984 0.43 2.15 352.0 79.0 79.0
19 123.645 0.59 2.94 354.0 79.0 79.0
20 129.112 0.54 2.69 354.0 79.0 79.0
21 134.280 0.47 2.36 351.0 80.0 80.0
22 139.176 0.43 2.15 352.0 80.0 80.0
23 143.841 0.40 2.00 352.0 80.0 80.0
24 148.299 0.37 1.85 352.0 80.0 80.0
25 152.637
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Run 2
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.03 -0.50 24.99 380 13.60 10.40 76.00 30.59 29.39
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 16.4899
0.9990 0.84 117.662 215.50 83 96.186 10.144 0.0954 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.707 54.31 162,527 309,658 8.82E+06 24 0.313 120 5.00 2.45
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 53.196 0.62 3.02 378.0 81.0 81.0 Wt. (Final) Wt. (Initial) lc
2 58.715 0.58 2.82 380.0 82.0 82.0 769.20 628.50 140.7
3 64.038 0.53 2.58 380.0 82.0 82.0 739.30 709.20 30.1
4 69.145 0.49 2.38 380.0 82.0 82.0 564.30 562.10 2.2
5 74.046 0.45 2.19 380.0 83.0 83.0 897.30 854.80 42.5
6 78.732 0.40 1.98 380.0 83.0 83.0 0.0
7 83.188 0.59 2.87 380.0 83.0 83.0
8 88.178 0.56 2.73 380.0 83.0 83.0 Isokinetics 97.0
9 93.835 0.54 2.63 380.0 83.0 83.0 Test Date 6/12/2024
10 98.990 0.48 2.34 380.0 83.0 83.0 Start Time enter
11 103.850 0.42 2.05 380.0 83.0 83.0 End Time enter
12 108.375 0.39 1.90 380.0 83.0 83.0
13 112.766 0.61 2.97 381.0 83.0 83.0
14 118.241 0.59 2.87 380.0 83.0 83.0
15 123.619 0.55 2.68 380.0 84.0 84.0
16 128.846 0.51 2.49 380.0 84.0 84.0
17 133.865 0.45 2.19 382.0 84.0 84.0
18 138.553 0.40 1.95 381.0 84.0 84.0
19 143.015 0.61 2.98 381.0 85.0 85.0
20 148.505 0.57 2.79 380.0 85.0 85.0
21 153.836 0.49 2.40 380.0 85.0 85.0
22 158.778 0.44 2.15 382.0 85.0 85.0
23 163.447 0.41 2.00 382.0 85.0 85.0
24 167.954 0.39 1.91 381.0 85.0 85.0
25 171.352
26
27
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Page 1
Run 3
Ash Grove - Main Kiln/Raw Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.03 -0.50 24.99 381 13.90 10.90 75.20 30.66 29.36
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 16.5569
0.9990 0.84 119.860 237.40 87 97.443 11.174 0.1029 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.708 54.42 162,791 310,283 8.76E+06 24 0.313 120 5.00 2.47
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 71.621 0.60 2.93 381.0 85.0 85.0 Wt. (Final) Wt. (Initial) lc
2 77.081 0.58 2.83 381.0 85.0 85.0 571.5 418.2 153.3
3 82.450 0.51 2.49 381.0 85.0 85.0 783.1 741.7 41.4
4 87.465 0.45 2.20 380.0 85.0 85.0 761.4 747.7 13.7
5 92.167 0.40 1.96 380.0 85.0 85.0 750.7 721.7 29.0
6 96.640 0.38 1.86 380.0 85.0 85.0 0.0
7 100.960 0.59 2.88 380.0 85.0 85.0
8 106.378 0.56 2.74 380.0 85.0 85.0 Isokinetics 98.9
9 111.646 0.54 2.64 381.0 86.0 86.0 Test Date 6/12/2024
10 116.826 0.48 2.35 382.0 86.0 86.0 Start Time enter
11 121.687 0.45 2.20 380.0 86.0 86.0 End Time enter
12 126.439 0.40 1.96 380.0 86.0 86.0
13 130.880 0.62 3.04 381.0 87.0 87.0
14 136.451 0.61 2.99 381.0 87.0 87.0
15 141.966 0.57 2.79 381.0 87.0 87.0
16 147.278 0.49 2.40 382.0 87.0 87.0
17 152.218 0.45 2.21 382.0 88.0 88.0
18 156.982 0.40 1.96 382.0 88.0 88.0
19 161.433 0.60 2.95 380.0 88.0 88.0
20 166.926 0.58 2.85 380.0 88.0 88.0
21 172.318 0.51 2.51 380.0 88.0 88.0
22 177.352 0.48 2.37 381.0 88.0 88.0
23 182.275 0.45 2.21 380.0 88.0 88.0
24 187.004 0.40 1.97 380.0 88.0 88.0
25 191.481
26
27
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29
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name Ash Grove - Coal Mill Raw Mill On
Company Contact:Cody Watkins
Contact Phone No.435-857-1283
Source Designation:Coal Mill Raw Mill On
Test & Review Dates
Test Date: 6/13/2024
Review Date: 9/19/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/Ton Clinker lbs/hr gr/dscf
0.070 10.000
Emission Rates - "Front Half"
lbs/Ton Clinker lbs/hr gr/dscf
0.006 0.6342 0.0063
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
29.00 4.587 0.9880 1.703 0.84 25.03 -0.5 0.238
Contractor Information
Contracting Company: Mostardi Platt
Contact: Mike Lipinski
Phone No.: 630-9210093-
Project No.:
1800
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
Ash Grove - Coal Mill Raw Mill On
Testing Results Lab Data - grams collected
Test Date 6/13/2024 6/13/2024 6/13/2024 6/13/2024 Lab Data Probe Filter Back 9.8
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.00585 0.0331 0
As ft^2 4.59 4.59 4.59 4.59 Run 2 0.00558 0.03351 0
Pbar 25.03 25.03 25.03 25.03 Run 3 0.00356 0.02282 0
Pq (static)-0.50 -0.50 -0.50 -0.50 Run 4 0.00503 0.04536
Ps 24.99 24.99 24.99 24.99
Avg. Ts F 163.25 162.96 163.96 164.08 Front Half Emissions Summary
CO2 - FCO2 7.60 6.70 6.70 6.20 Run 1 Run 2 Run 3 Run 4 Avg.
O2 16.50 16.90 16.90 16.90 gr./dscf 0.0065 0.0064 0.0043 0.0082 0.006
N2+C 75.90 76.40 76.40 76.90 lbs/hr 0.6435 0.6388 0.4309 0.8237 0.634
Md 29.88 29.75 29.75 29.67 lbs/Ton of Clinke 0.0060 0.0059 0.0040 0.0076 0.006
Ms 28.79 28.74 28.74 28.66
Y 0.99 0.99 0.99 0.99
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 118.18 121.91 120.25 119.15 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 197.90 188.90 187.80 190.00 gr./dscf 0.0065 0.0064 0.0043 0.0082 0.0063
AVG. Tm F 98.67 105.08 99.08 94.58 lbs/hr 0.6435 0.6388 0.4309 0.8237 0.6342
Vm std 92.90 94.76 94.47 94.37 lbs/MMBtu #DIV/0!
Vw std 9.32 8.89 8.84 8.94
Bws 0.09 0.09 0.09 0.09
S Bws 0.42 0.41 0.42 0.43
Avg. Sqrt
Dlp 0.98 0.98 0.98 0.98
Vs 65.54 65.70 65.56 65.62 F factor used
scfm wet 12764.04 12802.51 12754.25 12763.70 1800
acfm 18036.60 18082.49 18043.25 18060.23
Qsd dscfh 696047 702258 699774 699525.6
# Sample
Points 24.00 24.00 24.00 24.00
Dn 0.238 0.238 0.238 0.238
An 3.09E-04 3.09E-04 3.09E-04 3.09E-04
Start Time
End Time
Total Test
time 120.00 120.00 120.00 120.00
Time @ point 5.00 5.00 5.00 5.00
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
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Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
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Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
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Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
Page 1
Run 1
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 163.3 7.60 16.50 75.90 29.88 28.794
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.4176
0.9880 0.84 118.184 197.90 98.67 92.897 9.315 0.0911 0.4176 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.981 65.536 12,764 18,037 6.96047E+05 24 0.238 120 5.00 2.262917
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 6.419 1.00 2.35 162.0 97.0 97.0 Wt. (Final) Wt. (Initial) lc
2 11.420 0.99 2.33 162.0 97.0 97.0 468.50 399.70 68.8
3 16.400 1.00 2.35 162.0 97.0 97.0 739.00 677.70 61.3
4 21.420 0.99 2.33 162.0 97.0 97.0 779.00 745.60 33.4
5 26.400 0.98 2.31 163.0 97.0 97.0 940.90 906.50 34.4
6 31.360 0.97 2.28 163.0 97.0 97.0 0.0
7 36.300 0.96 2.26 163.0 98.0 98.0
8 41.210 0.96 2.26 163.0 98.0 98.0 Isokinetics 99.1
9 46.130 0.94 2.21 164.0 98.0 98.0 Test Date 6/13/2024
10 51.010 0.93 2.19 164.0 98.0 98.0 Start Time enter enter
11 55.820 0.92 2.16 164.0 98.0 98.0 End Time enter
12 60.630 0.92 2.16 164.0 98.0 98.0
13 65.445 1.10 2.59 164.0 99.0 99.0
14 70.700 0.99 2.33 164.0 99.0 99.0
15 75.700 0.99 2.33 164.0 99.0 99.0
16 80.690 0.97 2.28 164.0 99.0 99.0
17 85.640 0.96 2.26 164.0 100.0 100.0
18 90.570 0.96 2.26 164.0 100.0 100.0
19 95.500 0.94 2.21 163.0 100.0 100.0
20 100.380 0.94 2.21 163.0 100.0 100.0
21 105.260 0.93 2.19 163.0 100.0 100.0
22 110.120 0.92 2.16 163.0 100.0 100.0
23 114.950 0.92 2.16 163.0 101.0 101.0
24 119.790 0.91 2.14 163.0 101.0 101.0
25 124.603
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Page 1
Run 2
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 163 6.70 16.90 76.40 29.75 28.74

Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.4147
0.9880 0.84 121.909 188.90 105 94.762 8.892 0.0858 0.4147 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.982 65.70 12,803 18,082 7.02E+05 24 0.238 120 5.00 2.36
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 31.934 1.10 2.68 163.0 104.0 104.0 Wt. (Final) Wt. (Initial) lc
2 37.340 1.10 2.68 163.0 104.0 104.0 801.80 737.00 64.8
3 42.750 0.99 2.42 163.0 104.0 104.0 766.30 705.60 60.7
4 47.890 0.98 2.39 163.0 104.0 104.0 675.30 645.50 29.8
5 53.020 0.97 2.37 163.0 104.0 104.0 901.10 867.50 33.6
6 58.090 0.97 2.37 162.0 104.0 104.0 0.0
7 63.180 0.96 2.34 162.0 105.0 105.0
8 68.250 0.94 2.29 162.0 105.0 105.0 Isokinetics 100.2
9 73.270 0.94 2.29 162.0 105.0 105.0 Test Date 6/13/2024
10 78.290 0.92 2.24 162.0 105.0 105.0 Start Time enter
11 83.150 0.91 2.22 162.0 105.0 105.0 End Time enter
12 88.200 0.91 2.22 162.0 106.0 106.0
13 93.151 1.00 2.44 163.0 106.0 106.0
14 98.320 0.99 2.42 163.0 106.0 106.0
15 103.480 0.99 2.42 163.0 106.0 106.0
16 108.630 0.98 2.39 163.0 106.0 106.0
17 113.76 0.97 2.37 163.0 106.0 106.0
18 118.870 0.97 2.37 163.0 106.0 106.0
19 123.970 0.95 2.32 164.0 106.0 106.0
20 129.020 0.95 2.32 164.0 105.0 105.0
21 134.060 0.94 2.29 164.0 105.0 105.0
22 139.070 0.92 2.24 164.0 105.0 105.0
23 144.030 0.92 2.24 164.0 105.0 105.0
24 149.010 0.91 2.22 164.0 105.0 105.0
25 153.923
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Page 1
Run 3
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 164 6.70 16.90 76.40 29.75 28.74
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.4246
0.9880 0.84 120.245 187.80 99 94.468 8.840 0.0856 0.4246 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.980 65.56 12,754 18,043 7.00E+05 24 0.238 120 5.00 2.34
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 55.062 1.00 2.44 164.0 100.0 100.0 Wt. (Final) Wt. (Initial) lc
2 60.170 1.00 2.44 165.0 100.0 100.0 823.8 758.8 65.0
3 65.290 0.98 2.39 165.0 100.0 100.0 770.8 711.3 59.5
4 70.360 0.98 2.39 165.0 100.0 100.0 666.7 635.3 31.4
5 75.430 0.97 2.37 165.0 100.0 100.0 903.0 871.1 31.9
6 80.470 0.97 2.37 165.0 100.0 100.0
7 85.510 0.95 2.32 165.0 100.0 100.0
8 90.500 0.95 2.32 165.0 99.0 99.0 Isokinetics 100.3
9 95.480 0.93 2.27 165.0 99.0 99.0 Test Date 6/13/2024
10 100.410 0.93 2.27 164.0 99.0 99.0 Start Time enter
11 105.340 0.91 2.22 164.0 99.0 99.0 End Time enter
12 110.220 0.91 2.22 164.0 99.0 99.0
13 115.105 1.10 2.68 164.0 99.0 99.0
14 120.450 1.00 2.44 164.0 99.0 99.0
15 125.570 0.98 2.39 164.0 98.0 98.0
16 130.620 0.97 2.37 164.0 98.0 98.0
17 135.650 0.97 2.37 163.0 98.0 98.0
18 140.680 0.96 2.34 163.0 98.0 98.0
19 145.690 0.94 2.29 163.0 98.0 98.0
20 150.640 0.94 2.29 163.0 99.0 99.0
21 155.610 0.93 2.27 163.0 99.0 99.0
22 160.540 0.93 2.27 163.0 99.0 99.0
23 165.480 0.92 2.24 163.0 99.0 99.0
24 170.390 0.92 2.24 162.0 99.0 99.0
25 175.307
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Page 1
Run 4
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 164 6.20 16.90 76.90 29.67 28.66
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.4259
0.9880 0.84 119.147 190.00 95 94.365 8.943 0.0866 0.4259 0.999
Avg. Sqrt Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.979 65.62 12,764 18,060 7.00E+05 24 0.238 120 5.00 2.34
TRUE
Mv@ Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 77.465 1.100 2.68 165.0 96.0 96.0 Wt. (Final) Wt. (Initial) lc
5.315 2 82.780 0.99 2.42 165.0 96.0 96.0 829.8 763.6 66.2
5.070 3 87.850 0.98 2.39 165.0 96.0 96.0 775.8 715.1 60.7
5.020 4 92.870 0.98 2.39 165.0 96.0 96.0 670.3 640.9 29.4
5.030 5 97.900 0.96 2.34 165.0 96.0 96.0 911.4 877.7 33.7
4.980 6 102.880 0.96 2.34 165.0 96.0 96.0 0.0
4.980 7 107.860 0.95 2.32 165.0 95.0 95.0
4.950 8 112.810 0.95 2.32 165.0 95.0 95.0 Isokinetics #REF!
4.940 9 117.750 0.93 2.27 165.0 95.0 95.0 Test Date 6/13/2024
4.900 10 122.650 0.92 2.24 164.0 95.0 95.0 Start Time enter
4.870 11 127.520 0.91 2.22 164.0 95.0 95.0 End Time enter
4.840 12 132.360 0.92 2.24 164.0 95.0 95.0
4.877 13 137.237 0.99 2.42 164.0 94.0 94.0
5.033 14 142.270 0.99 2.42 164.0 94.0 94.0
5.040 15 147.310 0.98 2.39 164.0 94.0 94.0
5.020 16 152.330 0.98 2.39 164.0 94.0 94.0
5.010 17 157.340 0.96 2.34 164.0 93.0 93.0
4.960 18 162.300 0.96 2.34 163.0 93.0 93.0
4.960 19 167.260 0.95 2.32 163.0 93.0 93.0
4.940 20 172.200 0.94 2.39 163.0 93.0 93.0
4.910 21 177.110 0.95 2.32 163.0 93.0 93.0
4.930 22 182.040 0.93 2.27 163.0 93.0 93.0
4.890 23 186.930 0.92 2.24 163.0 95.0 95.0
4.850 24 191.780 0.91 2.22 163.0 95.0 95.0
4.832 25 196.612
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name Ash Grove - Coal Mill Raw Mill Off
Company Contact:Cody Watkins
Contact Phone No.435-857-1283
Source Designation:Coal Mill Raw Mill Off
Test & Review Dates
Test Date: 6/12/2024
Review Date: 9/15/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/Ton Clinker lbs/hr gr/dscf
0.070 10.000
Emission Rates - "Front Half"
lbs/Ton Clinker lbs/hr gr/dscf
0.005 0.6366 0.0064
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
29.00 4.587 0.9880 1.703 0.84 25.03 -0.5 0.238
Contractor Information
Contracting Company: Mostardi Platt
Contact: Mike Lipinski
Phone No.: 630-9210093-
Project No.:
1800
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
Ash Grove - Coal Mill Raw Mill Off
Testing Results Lab Data - grams collected
Test Date 6/12/2024 6/12/2024 6/12/2024 6/12/2024 Lab Data Probe Filter Back 9.8
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.01154 0.0263 0
As ft^2 4.59 4.59 4.59 Run 2 0.00456 0.03421 0
Pbar 25.03 25.03 25.03 Run 3 0.00766 0.03294 0
Pq (static)-0.50 -0.50 -0.50 Run 4
Ps 24.99 24.99 24.99
Avg. Ts F 157.71 163.08 157.50 Front Half Emissions Summary
CO2 - FCO2 7.60 6.70 6.70 Run 1 Run 2 Run 3 Run 4 Avg.
O2 16.50 16.90 16.90 gr./dscf 0.0062 0.0064 0.0067 0.006
N2+C 75.90 76.40 76.40 lbs/hr 0.6184 0.6337 0.6578 0.637
Md 29.88 29.75 29.75 lbs/Ton of Clinke 0.0052 0.0055 0.0057 #VALUE! 0.005
Ms 28.66 28.53 28.35
Y 0.99 0.99 0.99
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 117.20 117.75 121.17 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 227.20 229.30 268.80 gr./dscf 0.0062 0.0064 0.0067 0.0064
AVG. Tm F 89.75 91.67 108.75 lbs/hr 0.6184 0.6337 0.6578 0.6366
Vm std 93.60 93.72 93.54 lbs/MMBtu #DIV/0!
Vw std 10.69 10.79 12.65
Bws 0.10 0.10 0.12
S Bws 0.37 0.42 0.36
Avg. Sqrt
Dlp 0.98 0.99 0.99
Vs 65.56 66.29 66.16 F factor used
scfm wet 12883.59 12913.45 13005.30 1800
acfm 18043.65 18242.85 18207.96
Qsd dscfh 693753 694796 687350
# Sample
Points 24.00 24.00 24.00
Dn 0.238 0.238 0.238
An 3.09E-04 3.09E-04 3.09E-04
Start Time
End Time
Total Test
time 120.00 120.00 120.00
Time @ point 5.00 5.00 5.00
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
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Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
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Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
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Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
Page 1
Run 1
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 6/12/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 157.7 7.60 16.50 75.90 29.88 28.658
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.3660
0.9880 0.84 117.202 227.20 89.75 93.604 10.694 0.1025 0.3660 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.983 65.562 12,884 18,044 6.94E+05 24 0.238 120 5.00 2.206667
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 47.135 1.00 2.28 157.0 86.0 86.0 Wt. (Final) Wt. (Initial) lc
2 52.060 1.00 2.28 157.0 87.0 87.0 757.00 632.70 124.3
3 57.010 0.99 2.26 157.0 87.0 87.0 725.60 677.70 47.9
4 61.930 0.98 2.24 157.0 88.0 88.0 665.50 652.10 13.4
5 66.840 0.98 2.24 158.0 88.0 88.0 887.50 845.90 41.6
6 71.740 0.96 2.19 158.0 89.0 89.0 0.0
7 76.600 0.96 2.19 159.0 89.0 89.0
8 81.460 0.95 2.17 159.0 90.0 90.0 Isokinetics 100.2
9 86.300 0.93 2.12 159.0 90.0 90.0 Test Date 6/12/2024
10 91.090 0.93 2.12 158.0 91.0 91.0 Start Time enter enter
11 95.890 0.92 2.10 158.0 91.0 91.0 End Time enter
12 100.660 0.91 2.08 158.0 92.0 92.0
13 105.428 1.10 2.51 158.0 91.0 91.0
14 110.640 1.10 2.51 158.0 91.0 91.0
15 115.860 0.99 2.26 158.0 91.0 91.0
16 120.810 0.98 2.24 158.0 91.0 91.0
17 125.740 0.98 2.24 158.0 91.0 91.0
18 130.670 0.96 2.19 158.0 91.0 91.0
19 135.550 0.95 2.17 157.0 90.0 90.0
20 140.400 0.95 2.17 157.0 90.0 90.0
21 145.250 0.93 2.12 157.0 90.0 90.0
22 150.040 0.92 2.10 157.0 90.0 90.0
23 154.820 0.92 2.10 157.0 90.0 90.0
24 159.590 0.92 2.08 157.0 90.0 90.0
25 164.337
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Run 2
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 163 6.70 16.90 76.40 29.75 28.53

Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.4159
0.9880 0.84 117.753 229.30 92 93.725 10.793 0.1033 0.4159 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.988 66.29 12,913 18,243 6.95E+05 24 0.238 120 5.00 2.24
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 65.215 1.00 2.51 163.0 89.0 89.0 Wt. (Final) Wt. (Initial) lc
2 70.420 1.00 2.28 163.0 89.0 89.0 887.40 757.00 130.4
3 75.350 1.00 2.28 163.0 90.0 90.0 777.00 725.60 51.4
4 80.310 1.00 2.28 163.0 90.0 90.0 675.30 665.50 9.8
5 85.240 0.99 2.26 163.0 90.0 90.0 925.20 887.50 37.7
6 90.180 0.97 2.21 163.0 91.0 91.0 0.0
7 95.110 0.97 2.21 163.0 91.0 91.0
8 99.950 0.95 2.17 164.0 91.0 91.0 Isokinetics 100.2
9 104.770 0.95 2.17 164.0 92.0 92.0 Test Date 6/12/2024
10 109.620 0.94 2.14 164.0 92.0 92.0 Start Time enter
11 114.450 0.92 2.10 164.0 92.0 92.0 End Time enter
12 119.200 0.92 2.10 164.0 92.0 92.0
13 123.974 1.00 2.28 164.0 91.0 91.0
14 128.940 1.10 2.51 164.0 92.0 92.0
15 134.150 1.10 2.51 164.0 92.0 92.0
16 139.37 1.00 2.28 163.0 92.0 92.0
17 144.350 1.00 2.28 163.0 93.0 93.0
18 149.280 0.99 2.26 163.0 93.0 93.0
19 154.250 0.97 2.21 162.0 93.0 93.0
20 159.160 0.97 2.21 162.0 93.0 93.0
21 164.140 0.95 2.17 162.0 93.0 93.0
22 168.990 0.94 2.14 162.0 93.0 93.0
23 173.780 0.90 2.05 162.0 93.0 93.0
24 178.470 0.89 2.03 162.0 93.0 93.0
25 183.198
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Run 3
Ash Grove - Coal Mill Raw M Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
4.59 25.03 -0.50 24.99 158 6.70 16.90 76.40 29.75 28.35
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.3642
0.9880 0.84 121.170 268.80 109 93.544 12.652 0.1191 0.3642 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.987 66.16 13,005 18,208 6.87E+05 24 0.238 120 5.00 2.22
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 85.019 1.00 2.28 164.0 111.0 111.0 Wt. (Final) Wt. (Initial) lc
2 90.140 1.10 2.51 164.0 111.0 111.0 660.4 517.9 142.5
3 95.530 0.99 2.26 164.0 111.0 111.0 644.5 643.2 1.3
4 100.640 0.99 2.26 164.0 111.0 111.0 750.4 750.4 0.0
5 105.750 0.97 2.21 164.0 111.0 111.0 925.0 800.0 125.0
6 110.800 0.96 2.19 163.0 110.0 110.0
7 115.830 0.97 2.21 163.0 110.0 110.0
8 120.880 0.96 2.19 163.0 110.0 110.0 Isokinetics 101.1
9 125.910 0.95 2.17 163.0 109.0 109.0 Test Date 6/12/2024
10 130.900 0.93 2.12 163.0 109.0 109.0 Start Time enter
11 135.840 0.91 2.08 16.0 109.0 109.0 End Time enter
12 140.760 0.91 2.08 162.0 109.0 109.0
13 145.623 1.10 2.51 163.0 108.0 108.0
14 150.970 1.10 2.51 163.0 108.0 108.0
15 156.330 1.00 2.28 163.0 108.0 108.0
16 161.340 0.98 2.24 163.0 108.0 108.0
17 166.510 0.98 2.24 164.0 108.0 108.0
18 171.560 0.96 2.19 164.0 107.0 107.0
19 176.560 0.96 2.19 164.0 107.0 107.0
20 181.560 0.95 2.17 164.0 107.0 107.0
21 186.530 0.94 2.14 164.0 107.0 107.0
22 191.470 0.94 2.14 165.0 107.0 107.0
23 196.410 0.92 2.10 165.0 107.0 107.0
24 201.300 0.92 2.10 165.0 107.0 107.0
25 206.189
26
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name Ash Grove Cement - Clinker Cooler
Company Contact:Cody Watkins
Contact Phone No.435-857-1283
Source Designation:Clinker Cooler
Test & Review Dates
Test Date: 6/13/2024
Review Date: 8/21/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/Ton Clinker lbs/hr gr/dscf
0.070
Emission Rates - "Front Half"
lbs/Ton Clinker lbs/hr gr/dscf
0.002 0.2521 0.0004
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
105.00 60.132 0.9900 1.736 0.84 25.08 -0.4 0.311
Contractor Information
Contracting Company: Mostardi Platt
Contact: Mike Lipinski
Phone No.: 630-9210093-
Project No.:
1800
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
Ash Grove Cement - Clinker Cooler
Testing Results Lab Data - grams collected
Test Date 6/13/2024 6/13/2024 6/13/2024 6/13/2024 Lab Data Probe Filter Back 9.8
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.00025 0.00054 0
As ft^2 60.13 60.13 60.13 Run 2 0.00035 0.00045 0
Pbar 25.08 25.08 25.08 Run 3 0.00351 0.00101 0
Pq (static)-0.40 -0.40 -0.40 Run 4
Ps 25.05 25.05 25.05
Avg. Ts F 232.71 237.46 240.00 Front Half Emissions Summary
CO2 - FCO2 0.00 0.00 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
O2 20.90 20.90 20.90 gr./dscf 0.0001 0.0001 0.0008 0.000
N2+C 79.10 79.10 79.10 lbs/hr 0.0976 0.0996 0.5590 0.252
Md 28.84 28.84 28.84 lbs/Ton of Clinker 0.0008 0.0009 0.0048 #VALUE! 0.002
Ms 28.64 28.67 28.65
Y 0.99 0.99 0.99
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 111.81 111.25 111.19 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 36.10 28.40 32.60 gr./dscf 0.0001 0.0001 0.0008 0.0004
AVG. Tm F 81.88 95.50 102.00 lbs/hr 0.0976 0.0996 0.5590 0.2521
Vm std 90.95 88.26 87.18 lbs/MMBtu #DIV/0!
Vw std 1.70 1.34 1.53
Bws 0.02 0.01 0.02
S Bws 1.00 1.00 1.00
Avg. Sqrt Dlp 0.53 0.52 0.51
Vs 37.58 36.88 36.40 F factor used
scfm wet 86521.80 84344.79 82929.92 1800
acfm 135576.59 133071.56 131316.11
Qsd dscfh 5096093 4985179 4889730
# Sample
Points 24.00 24.00 24.00
Dn 0.311 0.311 0.311
An 5.28E-04 5.28E-04 5.28E-04
Start Time
End Time
Total Test
time 120.00 120.00 120.00
Time @ point 5.00 5.00 5.00
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
%
I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
Page 1
Run 1
Ash Grove Cement - Clinker Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
60.13 25.08 -0.40 25.05 232.7 0.00 20.90 79.10 28.84 28.637
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.7843
0.9900 0.84 111.808 36.10 81.88 90.946 1.699 0.0183 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.533 37.577 86,522 135,577 5.10E+06 24 0.311 120 5.00 2.165417
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 93.407 0.32 2.42 230.0 77.0 77.0 Wt. (Final) Wt. (Initial) lc
2 98.331 0.30 2.27 230.0 77.0 77.0 748.90 734.00 14.9
3 103.090 0.29 2.19 232.0 77.0 77.0 737.80 734.90 2.9
4 107.761 0.27 2.04 232.0 77.0 77.0 667.90 667.20 0.7
5 112.249 0.25 1.89 232.0 78.0 78.0 806.30 788.70 17.6
6 116.614 0.24 1.81 232.0 78.0 78.0 0.0
7 120.872 0.35 2.66 231.0 79.0 79.0
8 126.017 0.32 2.43 231.0 79.0 79.0 Isokinetics 101.8
9 130.946 0.30 2.28 231.0 79.0 79.0 Test Date 6/13/2024
10 135.719 0.29 2.20 231.0 80.0 80.0 Start Time enter enter
11 140.440 0.25 1.90 231.0 80.0 80.0 End Time enter
12 144.784 0.22 1.68 231.0 81.0 81.0
13 148.887 0.34 2.59 232.0 82.0 82.0
14 153.982 0.32 2.44 232.0 82.0 82.0
15 158.955 0.29 2.21 234.0 83.0 83.0
16 163.672 0.30 2.29 234.0 84.0 84.0
17 168.459 0.27 2.06 234.0 84.0 84.0
18 173.018 0.27 2.06 235.0 85.0 85.0
19 177.583 0.31 2.36 235.0 85.0 85.0
20 182.484 0.30 2.29 235.0 86.0 86.0
21 187.285 0.27 2.07 235.0 87.0 87.0
22 191.887 0.29 2.22 235.0 88.0 88.0
23 196.624 0.24 1.84 235.0 88.0 88.0
24 200.971 0.23 1.77 235.0 89.0 89.0
25 205.215
26
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Page 1
Run 2
Ash Grove Cement - Clinker Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
60.13 25.08 -0.40 25.05 237 0.00 20.90 79.10 28.84 28.67

Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.9479
0.9900 0.84 111.247 28.40 96 88.257 1.337 0.0149 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.521 36.88 84,345 133,072 4.99E+06 24 0.311 120 5.00 2.11
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 6.491 0.34 2.62 238.0 92.0 92.0 Wt. (Final) Wt. (Initial) lc
2 11.678 0.32 2.46 238.0 92.0 92.0 759.20 748.50 10.7
3 16.681 0.29 2.23 238.0 92.0 92.0 756.90 750.20 6.7
4 21.482 0.28 2.16 238.0 93.0 93.0 746.80 746.00 0.8
5 26.189 0.23 1.77 238.0 93.0 93.0 830.70 820.50 10.2
6 30.455 0.22 1.70 238.0 93.0 93.0 0.0
7 34.627 0.33 2.55 238.0 95.0 95.0
8 39.768 0.31 2.40 237.0 95.0 95.0 Isokinetics 100.9
9 44.736 0.30 2.32 237.0 95.0 95.0 Test Date 6/13/2024
10 49.629 0.26 2.01 238.0 95.0 95.0 Start Time enter
11 54.184 0.23 1.78 237.0 95.0 95.0 End Time enter
12 58.445 0.21 1.63 237.0 96.0 96.0
13 62.546 0.31 2.41 237.0 96.0 96.0
14 67.539 0.30 2.33 237.0 96.0 96.0
15 72.441 0.27 2.09 237.0 96.0 96.0
16 77.091 0.29 2.25 237.0 96.0 96.0
17 81.911 0.24 1.86 237.0 97.0 97.0
18 86.283 0.23 1.79 237.0 97.0 97.0
19 90.583 0.30 2.33 238.0 98.0 98.0
20 95.489 0.29 2.25 238.0 98.0 98.0
21 100.342 0.27 2.10 237.0 98.0 98.0
22 104.989 0.25 1.94 238.0 98.0 98.0
23 109.497 0.24 1.87 237.0 98.0 98.0
24 113.877 0.24 1.87 237.0 98.0 98.0
25 118.297
26
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Page 1
Run 3
Ash Grove Cement - Clinker Flow & Moisture Test Date 5/13/2009
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
60.13 25.08 -0.40 25.05 240 0.00 20.90 79.10 28.84 28.65
Brother Taggart
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 2.0404
0.9900 0.84 111.192 32.60 102 87.181 1.534 0.0173 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
0.513 36.40 82,930 131,316 4.89E+06 24 0.311 120 5.00 2.07
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 19.745 0.31 2.41 240.0 100.0 100.0 Wt. (Final) Wt. (Initial) lc
2 24.743 0.30 2.33 240.0 100.0 100.0 768.6 755.3 13.3
3 29.670 0.28 2.18 240.0 100.0 100.0 747.9 743.7 4.2
4 34.449 0.27 2.10 240.0 100.0 100.0 782.5 780.0 2.5
5 39.123 0.24 1.87 240.0 100.0 100.0 848.7 836.1 12.6
6 43.509 0.23 1.79 240.0 100.0 100.0
7 47.843 0.30 2.34 241.0 101.0 101.0
8 52.765 0.28 2.18 241.0 101.0 101.0 Isokinetics 101.7
9 57.549 0.27 2.10 241.0 101.0 101.0 Test Date 6/13/2024
10 62.228 0.24 1.87 241.0 101.0 101.0 Start Time enter
11 66.639 0.25 1.95 241.0 101.0 101.0 End Time enter
12 71.121 0.21 1.64 241.0 102.0 102.0
13 75.255 0.33 2.58 239.0 102.0 102.0
14 80.434 0.30 2.35 239.0 102.0 102.0
15 85.382 0.28 2.19 239.0 102.0 102.0
16 90.162 0.27 2.12 239.0 103.0 103.0
17 94.884 0.23 1.80 239.0 103.0 103.0
18 99.224 0.21 1.65 239.0 103.0 103.0
19 103.371 0.31 2.42 240.0 103.0 103.0
20 108.416 0.30 2.35 240.0 104.0 104.0
21 113.370 0.27 2.12 240.0 104.0 104.0
22 118.065 0.25 1.96 240.0 105.0 105.0
23 122.602 0.22 1.73 240.0 105.0 105.0
24 126.870 0.20 1.57 240.0 105.0 105.0
25 130.937
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Page 1
Source
Reference Methods 30B
Source Information
Company Name Ash Grove Cement
Company Contact:Cody Watkins
Contact Phone No.[phone]
Stack Designation:Coal Mill/Mill on Hg
Test & Review Dates
Test Date:6/13/2024
Review Date: 11/6/2024
Observer:Unobserved
Reviewer:Robert Sirrine
Emission Limits Emission Rates
Hg Hg
lb/MM tons clinker 55.0 0.30
µg/dscm 0.85
lb/MMBtu 0.000008579
% Reduction
% O2 Correction as a whole No.0.0
Test Information
Equivalent Diameter
(in.)As ft^2 Train I.D.Y ∆H @ Cp Pbar Pq (static)
MDL
ng Hg
29.00 4.588 Train "A"1.0070 0.84 24.08 -0.5 0.000001
Train "B"0.9760
Electrical Output of the Unit Heat Input
Average. MW
Load
Max Elecctrical
Output (MEO)
MW Load
Contractor Information
Contact:Mike Lipinski
Contracting Company:Mostardi Platt
Address:Henderson NV
Phone No.:630-993-2100
Project No.:
9780

Tabs Are S
Round
Maximum Annual Electrical
Output
GW-hr
MHI Maximum Heat
Input of the unit
MMBTU/hr
Maximum annual
Potential Heat Input
TBTU/yr
Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Method 19 - F factors for Coal, Oil, and Gas
Fd Fw Fc
dscf/mmBtu wscf/mmBtu dscf/mmBtu
Diluent
F factor used
O2
CO2
Anthracite 2
Bituminous 2
Lignite
Natural
Propane
Butane
10100COAL
OIL
GAS
9780
9860
9190
8710
8710
8710
10540
10640
11950
10320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
Page 1
Memo&Notes
RM 30B
Average => 0.7744 0.8485 5.29E-11 0.298721 6.07 8.58E-06 7.78960
Run Validation Run Date µg/wscm µg/dscm lbs/dscm b/MM Tons Clin E lb/yr %CO2
Fc
dscf/MMBTU lbs/MMBtu lbs/Tbtu
Run Valid Run 1 6/13/24 0.7749 0.85247 5.319E-11 0.294605706 #DIV/0!5.90 9780 8.8176E-06 8.0152
Run Valid Run 2 6/13/24 0.7083 0.77496 4.836E-11 0.276232095 #DIV/0!6.10 9780 8.5285E-06 7.0862
Run Valid Run 3 6/13/24 0.8399 0.91796 5.728E-11 0.32532486 #DIV/0!6.20 9780 8.3910E-06 8.2675
Run 4
Run 5
Run 6
Run 7
Run 8
Run 9
Run 10
Run 11
Run 12
Page 1
RM 30B
Cal. Curve
used:Polynomial MDL = 0.0000 Average Spike Recovery = 94.1%
Ash Grove Cement
Coal Mill/Mill on Hg Nunber of Runs Used for Spike Recovery Calculation 3
Cal.
Curve
Used Train
ID
Start
Date
Start
Time
End
Date
End
Time
Trap
ID
Section 1
Area Count
Section 1
Mass
(ng)
Section 2
Area Count
Section 2
Mass (ng)
Total
Mass (ng)
(Section 2)
Breakthrough
(%)
Spike
Mass
(ng)
Field (Spike)
Recovery
"R"
Between
85% & 115%
1A OLC189974 5,300.00 42.100 208.00 1.6000 43.700 3.80%
1B OLC701370 17,200.00 136.900 190.00 1.5000 138.400 1.09% 100.00 99.41%
2A OLC607250 5,030.00 40.000 380.00 3.0000 43.000 7.50%
2B OLC701470 16,400.00 130.500 343.00 2.7000 133.200 2.06% 100.00 86.99%
3A OLC667965 5,900.00 46.900 158.00 1.2000 48.100 2.55%
3B OLC701305 17,100.00 136.100 410.00 3.2000 139.300 2.35% 100.00 96.04%
4A4B
5A
5B
6A6B
7A
7B
8A
8B
9A
9B
10A
10B
11A
11B
12A
12B
Spike recovery Specification between 85 - 115%
3-Sets of Spike Recoveries Requiered
8:30
9:45 10:45
12:10 13:10
6/13/24
6/13/24
6/13/24
6/13/24
6/13/24
6/13/24
7:301
1
1
3
3
Page 1
RM 30B
Coal Mill/Mill on H
Cal.
Curve
Used Train
ID
1A
1B
2A
2B
3A
3B
4A4B
5A
5B
6A6B
7A
7B
8A
8B
9A
9B
10A
10B
11A
11B
12A
12B
1
1
1
3
3
RED is "Input Data"
Black is "Calculation"
FALSE
0.5
AGREE
Mosture
(%)
Std Sample Volume (Std
L)
Wet Basis
Concentraion
(µg/m3)
- Spike Mass
Avg. Wet Basis
Concentration
(µg/m3)
(%)
Relative
Deviation
µg/dscm
Dry Basis
Concentration
(µg/dscm)
Avg Dry Basis
Concentration
(µg/dscm)
48.921 0.811988717 0.893277
47.310 0.737805961 0.811668
48.647 0.807901823 0.883919
49.850 0.608722166 0.665998
48.349 0.910287700 0.994850
46.726 0.769582245 0.841073
0.774897339 4.79%0.85247
0.708311995 14.06%0.77496
0.839934973 8.38%0.91796
9.10%
8.60%
8.50%
Page 2
30 Day LEE
Ash Grove Cement 67891011121314151617181920212223
Coal Mill/Mill on Hg
1A 1B 2A 2B 3A 3B 4A 4B 5A 5B 6A 6B 7A 7B 8A 8B 9A 9B
Start Date
Start Time
End Date
End Time
Elapsed Time 0.12 days
Trap ID OLC189974 OLC701370 OLC607250 OLC701470 OLC667965 OLC701305 30-Day Average
0.049 0.047 0.049 0.050 0.048 0.047
42.1 136.9 40 130.5 46.9 136.1
1.6 1.5 3 2.7 1.2 3.23.80% 0.011 7.50% 0.021 2.55% 0.024
100.000 100.000 100.000
0.848
6.24E-115.29E-119780
0.029111111
6.066666667
7.789633333
720460
0.298720887
0
MEO - Maximum Electrical Output of the Unit MW #DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
#DIV/0! #DIV/0! #DIV/0!
0.0 0.0 0.0
3.25E-01
6/13/24
7:30
6/13/24
8:30
1.00 hr
6/13/24
9:45
6/13/24
10:45
1.00 hr
6.24E-11 6.24E-115.73E-11
6/13/24
12:10
6/13/24
13:10
1.00 hr
K Conversion Factor lb-dscm/ug-dscfCd Average Hg Concentration from all traps lb/dscm 6.24E-114.84E-11 6.24E-11 6.24E-11 6.24E-11 6.24E-11
9780 9780
6.24E-115.3194E-11
9780
0
Average CO2vw % from CEM 5.90 6.10 6.20
Bws - Measured Stack Gas Moisture Content- percent 0.091 0.086 0.085 0 0 0 0 0
Fc - Fuel Factor (dscf/MMBTU)
721,380.0 720,600.0 719,400.0
E - Average Hg Emission Rate lb/TBTU 8.0152 7.0862 8.2675
Qh Avg. stack gas Volumetric Flow Rate - wscf per hour
m1 - Hg mass from tube Section 1 nanograms (ng)
m2 - Hg mass from tube Section 2 nanograms (ng)B - % Breakthrough
Ca - Hg Trap A - µg/dscm
Cb - Hg Trap B - µg/dscm
RD - Relative Deviatio - percent
Spike
Cavg - Average Concentration Hg µg/dscm
6.24E-11
8.38%
Vm (std) dscm
4.79% 14.06%
0.893276916
0.811667724
0.883918844
0.665997994
0.994849945
0.841073492
0.852 0.775 0.918
Eyr Average Hg Emission Rate - lb/yr
Mh Average Hg Emission Rate lb/MM Tons Clincker (BWS Needed
MWavg. Average Load
Eho - Average Hg Emissions lb/GW-hr
GWh - Maximum Annual Potential Electical Output GW-hr
Eyr Average Hg Emission Rate - lb/yr
MHI Maximum Heat Input of the Unit MMBTU/hr
HImax Maximum Annual Potential Heat Input TBTU/yr
2.95E-01 2.76E-01
Page 1
Cal Curve 1
MDL Date 2
0.000
Slope
(Calibration
Coeff.)
Intercept R2
R2 must be ≥ 0.99
Coal Mill/Mill on Hg Daily Calibration Coal Calibration
calibration - Section 1 reading within ±10%
Description "Y"
Expected Mass (ng)
"X"
Area Counts Calculated Mass (ng) % Error
Std:25 3300 26.27 5.1%
Std:50 6400 50.95 1.90%
Std:100 12000 95.53 -4.47%
Std:250 33600 267.49 7.00%
Std:500 61700 491.20 -1.76%
Std:
Std:
Std:
Std:
Std:
Std:
Std:
ICVS:100 12200 97.13 -2.87%
Independent Calibration Verification Standard (ICVS) must be ±10% of true value
Section 2 - Response Factor Determination a b c
R2
R2 must be ≥ 0.99
Description Estimated Mass (ng) Area Counts
Response Factor
(ng Hg)0.00E+00 0.007961 0.002 0.997487
Std:25 3300 25.08
Continuing Calibration Verification Standard (CCVS)
Description Expected Mass (ng) Area Counts Calculated Mass (ng) % Error
CCV-Std Run #100 13100 104.29 4.29%
CCV-Std Run #100 13100 104.29 4.29%
CCV-Std Run #100 13400 106.68 6.68%
CCV-Std Run #
CCV-Std Run #
CCV-Std Run #
must be ±10% of true value
11.5 Blanks. The analysis of blanks is optional. The analysis of blanks is useful
to verify the absence of, or an acceptable level of, Hg contamination. Blank levels should
be considered when quantifying low Hg levels and their potential contribution to meeting
the sorbent trap section 2 breakthrough requirements; however, correcting sorbent trap
results for blank levels is prohibited.
Ash Grove Cement
y = 0.008x - 2.7503
R² = 0.9975
0
100
200
300
400
500
600
0 10000 20000 30000 40000 50000 60000 70000
X
-

E
x
p
e
c
t
e
d

M
a
s
s

(
n
g
)
Y- Area Count
Linear Regression Curve
y = 2E-08x2 + 0.0066x + 7.8739
R² = 0.9991
0
100
200
300
400
500
600
0 10000 20000 30000 40000 50000 60000 70000
Hg

M
a
s
s

(
n
g
)

Area Count
Polynomial Curve
Use Polynomial Curve
Use Linera Regression
Page 1
AG RM 25 THC 2024 rev
Compromis
Ash Grove Cement Coal Mill/Raw Mill On
Casey Mueller
435-857-1283Ash Grove Cement
6/13/2024 Tabs Are Shown
11/7/2024
none
Robert Sirrine
Emission Limits Emission Rates
VOC VOC
mg/L gas
24.0 14.18
lbs./hr.
7.00
As ft^2 Y Dl H @ Cp Pbar Pq (static)
Ps
Stack Pressure
4.59 0.9950 1.535 0.84 25.49 -0.9 25.49
Mike Lipinski
Mostardi Platt
7715 Commercial Way, Suite 155, Henderson NV 89102
630-993-2100 Btu/hr Selected
#N/A

Division of Air Quality
Instrumental Reference Methods - Gaseous Measurements
Round
m corrected for %O2
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
Yes
Yes
AG RM 25 THC 2024 rev
Division of Air Quality
NSPS Relative Accuracy Performance Specification Test - CEMS Certification
Ash Grove Cement Coal Mill/Raw Mill On
Ash Grove Cement
Average Emission
Wet
VOC
(Propane)
VOC
(Butane)
VOC
(Ethane)Average % concentration
lbs./hr. 0.19 CO2 O2
ppm corrected for %O2 14.177 6.08 16.93
Run 1
Wet
VOC
(Propane)
VOC
(Butane)
VOC
(Ethane)
Molecular Weight 44.1 58.1 30.1
Qs dscf min 7.074E+03 CO2 O2
ppm corrected for %O2 12.88 5.92 16.99
lbs/hr 0.17 5.89 16.99
Run 2
Wet
VOC
(Propane)
VOC
(Butane)
VOC
(Ethane)
Molecular Weight 44.1 58.1 30.1
Qs dscf min 7.105E+03 CO2 O2
ppm corrected for %O2 14.10 6.11 16.92
lbs/hr 0.19 6.07 16.83
Run 3
Wet
VOC
(Propane)
VOC
(Butane)
VOC
(Ethane)
Molecular Weight 44.1 58.1 30.1
Qs dscf min 7.075E+03 CO2 O2
ppm corrected for %O2 15.58 6.22 16.91
lbs/hr 0.21 6.15 16.75
Corrected Value
Raw Value
mg/Liter of gasoline
Corrected Value
Raw Value
Corrected Value
Raw Value
Wet CEM
Yes
Correct For O2
Yes
State of Utah CalError Page 1
VOC K3
(Propane)O2
Span Value 130.00 Span Value 22.12
Units ppm Units %
Cylinder No.
Expiration
Date Cylinder Value: Response Difference CAL. ERROR Status Cylinder No.
Expiration
Date
Cylinder
Value:Response Difference
CAL. ERROR Status
Zero Gas 0.00 0.00 0.00 0.00%Passed Cal.Zero Gas 0.00 0.00 0.00 0.00%Passed Cal.
Low-level Cal. Gas 10.80 10.20 0.60 0.46%Passed Cal.Mid-level Cal. Gas 11.24 11.20 0.04 0.18%Passed Cal.
Mid-level Cal. Gas 19.82 20.00 0.18 0.14%Passed Cal.High-level Cal. Gas 22.12 22.10 0.02 0.09%Passed Cal.
High-level Cal. Gas 30.17 30.20 0.03 0.02%Passed Cal.
<0.25% of span value Zero Gas 0.00%
<0.10% of span value Zero Gas 0.00%40 to 60% of span value Low-level Cal. Gas 50.8%
25 to 35% of span value Low-level Cal. Gas 8.31%80 to 100% of span value Mid-level Cal. Gas 100.00%
45 to 55% of span value Mid-level Cal. Gas 15.25%
80 to 90% of span value High-level Cal. Gas 23.21%
VOC K4
(Butane)CO2
Span Value Span Value 22.58
Units ppm Units %
Cylinder No.
Expiration
Date Cylinder Value: Response Difference CAL. ERROR Status Cylinder No.
Expiration
Date
Cylinder
Value:Response Difference CAL. ERROR Status
Zero Gas Zero Gas 0.000 0.000 0.00 0.00%Passed Cal.
Low-level Cal. Gas Mid-level Cal. Gas 11.260 11.200 0.06 0.27%Passed Cal.
Mid-level Cal. Gas High-level Cal. Gas 22.580 22.400 0.18 0.80% Passed Cal.
High-level Cal. Gas
<0.25% of span value Zero Gas 0.00%
<0.10% of span value Zero Gas 40 to 60% of span value Low-level Cal. Gas 49.9%
25 to 35% of span value Low-level Cal. Gas 80 to 100% of span value Mid-level Cal. Gas 100.00%
45 to 55% of span value Mid-level Cal. Gas
80 to 90% of span value High-level Cal. Gas
0.00
VOC K2 (Ethane)
0.00
Span Value 0.00
Units ppm
Cylinder No.
Expiration
Date Cylinder Value: Response Difference CAL. ERROR Status
Zero Gas
Low-level Cal. Gas
Mid-level Cal. Gas
High-level Cal. Gas
<0.10% of span value Zero Gas
25 to 35% of span value Low-level Cal. Gas
45 to 55% of span value Mid-level Cal. Gas
80 to 90% of span value High-level Cal. Gas
Page 1
AG RM 25 THC 2024 rev
Division of Air Quality Stack Test Review of
Ash Grove Cement Coal Mill/Raw Mill On
VOC K3
(Propane)
VOC K4
(Butane)
VOC K2
(Ethane)CO2 O2 Ash Grove Cement
CS Calibration Span 130.00 22.58 22.12
Units ppm ppm ppm % %
CV - Cylinder Value: VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.80 11.26 11.24
Mid-Level 19.82 11.26 11.24
High-Level 30.17 22.58 22.12
Zero Gas 0.00% 0.00% 0.00%
Low Level Cal Gas 8.31%
Mid leverl Cal. Gas 15.25% 49.87% 50.81%
High Level Cal. Gas 23.21% 100.00% 100.00%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 19.82 11.26 11.24
Calibration Error Test
Cs - Measured Concentration VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.20 11.20 11.20
Mid-Level 20.00 11.20 11.20
High-Level 30.20 22.40 22.10
Enter Up-scale Analyzer Response to be used during testing.
20.00 11.20 11.20
ABS Difference:
Zero Gas 0.00 0.00 0.00
Low level Cal. Gas 0.60
Mid level Cal. Gas 0.18 0.06 0.04
High level Cal. Gas 0.03 0.18 0.02
Pre-Test Sampling SystemDrift
Initial Values VOC VOC VOC CO2 O2
CO - Low-Level 0.20 0.00 0.00 System Bias.
SBi - Zero Drift 0.15% TRUE TRUE 0.00% 0.00%± 5% of Span
Difference 0.2 TRUE TRUE 0 0
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.00 11.30 11.70
SBi - Up-Scale Drift 0.00% TRUE TRUE 0.44% 2.26%
Difference 0.00 TRUE TRUE 0.10 0.50
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:6/13/2024 VOC VOC VOC VOC
(Propane) (Butane) (Ethane)CO2 O2 VOC
Enter THC= 3.30 5.89 17.33 VOC
CO2/O2
Post-Test System Drift =(Cs - Cdir)/CS x 100
Final Values VOC VOC VOC CO2 O2
CO - Low-Level 0.40 0.00 0.20 System Bias.
SBi - Zero Bias 0.31% TRUE TRUE 0.00% 0.90%± 5% of Span
Difference 0.4 TRUE TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.20 11.10 11.30
SBi - Up-Scale Bias 0.15% TRUE TRUE 0.44% 0.45%
Difference 0.2 TRUE TRUE 0.1 0.1
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Error % of Span - D=ABS(SBf - SBi)
Low-Level Cal Error 0.15% TRUE TRUE 0.00% 0.90% Drift
Difference 0.2 TRUE TRUE 0.0 0.2 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Cal. Error 0.15% TRUE TRUE 0.00% 1.81%
Difference 0.2 TRUE TRUE 0.2 0.4
Pass or Re-Calibrate Pass Pass Pass
<0.10% of the Span Value - O2 0 to 20%
25 to 35% of the Span Value
45 to 55% of the span value - O2 40% to 60%
80 to 90% of the span value - O2 100%
NOTE
These cells scans for the appropriate
CMAand Cir. gas after the Cm - Up-scale gas is entered.
If this scan is incorrect change the
Cma and Cdir to the correct gas value.
Failed Bias Dialog
Failed Drift Dialog
CO Calibration Gas
Failed Bias Dialog
AG RM 25 THC 2024 rev
Division of Air Quality Stack Test Review of
Ash Grove Cement Coal Mill/Raw Mill On
VOC K3
(Propane)
VOC K4
(Butane)
VOC K2
(Ethane)CO2 O2 Ash Grove Cement
CS Calibration Span 130.00 22.58 22.12
Units ppm ppm ppm % % Unprotected
CV - Cylinder Value: VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.80 11.26 11.24
Mid-Level 19.82 11.26 11.24
High-Level 30.17 22.58 22.12
Zero Gas 0.00% 0.00% 0.00%
Low Level Cal Gas 8.31%
Mid leverl Cal. Gas 15.25% 49.87% 50.81%
High Level Cal. Gas 23.21% 100.00% 100.00%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 19.82 11.26 11.24
Calibration Error Test
Cs - Measured Concentration VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.20 11.20 11.20
Mid-Level 20.00 11.20 11.20
High-Level 30.20 22.40 22.10
Enter Up-scale Analyzer Response to be used during testing.
20.00 11.20 11.20
ABS Difference:
Zero Gas 0.00 0.00 0.00
Low level Cal. Gas 0.60
Mid level Cal. Gas 0.18 0.06 0.04
High level Cal. Gas 0.03 0.18 0.02
Pre-Test Sampling SystemDrift
Initial Values VOC VOC VOC CO2 O2
CO - Low-Level 0.40 0.00 0.20 System Bias.
SBi - Zero Drift 0.31% TRUE TRUE 0.00% 0.90%± 5% of Span
Difference 0.4 TRUE TRUE 0 0.2
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.20 11.10 11.30
SBi - Up-Scale Drift 0.15% TRUE TRUE 0.44% 0.45%
Difference 0.20 TRUE TRUE 0.10 0.10
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:6/13/2024 VOC VOC VOC VOC
(Propane) (Butane) (Ethane)CO2 O2 VOC
Enter THC= 3.70 6.07 16.83 VOC
CO2/O2
Post-Test System Drift =(Cs - Cdir)/CS x 100
Final Values VOC VOC VOC CO2 O2
CO - Low-Level 0.50 0.10 0.20 System Bias.
SBi - Zero Bias 0.38% TRUE TRUE 0.44% 0.90%± 5% of Span
Difference 0.5 TRUE TRUE 0.1 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.20 11.20 11.20
SBi - Up-Scale Bias 0.15% TRUE TRUE 0.00% 0.00%
Difference 0.2 TRUE TRUE 0.0 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Error % of Span - D=ABS(SBf - SBi)
Low-Level Cal Error 0.08% TRUE TRUE 0.44% 0.00% Drift
Difference 0.1 TRUE TRUE 0.1 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Cal. Error 0.00% TRUE TRUE 0.44% 0.45%
Difference 0.0 TRUE TRUE 0.1 0.1
Pass or Re-Calibrate Pass Pass Pass
<0.10% of the Span Value - O2 0 to 20%
25 to 35% of the Span Value
45 to 55% of the span value - O2 40% to 60%
80 to 90% of the span value - O2 100%
Failed Bias Dialog
Failed Drift Dialog
Failed Bias Dialog
AG RM 25 THC 2024 rev
Division of Air Quality Stack Test Review of
Ash Grove Cement Coal Mill/Raw Mill On
VOC K3
(Propane)
VOC K4
(Butane)
VOC K2
(Ethane)CO2 O2 Ash Grove Cement
CS Calibration Span 130.00 22.58 22.12
Units ppm ppm ppm % % Unprotected
CV - Cylinder Value: VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.80 11.26 11.24
Mid-Level 19.82 11.26 11.24
High-Level 30.17 22.58 22.12
Zero Gas 0.00% 0.00% 0.00%
Low Level Cal Gas 8.31%
Mid leverl Cal. Gas 15.25% 49.87% 50.81%
High Level Cal. Gas 23.21% 100.00% 100.00%
Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration.
CDir CMA 19.82 11.26 11.24
Calibration Error Test
Cs - Measured Concentration VOC VOC VOC CO2 O2
Zero Gas 0.00 0.00 0.00
Low-Level 10.20 11.20 11.20
Mid-Level 20.00 11.20 11.20
High-Level 30.20 22.40 22.10
Enter Up-scale Analyzer Response to be used during testing.
20.00 11.20 11.20
ABS Difference:
Zero Gas 0.00 0.00 0.00
Low level Cal. Gas 0.60
Mid level Cal. Gas 0.18 0.06 0.04
High level Cal. Gas 0.03 0.18 0.02
Pre-Test Sampling SystemDrift
Initial Values VOC VOC VOC CO2 O2
CO - Low-Level 0.50 0.10 0.20 System Bias.
SBi - Zero Drift 0.38% TRUE TRUE 0.44% 0.90%± 5% of Span
Difference 0.5 TRUE TRUE 0.1 0.2
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.20 11.20 11.20
SBi - Up-Scale Drift 0.15% TRUE TRUE 0.00% 0.00%
Difference 0.20 TRUE TRUE 0.00 0.00
Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal.
Raw Test Data Time Start Stop
Test Date:6/13/2024 VOC VOC VOC VOC
(Propane) (Butane) (Ethane)CO2 O2 VOC
Enter THC= 4.10 6.15 16.75 VOC
CO2/O2
Post-Test System Drift =(Cs - Cdir)/CS x 100
Final Values VOC VOC VOC CO2 O2
CO - Low-Level 0.20 0.00 0.20 System Bias.
SBi - Zero Bias 0.15% TRUE TRUE 0.00% 0.90%± 5% of Span
Difference 0.2 TRUE TRUE 0.0 0.2
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
CM - Up-scale Gas 20.20 11.00 11.20
SBi - Up-Scale Bias 0.15% TRUE TRUE 0.89% 0.00%
Difference 0.2 TRUE TRUE 0.2 0.0
Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal.
Calibration Error % of Span - D=ABS(SBf - SBi)
Low-Level Cal Error 0.23% TRUE TRUE 0.44% 0.00% Drift
Difference 0.3 TRUE TRUE 0.1 0.0 3% of Span
Pass or Re-Calibrate Pass Pass Pass
Up-scale Cal. Error 0.00% TRUE TRUE 0.89% 0.00%
Difference 0.0 TRUE TRUE 0.2 0.0
Pass or Re-Calibrate Pass Pass Pass
<0.10% of the Span Value - O2 0 to 20%
25 to 35% of the Span Value
45 to 55% of the span value - O2 40% to 60%
80 to 90% of the span value - O2 100%
Failed Bias Dialog
Failed Drift Dialog
Failed Bias Dialog
Source Information
Division of Air Quality
Compliance Demonstration
Method 23 for Dioxin/Furan Emissions
Source Information
Company Name Ash Grove Cement - Main Kiln DF Mill on
Company Contact:Cody Watkins
Contact Phone No.435-857-1283
Source Designation:Main Kiln DF Mill on
Test & Review Dates
Test Date: 6/13/2024
Review Date: 11/7/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/MMBtu lbs/hr ng/dscm
0.200 0.20
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.9998 0.0024
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
132.00 95.03 0.9950 1.669 0.84 25.09 -0.6 0.276
Contractor Information
Contracting Company: Mostardi Platt
Contact: Mike Lipinski
Phone No.: 630-993-2100
Project No.:
Round
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Compliance Demonstration of
Reference Method 23 for Dioxins/Furans - Toxic Equivalents
Ash Grove Cement - Main Kiln DF Mill on
Testing Results Lab Data - TEQ nano-grams collected
Test Date 6/13/2024 6/13/2024 6/13/2024 6/13/2024 Lab Data Probe Filter Back
Round Run 1 Run 2 Run 3 Run 4 Run 1 0 0.00499
As ft^2 95.03 95.03 95.03 95.03 Run 2 0 0.00704
Pbar 25.09 24.84 25.55 25.09 Run 3 0 0.00608
Pq (static)-0.60 -0.60 -0.60 -0.60 Run 4
Ps 25.05 24.80 25.51 25.05
Avg. Ts F 231.33 233.50 234.75 Front Half Emissions Summary
CO2 - FCO2 14.60 16.10 16.30 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
O2 12.00 11.70 11.60 0.00 ng/dscf 3.7244E-05 5.3144E-05 4.4741E-05 0.00004504
N2+C 73.40 72.20 72.10 100.00 lbs/hr 0.82942437 1.17046700 0.99947626 0.99978921
Md 30.82 31.04 31.07 28.00 ng/dscm@7% O2 0.002054 0.0028355 0.00236154 0.0024
Ms 29.02 29.20 29.26 28.00
Y 1.00 1.00 1.00 1.00
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 162.25 164.96 165.08 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 464.00 463.40 463.80 gr./dscf 0.0006 0.0008 0.0007 0.0007
AVG. Tm F 76.38 86.08 87.88 lbs/hr 0.8294 1.1705 0.9995 0.9998
Vm std 133.98 132.47 135.89 lbs/MMBtu
Vw std 21.84 21.81 21.83 #VALUE!
Bws 0.14 0.14 0.14
S Bws 1.00 1.00 1.00
Avg. Sqrt Dlp 0.77 0.77 0.77
Vs 53.70 53.89 53.05 F factor used
scfm wet 195769.11 193885.61 195976.79
acfm 306211.84 307283.42 302495.90
Qsd dscfh 10099767.65 9988468.80 10131053.98# Sample
Points 24.00 24.00 24.00 36.00
Dn 0.28 0.28 0.28 0.28
An 4.15E-04 4.15E-04 4.15E-04 4.15E-04
Total Test time 180.00 180.00 180.00 180.00
Time @ point 7.50 7.50 7.50 7.50
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.09 -0.60 25.05 231 14.60 12.00 73.40 30.82 29.02
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.7394
0.9950 0.84 162.246 464.00 76.38 133.981 21.840 0.1402 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.767 53.70 195,769 306,212 1.00998E+07 24 0.276 180 7.50 1.982500
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 80.155 0.55 1.85 232 74 74 Wt. (end) Wt. (start) lc
2 86.650 0.57 1.92 232 74 74 732.1 413.2 318.9
3 93.270 0.59 1.99 232 74 74 835.2 724.7 110.5
4 100.010 0.60 2.02 232 75 75 749.3 743.1 6.2
5 106.820 0.62 2.09 233 75 75 794.0 786.3 7.7
6 113.740 0.63 2.12 233 75 75 842.2 821.5 20.7
7 120.719 0.54 1.82 233 75 75 0.0
8 127.160 0.55 1.85 233 75 75 Isokinetics 101.2
9 133.680 0.57 1.92 233 75 75 Test Date 6/13/2024
10 140.310 0.59 1.99 232 75 75
11 147.060 0.61 2.06 232 75 75
12 153.930 0.63 2.12 232 75 75
13 160.910 0.55 1.85 231 76 76
14 167.430 0.56 1.89 231 76 76
15 174.030 0.58 1.95 231 76 76
16 180.740 0.60 2.02 230 77 77
17 187.590 0.61 2.06 230 77 77
18 194.490 0.62 2.09 230 77 77
19 201.450 0.54 1.82 230 79 79
20 207.950 0.56 1.89 230 79 79
21 214.590 0.59 1.99 230 79 79
22 221.400 0.61 2.06 230 80 80
23 228.350 0.62 2.09 230 80 80
24 235.340 0.63 2.12 230 80 80
25 242.401
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Run 2
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 24.84 -0.60 24.80 234 16.10 11.70 72.20 31.04 29.20
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.8293
0.9950 0.84 164.955 463.40 86 132.471 21.812 0.1414 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.767 53.89 193,886 307,283 9.99E+06 24 0.276 180 7.50 1.98
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 44.214 0.54 1.82 233.0 84.0 84.0 Wt. (end) Wt. (start) lc
2 50.760 0.55 1.85 233.0 85.0 85.0 737.80 419.00 318.8
3 57.400 0.58 1.95 233.0 85.0 85.0 856.90 746.30 110.6
4 64.220 0.59 1.99 233.0 85.0 85.0 751.80 744.90 6.9
5 71.090 0.61 2.06 233.0 85.0 85.0 768.80 761.60 7.2
6 78.080 0.63 2.12 233.0 86.0 86.0 793.6 773.7 19.9
7 85.202 0.54 1.82 233.0 86.0 86.0 0.0
8 91.780 0.56 1.89 234.0 86.0 86.0 Isokinetics 101.2
9 98.480 0.59 1.99 234.0 86.0 86.0 Test Date 6/13/2024
10 105.360 0.61 2.06 234.0 86.0 86.0
11 112.360 0.62 2.09 233.0 86.0 86.0
12 119.420 0.63 2.12 233.0 86.0 86.0
13 126.554 0.55 1.85 234.0 86.0 86.0
14 133.180 0.57 1.92 234.0 86.0 86.0
15 139.950 0.58 1.95 234.0 86.0 86.0
16 146.770 0.60 2.02 234.0 86.0 86.0
17 153.710 0.62 2.09 234.0 87.0 87.0
18 160.790 0.62 2.09 234.0 87.0 87.0
19 167.866 0.54 1.82 234.0 87.0 87.0
20 174.450 0.57 1.92 234.0 87.0 87.0
21 181.220 0.59 1.99 234.0 87.0 87.0
22 188.120 0.60 2.02 233.0 87.0 87.0
23 195.080 0.61 2.06 233.0 87.0 87.0
24 202.090 0.62 2.09 233.0 87.0 87.0
25 209.169
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Run 3
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.55 -0.60 25.51 235 16.30 11.60 72.10 31.07 29.26
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 1.8201
0.9950 0.84 165.082 463.80 88 135.892 21.831 0.1384 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.766 53.05 195,977 302,496 1.01E+07 24 0.276 180 7.50 1.98
TRUE 7/19/1901
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 11.645 0.54 1.82 235.0 87.0 87.0 Wt. (end) Wt. (start) lc
2 18.220 0.56 1.89 235.0 87.0 87.0 734.1 416.5 317.6
3 24.930 0.58 1.95 235.0 87.0 87.0 792.9 682.0 110.9
4 31.760 0.59 1.99 235.0 87.0 87.0 742.2 736.8 5.4
5 38.650 0.60 2.02 235.0 87.0 87.0 680.1 671.0 9.1
6 45.600 0.62 2.09 235.0 88.0 88.0 838.0 817.2 20.8
7 52.682 0.54 1.82 235.0 88.0 88.0 0.0
8 59.270 0.55 1.85 236.0 88.0 88.0 Isokinetics 102.3
9 65.930 0.58 1.95 236.0 88.0 88.0 Test Date 6/13/2024
10 72.770 0.60 2.02 236.0 88.0 88.0
11 79.720 0.61 2.06 236.0 88.0 88.0
12 86.740 0.63 2.12 236.0 88.0 88.0
13 93.868 0.55 1.85 235.0 89.0 89.0
14 100.530 0.57 1.92 235.0 89.0 89.0
15 107.330 0.58 1.95 235.0 89.0 89.0
16 114.180 0.60 2.02 234.0 89.0 89.0
17 121.160 0.61 2.06 234.0 89.0 89.0
18 128.200 0.62 2.09 234.0 89.0 89.0
19 135.294 0.54 1.82 233.0 89.0 89.0
20 141.900 0.56 1.89 233.0 87.0 87.0
21 148.630 0.59 1.99 234.0 87.0 87.0
22 155.520 0.61 2.06 234.0 87.0 87.0
23 162.530 0.62 2.09 234.0 87.0 87.0
24 169.600 0.63 2.12 234.0 87.0 87.0
25 176.727
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Method 23 for Dioxin/Furan Emissions
Source Information
Company Name Ash Grove Cement - Main Kiln DF Mill off
Company Contact:Casey Mueller
Contact Phone No.435-857-1214
Source Designation:Main Kiln DF Mill off
Test & Review Dates
Test Date: 6/13/2024
Review Date: 10/30/2024 Tabs Are Shown
Observer:none
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/MMBtu lbs/hr ng/dscm
0.200 0.20
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
44.3572 0.12
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
132.00 95.03 0.9950 1.669 0.84 25.03 -0.7 0.275
Contractor Information
Contracting Company: Mostardi Platt
Contact: Mike Lipinski
Phone No.: 630-993-2100
Project No.:
Round
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Compliance Demonstration of
Reference Method 23 for Dioxins/Furans - Toxic Equivalents
Ash Grove Cement - Main Kiln DF Mill off
Testing Results Lab Data - TEQ nano-grams collected
Test Date 6/13/2024 6/13/2024 6/13/2024 6/13/2024 Lab Data Probe Filter Back
Round Run 1 Run 2 Run 3 Run 4 Run 1 0 0.22556288
As ft^2 95.03 95.03 95.03 95.03 Run 2 0 0.27641394
Pbar 25.03 24.84 24.84 25.03 Run 3 0 0.29780985
Pq (static)-0.70 -0.70 -0.70 -0.70 Run 4
Ps 24.98 24.79 24.79 24.98
Avg. Ts F 344.13 382.75 385.42 Front Half Emissions Summary
CO2 - FCO2 13.70 13.60 13.90 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
O2 10.20 10.40 10.90 0.00 ng/dscf 1.9783E-03 2.6674E-03 2.8480E-03 0.00249791
N2+C 76.10 76.00 75.20 100.00 lbs/hr 37.29722532 46.10768869 49.66659537 44.35716979
Md 30.60 30.59 30.66 28.00 ng/dscm@7%O2 0.090758 0.1247011 0.13980079 0.118
Ms 28.77 28.76 28.83 28.00
Y 1.00 1.00 1.00 1.00
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 137.49 129.02 131.31 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 412.60 375.00 375.60 gr./dscf 0.0305 0.0412 0.0440 0.0385
AVG. Tm F 72.38 84.79 89.50 lbs/hr 37.2972 46.1077 49.6666 44.3572
Vm std 114.02 103.63 104.57 lbs/MMBtu
Vw std 19.42 17.65 17.68 #VALUE!
Bws 0.15 0.15 0.14
S Bws 1.00 1.00 1.00
Avg. Sqrt Dlp 0.70 0.66 0.67
Vs 53.36 51.66 52.23 F factor used
scfm wet 166774.44 152909.40 154101.16
acfm 304237.56 294583.79 297819.14
Qsd dscfh 8550089.56 7839259.86 7908900.06# Sample
Points 24.00 24.00 24.00 36.00
Dn 0.28 0.28 0.28 0.28
An 4.12E-04 4.12E-04 4.12E-04 4.12E-04
Total Test time 180.00 180.00 180.00 180.00
Time @ point 7.50 7.50 7.50 7.50
80.00
90.00
100.00
110.00
120.00
1357911131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11131517192123252729313335373941434547
% I
s
o
k
i
n
e
t
i
c
Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 25.03 -0.70 24.98 344 13.70 10.20 76.10 30.60 28.77
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 10.3922
0.9950 0.84 137.489 412.60 72.38 114.017 19.421 0.1455 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.702 53.36 166,774 304,238 8.55009E+06 24 0.275 180 7.50 1.679583
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 81.571 0.61 2.06 340 71 71 Wt. (end) Wt. (start) lc
2 88.010 0.57 1.92 340 71 71 948.0 679.1 268.9
3 94.230 0.54 1.82 341 71 71 845.2 735.6 109.6
4 100.290 0.48 1.62 341 71 71 725.7 719.0 6.7
5 106.000 0.42 1.42 341 71 71 670.1 663.2 6.9
6 111.340 0.39 1.31 341 71 71 851.9 831.4 20.5
7 116.480 0.59 1.99 342 72 72 0.0
8 122.730 0.52 1.75 342 72 72 Isokinetics 102.5
9 128.590 0.48 1.62 342 72 72 Test Date 6/13/2024
10 134.230 0.45 1.52 343 72 72
11 139.680 0.41 1.38 343 72 72
12 144.880 0.38 1.28 343 72 72
13 149.890 0.60 2.20 345 72 72
14 156.180 0.58 1.95 345 72 72
15 162.360 0.53 1.79 345 73 73
16 168.280 0.49 1.65 345 73 73
17 173.980 0.46 1.55 346 73 73
18 179.490 0.41 1.38 346 73 73
19 184.690 0.61 2.06 347 73 73
20 191.040 0.58 1.95 347 74 74
21 197.240 0.54 1.82 347 74 74
22 203.210 0.47 1.58 349 74 74
23 208.790 0.41 1.38 349 74 74
24 213.990 0.39 1.31 349 74 74
25 219.060
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Run 2
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 24.84 -0.70 24.79 383 13.60 10.40 76.00 30.59 28.76
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 17.1207
0.9950 0.84 129.017 375.00 85 103.626 17.651 0.1455 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.662 51.66 152,909 294,584 7.84E+06 24 0.275 180 7.50 1.23
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 21.513 0.52 1.46 381.0 84.0 84.0 Wt. (end) Wt. (start) lc
2 27.370 0.49 1.37 381.0 84.0 84.0 794.00 565.60 228.4
3 33.060 0.45 1.26 381.0 84.0 84.0 875.40 764.50 110.9
4 38.500 0.39 1.09 381.0 84.0 84.0 729.10 722.20 6.9
5 43.580 0.36 1.01 381.0 84.0 84.0 720.40 712.40 8.0
6 48.450 0.35 0.98 382.0 84.0 84.0 845.9 825.1 20.8
7 53.250 0.55 1.52 382.0 84.0 84.0 0.0
8 59.270 0.49 1.37 382.0 84.0 84.0 Isokinetics 101.6
9 64.950 0.46 1.29 382.0 85.0 85.0 Test Date 6/13/2024
10 70.470 0.41 1.15 382.0 85.0 85.0
11 75.670 0.39 1.09 382.0 85.0 85.0
12 80.750 0.37 1.04 383.0 85.0 85.0
13 85.690 0.54 1.51 383.0 85.0 85.0
14 91.670 0.51 1.43 383.0 85.0 85.0
15 97.470 0.47 1.32 383.0 85.0 85.0
16 103.370 0.43 1.20 383.0 85.0 85.0
17 108.370 0.38 1.06 383.0 85.0 85.0
18 113.380 0.36 1.01 383.0 85.0 85.0
19 118.250 0.52 1.46 383.0 85.0 85.0
20 124.110 0.49 1.37 385.0 85.0 85.0
21 129.800 0.45 1.26 385.0 85.0 85.0
22 135.240 0.42 1.18 385.0 86.0 86.0
23 140.510 0.39 1.09 385.0 86.0 86.0
24 145.590 0.37 1.04 385.0 86.0 86.0
25 150.530
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Run 3
Ash Grove Cement - Main K Flow & Moisture Test Date 6/13/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
95.03 24.84 -0.70 24.79 385 13.90 10.90 75.20 30.66 28.83
YCpVm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 17.6798
0.9950 0.84 131.305 375.60 90 104.568 17.679 0.1446 0.9990 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
0.669 52.23 154,101 297,819 7.91E+06 24 0.275 180 7.50 1.26
TRUE 7/19/1901
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 52.355 0.54 1.51 386.0 89.0 89.0 Wt. (end) Wt. (start) lc
2 58.360 0.50 1.40 386.0 89.0 89.0 719.9 487.3 232.6
3 64.140 0.48 1.34 386.0 89.0 89.0 848.3 741.1 107.2
4 69.800 0.45 1.26 386.0 89.0 89.0 791.4 785.0 6.4
5 75.280 0.39 1.09 386.0 89.0 89.0 626.5 619.0 7.5
6 80.380 0.37 1.04 386.0 89.0 89.0 826.4 804.5 21.9
7 85.350 0.52 1.46 386.0 89.0 89.0 0.0
8 91.250 0.49 1.37 386.0 89.0 89.0 Isokinetics 101.6
9 96.970 0.47 1.32 386.0 89.0 89.0 Test Date 6/13/2024
10 102.570 0.44 1.23 386.0 89.0 89.0
11 107.990 0.41 1.15 385.0 89.0 89.0
12 113.220 0.38 1.06 385.0 89.0 89.0
13 118.260 0.52 1.46 385.0 90.0 90.0
14 124.170 0.50 1.40 385.0 90.0 90.0
15 129.960 0.47 1.32 385.0 90.0 90.0
16 135.580 0.43 1.20 385.0 90.0 90.0
17 140.950 0.40 1.12 385.0 90.0 90.0
18 146.130 0.37 1.04 385.0 90.0 90.0
19 151.110 0.51 1.43 385.0 90.0 90.0
20 156.960 0.49 1.37 385.0 90.0 90.0
21 162.700 0.46 1.29 385.0 90.0 90.0
22 168.250 0.41 1.15 385.0 90.0 90.0
23 173.500 0.39 1.09 385.0 90.0 90.0
24 178.610 0.38 1.06 385.0 90.0 90.0
25 183.660
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