DAQ-2024-007209

rnostardi e platt
Gontinuous Emissions Monitoring System
Relative Accuracy Test Audit Report
Ash Grove Gement Company
rLeamington Gement Plant
Main Kiln Stack
Leamington, Utah
June 20,2023
Report Submittal Date
August 10,2023
@ Copyright2023
Allrights reserved in
Mostardi Platt
Project No. M2325124
TABLE OF CONTENTS
1.0 EXECUTTVE SUMMARY............... ............................1
2.0 TEST METHODOLOGY............ ...........2
Method 1 Sample and Velocity Traverse Determination................. ...............2
Method 2 and 2H Volumetric Flow Rate Determination ................. ................2
Method 3A Oe Determination...... ........3
Method 4 Moisture (HzO) Determination ................3
Method 25A Total Hydrocarbon (THC) Determination ................. ..................3
Method 30B Hg Determination ................. ..............3
Method 3201321 HCl, COz, HzO, NOx, and CO Determination ................. .........................4
3.0 TEST RESULT SUMMARIES ..............5
4.0 CERTIFICATION
APPENDICES
Appendix A - Test Section Diagrams ...................17
Appendix B - Sample Train Diagrams............... .......................20
Appendix C - Calculation Nomenclature and Formulas ...........25
Appendix D - Reference Method Test Data .........36
Appendix E - CEMS and Plant Operating Data............ ..........., 64
Appendix F - Field Data Sheets ........90
Appendix G - Calibration and Response Time Data ........... ....................... 132
Appendix H - Calibration Gas Cylinder Data ......148
Appendix l- Mercury QA Data...... .....................156
Project No. M232512A
Main Kiln Stack
@Mostardi Platt
1.0 EXECUTIVE SUMMARY
Mostardi Platt conducted a Continuous Emissions Monitoring System (CEMS) Relative Accuracy
Test Audit (RATA) for Ash Grove Cement Company at the Leamington Cement Plant in
Leamington, Utah, on the Main Kiln Stack on June 20,2023. This report summarizes the results
of the test program and test methods.
The test location, test date, and test parameters are summarized below.
The purpose of the test program was to demonstrate the relative accuracies of the Main Kiln Stack
NOx, CO, COz, Oz, THC, Hg, HCl, and volumetric flow analyzers during the specified operating
condition. The test results from this program indicate that each CEMS meets the United States
Environmental Protection Agency (USEPA) annual performance specification for relative
accuracy as published in 40 Code of Federal Regulations Part 60 (40CFR60) and 40 CFR 63
Subpart LLL.
Note that all reference method data is one hour ahead of plant CEMS time.
RATA TEST INFORMATION
Test Location Test Date Test Parameters
Main Kiln Stack June 20,2023
Carbon Dioxide (COz), Oxygen (Oz),
Nitrogen Oxides (NOx), Carbon Monoxide
(CO), Total Hydrocarbons (THC), Mercury
(Hg), Volumetric Flowrate (VFR), and
Hydrogen Chloride (HCl)
RATA RESULTS
Test
Location Parameter Units
Relative Accu racy Acceptance
Criteria
Relative
Accuracy
(RA)
Main Kiln
Stack
NOx ppmvw 320.0o/o of the mean reference value 15.06%
NOx lb/hr <20.0% of the mean reference value 15.64Yo
co ppmvw 3 10.0Yo of the mean reference value 5.69%
co lb/hr 3 20.0o/o of the mean reference value 6.1'.t%
COz o/o wal 3 20.0o/o of the mean reference value 6.94Yo
Oz o/o dry < 20.0% of the mean reference value 2.360/o
VFR scfh 310.0o/o of the mean reference value 1.41%
THC ppmvd@7o/oOz 3 10.0o/o of the applicable performance
standard of 24 ppmvd @7% Oz
1.41o/o
Hg ug/wscm s 1.0 ug/wscm + confidence coefficient
(cc) for sources s5.0 ug/wscm
0.234 mean
difference + cc
HCt ppmvd@3%Oz < 15.0% of the applicable performance
standard of 3.0 ppmvd @7o/o Oz 7.73o/o
Project No. M2325124
Main Kiln Stack
1 of 166 @Mostardi Platt
TEST PERSONNEL INFORMATION
Location Address Contact
Test Facility Ash Grove Cement Company
ur-132
Leamington, UT 84638
Mr. Cody Watkins
Environmental Manager
(43s) 857-1212
[e-mail]
Testing Company
Representative
MostardiPlatt
SSS lndustrial Drive
Elmhurst, 1160126
Mr. Richard J. Sollars ll
RegionalManager
(630) e93-2100
[e-mail]
www.mostardiplaft.com
The identifications of the individuals associated with the test program are summarized below.
The test crew consisted of W. Petrovich, S. McGough, T. Magana, B. Alba, and R. Sollars of Mostardi
Platt.
2.0 TEST METHODOLOGY
Emission testing was conducted following the USEPA methods specified in 40CFR60, Appendix
A in addition the Mostardi Platt Quality Manual. Schematics of the test section diagrams and
sampling trains used are included in AppendixAand B respectively. Calculation nomenclature are
included in Appendix C. Copies of analyzer print-outs for each test run are included in Appendix
D. CEM data and process data as provided by Ash Grove Cement Company are also included in
Appendix E.
The following methodologies were used during the test program:
Method 1 Sample and Velocity Traverse Determination
Test measurement points were selected in accordance with USEPA Method 1, 40CFR60,
Appendix A. The characteristics of the measurement location is summarized below.
Method 2 and 2H Volumetric Flow Rate Determination
Gas velocity was measured following USEPA Method 2, 40CFR60, Appendix A, for purposes of
calculating stack gas volumetric flow rate and emission rates on a lb/hr basis. An 8-foot long S-
type pitot tube, 0-10 inch differential pressure gauge, and K-type thermocouple and temperature
readout were used to determine gas velocity at each sample point. ln accordance with Method
2H, a default wall affect adjustment factor of 0.995 was used for non-brick and mortar stacks. All
of the equipment used was calibrated in accordance with the specifications of the Method. Copies
Poject No. M232512A
Main Kiln Stack
SAMPLE POINT SELECTION
Test
Location
Stack
Diameter
Upstream
Distance
Downstream
Distance Test Parameters
Number of
Sampling
Points
Main Kiln
Stack 132 lnches 4.09
Diameters
5.05
Diameters
Oz,COz, NOx, CO,
THC, Hg 3
Volumetric Flowrate 16
2 of 166 OMostardi Plaft
of field data sheets are included in Appendix F. Calibration data are presented in Appendix G. This
testing met the performance specifications as outlined in the Method.
Method 3A Oz Determination
Stack gas Oz concentrations and emission rates were determined in accordance with USEPA
Method 3A, 40CFR60, Appendix A. A Thermo analyzer was used to determine the Oz
concentrations in the manner specified in the Method. The instrument has a paramagnetic
detector and operates in the nominal range of 0% to 25% with the specific range determined by
the high-level calibration gas. High-range calibrations were performed using USEPA Protocolgas.
Zero nitrogen (a low ppm pollutant in balance nitrogen calibration gases)was introduced during
other instrument calibrations to check instrument zero. High- and a mid-range % Oz levels in
balance nitrogen were also introduced. Zero and mid-range calibrations were performed using
USEPA Protocol gas. Copies of the gas cylinder certifications are found in Appendix H. This
testing met the performance specifications as outlined in the Method.
Method 4 Moisture (HzO) Determination
Stack gas moisture content was determined using a Method 4 sampling train. ln this technique,
stack gas is drawn through a series of four impingers. The first two impingers are each charged
with 100 mls of deionized, distilled water. lmpinger three is left empty and impinger four is charged
with clean, dried silica gel. The entire impinger train is measured or weighed before and after each
test run to determine the mass of moisture condensed.
During testing, the sample train was operated in the manner specified in USEPA Method 4. All of
the data specified in Method 4 (gas volume, delta H, impinger outlet well temperature, etc.)was
recorded on field data sheets.
All of the equipment used is calibrated in accordance with the specifications of the Method.
Calibration data can be found in Appendix G.
Method 25A Total Hydrocarbon (THC) Determination
THC concentrations and emission rates were determined in accordance with Method 25A. A
Thermo Fisher 51i analyzer was used to determine THC concentrations. Stack gas was delivered
to the system via a Teflon@ sampling line, heated to a temperature of 375"F.
The system was calibrated using certified calibration gases of propane. A list of calibration gases
used and the results of all calibration and other required quality assurance checks can be found
in Appendix G. Copies of calibration gas certifications can be found in Appendix H.
Method 308 Hg Determination
Paired trains were utilized sampling three test points per test run at the Main Kiln Stack.
Per Method 30B sampling, each sample was collected on the paired in-situ sorbent traps. 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, lnc. and meets all
requirements for Method 308 sampling. Samples were analyzed onsite utilizing an Ohio Lumex,
lnc. analyzer for total gaseous mercury. Sample analysis data and mercury quality assurance and
control data are found in Appendix l. All of the equipment used was calibrated in accordance with
the specifications of the Method.
Project No. M2325124
Main Kiln Stack
3 of 166 @Mostardi Platt
Method 32A1321 HGl, COz, HzO, NOx, and CO Determination
Extractive Fourier transform infrared (FTIR) spectrometry following USEPA Method 320 and
Method 321 will be performed for determination of HCl, COz, HzO, NOx, and CO.
FTIR technology works on the principle that most gases absorb infrared light. This is true for all
compounds with the exception of homonuclear diatomic molecules and noble gases such as: Nz,
Oz, Hz, He, Ne, and Ar. Vibrations, stretches, bends, and rotations within the bonds of a molecule
determine the infrared absorption distinctiveness. The absorption creates a "fingerprint" which is
unique to each given compound. The quantity of infrared light absorbed is proportional to the gas
concentration. Most compounds have absorbencies at different infrared frequencies, thus
allowing the simultaneous analysis of multiple compounds at one time. The FTIR software
compares each sample spectrum to a user-selected list of calibration references and
concentration data is generated.
FTIR data will be collected using an MKS MultiGas 2030 FTIR spectrometer. Analyte spiking with
HCI and SFo gas will assure the ability of the FTIR to quantify analytes in the presence of effluent
gas. Ethylene gas will be used as the calibration transfer standard. All analyte spikes will be
introduced using an instrument grade stainless steel rotometer. All QA/QC procedures will be
within the acceptance criteria allowance of Methods 320 and 321.
Project No. M2325'l2A
Main Kiln Stack
4 of 166 @Mostardi Platt
3.0 TEST RESULT SUMMARIES
Client Ash Grow Cement Company Location: Main Kiln Stack
Facility: Leamington Cement Plant Datel.6120123
Project #: M232512 Te$ Method: 320
NOx oPmvw RATA
1=accept
0=reject
Te$
Run
Clinker
ton/hr Iest Date Start Time End Time RM NOx
Ppmw,
CEM NOx
ppmvw
(RMCEM)
Difference
(dt)
(RM€EM)
Difference2
(di2)
0 1 '117.5 06120123 7:30 7:59 197.6 228.8 -31.2 973.M
1 2 118.4 06t20t23 8:07 8:36 208.3 238.9 -30.6 936.36
1 3 114.7 06120t23 8:43 9:12 209.7 240.0 -30.3 918.09
1 4 119.1 06120t23 q.35 '10:04 195.6 225.4 -29.8 888.04
I 5 119.1 06120t23 10:12 1O:4'l 192.8 222.6 -29.8 888.04
1 6 119.3 06t20t23 10:48 '11:17 207.8 238.0 -30.2 912.U
1 7 119.3 06120t23 11:38 12:07 200.1 229.3 -29.2 852.64
1 8 119.5 o6t20t23 12:.13 12:42 198.1 226.7 -28.6 817.96
1 9 119.0 06t20t23 12:50 13:19 210.3 240.0 -29.7 882.09
10 1't8.6 06120t23 13:40 14:09 193.9 220.1 -26.2 686.,14
n 9
(0.s75)2.306
Mean Reference Method Value 201.84 RM avg
Mean GEM Value 231.222 3EM avg
Sum of Differencer -264.400 I
Mean Difference a9.378
Sum of Differences Squared 7781.700 ,i2
Standard Deviatior 1.333 ld
Confi de nce Coeffi cl e nt 2.5oh Error (1 -tall'1.025 gc
Relative Accuracl 15.06 RA
Project No. M2325124
Main Kiln Stack
5 of 166 @Mostardi Platt
Client: Ash Grow Cement Company
Facility: Leamington Cement Plant
Proiect #: M232512
Location: Main Kiln Stack
Test Method: 320, 2
NO,lb/hr RATA
1=accept
0=reject
Te*
Run
Clinker
ton/hr Iesil Date Start Time End Time RM NO,
lb/hr
CEM NO,
lb/hr
(RM-CEM)
Difference
(di)
(RMCEM)
Difference2
(di2)
1 1 117.5 06t20t23 7;30 7:59 270.63 295.62 -24.99 624.5001
1 2 118.4 06t20t23 8:07 8:36 279.72 310.25 30.53 932.0809
1 3 114.7 06120123 8:43 9:12 276.18 312.57 -36.39 1324.2321
1 4 119.1 06t20t23 9:35 10:04 255.74 298.89 43.15 1861 .9225
1 5 119.1 06120123 10'.12 10:-41 260.06 298.88 -38.82 1506.9924
0 6 119.3 06120t23 1O:.48 11:17 272.24 318.28 46.04 2119.6816
1 7 119.3 06t20t23 11:38 12:07 263.61 307.60 43.99 1935."t201
I I 119_5 06120123 12:13 12:42 262.10 304.26 42.16 1777.4656
1 9 119.0 06t20123 12:50 13:19 283.02 321.87 -38.8s 1509.3225
1 10 118.6 06120123 13:40 14:09 261 .15 296.51 35.36 1250.3296
n 9
t(0.975)2.306
Mean Reference Method Value 268.023 RM avg
Mean CEM Value 305.{6'l iEM avq
Sum of Differencer -33/..240 da
Mean Difference -37.138 d
Sum of Differences Squareo 12721.966 di2
Standard Deviation 6.215 sd
Confi de nce Coeffi cie nt 2.5o/o Error (1 -tail 4.777 cc
Relative Accuracv 15.64 RA
Project No. M2325124
Main Kiln Stack
6 of 166 OMostardi Platt
Client: Ash Grore Cement Company Location: Main Kiln Stack
Facility: Leamington Cement Plant Dale:6120123
Project #: M232512 Test Method: 320
CO pomvw RATA
1=accept
0=reject
Test
Run
Clinker
ton/hr Test Date Start Time End Time RM CO
ppmvw
CEM CO
ppmvw
(RM.CEM)
Difference
(di)
(RMCEM)
Difference2
(di1
1 1 117.5 06t20t23 7:30 7:59 1021.0 985.1 35.9 1288.81
1 2 118.4 06120t23 8:07 8:36 'l 185.8 1225.6 -39.8 1584.04
1 3 114.7 o6t20t23 8:43 9:12 1253.7 t286.8 33.'l 1095.61
1 4 119.1 06t20t23 9:35 10:04 1488.8 1566.4 -77.6 6021.76
I 5 119.1 06t20123 1O:12 1O:41 577.9 529.2 48.7 2371.69
1 6 119.3 06t20t23 10:48 11'.17 44't.1 4U.4 6.7 44.89
1 7 119.3 o6t20t23 11:38 12:O7 455.6 468.0 -12.4 153.76
1 8 119.5 06t20t23 12:13 12:42 465.1 470.4 -5.3 28.09
0 I 119.0 06t20t23 12:50 13:19 618.6 697.8 -79.2 6272.64
1 10 118.6 06t20t23 13:40 14:09 538.4 595"7 -57.3 3283.29
n 9
(0.975)2.306
Mean Reference Method Value 825.267 RM avq
Mean CEM Value 840.178 CEM avq
Sum of Differences -134.200 di
Mean Difference -14.911 d
Sum of Differences Squared 1s871.940 di2
Standard Deviation 41.640 sd
Confi de nce Coefficie nt 2.5o/o Enor 11 -laill 32.007 cc
Relative Accurac 5.69 RA
Project No. M2325124
Main Kiln Stack
7 of '166 @Mostardi Platt
Client Ash Grow Cement Company
Facility: Leamington Cement Plant
Project #: M232512
Location: Main Kiln Stack
TeS Method: 320, 2
GO lb/hr RATA
l=accept
0=reject
Test
Run
Clinker
ton/hr Test Date Start Time End Time RM
CO lb/hr
CEM
GO lb/hr
(RM.cEM)
Difference
(di)
(RM4EM)
Difference2
(di2)
1 1 117.5 06120123 7:30 59 851.'t5 775.53 75.62 5718.38/,4
1 2 118.4 06t20t23 8:07 36 968.83 968.55 0.28 0.07u
1 3 114.7 06t20t23 8:43 9:12 1004.69 1020.09 -15.40 237.1600
1 4 1't9.1 06t20t23 9:35 10:04 1184.30 1264.87 40.57 6491 .5249
I 5 119.1 06120t23 1O:12 1O:'41 474.32 432.85 41.47 1719.7609
b 1't9.3 06t20t23 10:48 11:17 351.72 353.53 1.8'1 3.2761
7 't 19.3 06120123 11:38 12:07 365.1 9 382.30 -17.11 292.7521
1 8 1 19.5 06120t23 12:13 12:42 374.52 3U.49 -s.97 99.4009
0 I 119.0 06t20123 12:50 13: 19 506.55 569.95 63.40 4019.5600
10 118.6 06120t23 13:40 14:09 441.37 488.09 46.72 2182.758/.
n I
(0.97s)2.306
Mean Reference Method Value 668.454 RM avo
Mean CEM Value 674.478 CEM avE
Sum of Differencer 4.210 di
Mean Difference 6.023 d
Sum of Differences Souarec 16745.096 di2
Standard Deviatior 45.303 sd
Confi dence Coefficient 2.5o/o Error 11 -lai 34.82t cc
Relative Accuracl 6.11 RA
Project No. M232512A
Main Kiln Stack
8 of '166 OMostardi Platt
Clienf Ash Grow Cement Company
Facility: Leamington Cement Plant
Project#: M232512
Location: Main Kiln Stack
Te* Method: 320
CO2% (wet) RATA
'l=accepl
0=reject
Test
Run
Clinker
ton/hr
Test
Date Start Time End Time RM CO2 %
(wet)
CEM CO2o/o
(wet)
(RM.CEM)
Difference
(di)
(RMCEM)
Difference2
(di1
1 1 117.5 06120t23 7:30 7:59 12.7 13.6 {.9 0.81
1 2 118.4 06t20t23 8:07 8:36 12.8 13.5 4.7 0.49
1 3 114.7 06120123 8:43 9:12 12.8 13.7 4.9 0.81
1 4 1 19.1 06124t23 9:35 10:04 12.5 13.3 {.8 0.64
1 5 1 19.1 06t20t23 10:12 10:41 12.5 13.3 4.8 0.64
1 6 1 19.3 06t20t23 1o.4R 1'.l 17 12.5 13.4 4.9 0.81
1 7 1 19.3 06t20t23 '11:38 '12:O7 12.5 '13.3 4.8 0.&
1 8 1 19.5 06t20123 12:13 12:42 12.5 13.3 {.8 0.64
1 I 1 19_0 06t20t23 12:50 13:19 12.5 't3.3 -0.8 0.&
0 10 118.6 06t20t23 13:40 14:09 12.5 13.4 4.9 0.81
n I
(0.9751 2.306
Mean Reference Method Value 12.589 RM avo
Mean CEM Value 13.411 CEM avE
Sum of Differences -7.400 di
Mean Difference 4.822 d
Sum of Differences Squared 6.120 di2
Standard Deviation 0.067 Bd
Confidence Coefficient 2.5% Error (1-tail 0.051 CG
Relative Accuracy 6.94 RA
Project No. M2325124
Main Kiln Stack
9 of '166 @Mostardi Platt
Client: Ash Grow Cement Company Location: Main Kiln Stack
Facility: Leamington Cement Plant DaE:6120123
Project #: M232512 Tesil Method: 34
02 % (wet) RATA
1=accept
0=reject
Test
Run
Clinker
ton/hr
Test
Date Start Time End Time RM02%
(wet)
cEM 02 %
(wet)
(RM-CEM)
Difference
(di)
(RMCEM)
Difference2
(di2)
1 1 117.5 06120t23 7:30 7:59 9.2 9.0 o.2 0.04
0 2 118.4 06t20123 8:07 8:36 9.4 8.9 0.5 0.25
1 3 114.7 06t20t23 8:43 9:12 9.3 8.8 0.5 0.25
1 4 1 19.1 06t20t23 9:35 10:04 9.0 9.0 0.0 0.00
1 5 119.1 06t20t23 10:12 1O:41 9.0 9.1 {.1 0.01
1 6 119.3 06120123 10:48 11:.17 9.1 9.1 0.0 0.00
1 7 119.3 o6t20t23 1 1:38 12:07 9.2 9.1 0.1 0.01
1 8 119.s 06t20t23 12:.13 12'.42 9.0 9.1 {.1 0.01
1 I 1 19.0 06120123 12:50 13:19 9_1 9.2 {.1 0.01
1 10 118.6 06t20t23 13:40 14:09 9.2 9.1 0.1 0.01
n I
t(0.97!2.306
Mean Refurence Method Value 9.122 RM avq
Mean CEM Value 9.056 CEM avq
Sum of Differences 0.600 di
Mean Difference 0.067 d
Sum of Differences Squared 0.340 di2
Standard Deviation 0.194 sd
Confi de nce Coefficie nt 2.5o/o Error 11 -lai 0.149 cc
Relative Accuracy 2.35 RA
Project No. M232512A
Main Kiln Stack
10 of 166 @Mostardi Platl
Client: Ash Grole Cement Company Location: Main Kiln Stack
Facility: Leamington Cement Plant Test ltr/lethod: 25A, 34
Projec{ #: l.v1232512
Applicable Standard: 24
THC oomvd @ 7oh 02 RATA
1=accept
0=reject
Test
Run
Glinker
ton/hr Test Date Start Tirne End Time
RM THC
ppmvd @ 7%
02
CEM THC
ppmvd@7o/o
02
(RM-CEM)
Difference
(di)
(RM-CEM)
Difference2
(di2)
0 1 117.533 06120t23 7:30 7:59 13.7 13.1 0.6 0.41
1 2 118.437 06120123 8:07 8:36 18.9 18.6 0.3 0.08
1 3 114.737 06120123 8:43 9'.12 13.3 12.8 0.5 0.30
1 4 1't9.067 06t20t23 9:35 10:04 13.3 12.8 0.5 0.21
1 5 119.14 06120123 10:12 10:41 13.2 13.2 0.0 0.00
1 6 119.287 06t20t23 10:48 11:17 13.3 13.5 -0.2 0.05
1 7 119.3 06t20t23 11:38 12:07 13.6 13.7 -0.1 0.01
1 8 119.473 06t20t23 12:13 12:42 12.9 13.6 -o.7 0.42
1 I 1 19.003 06120123 12:5O 13:19 '13.3 13.4 -0.1 0.00
I 10 118.613 06t20123 13:40 14:09 12.7 13.2 -0.5 0.23
n 9
r(0.975)2.306
llllean Reference Method Value 13.833 RM avq
Itllean CEM Value 13.861 CEM avq
Sum of Differences -0.247 di
lllean Difference -0.027 d
Sum of Differences Squarec 1.312 di2
Standard Deviatior 0./O4 sd
Confidence Coefiicient 2.5% Error (1-tail)0.310 GC
Relative Accuracy - APS 1.41 RA
o Relatile accuracy based upon +t- 10% of applicable standard of 24 ppmvd @7o/" 02
Project No. M2325124
Main Kiln Stack
11 of 166 @Mostardi Platt
Glient Ash Grow Cement Company
Plant Leamington Cement Plant
Project #: M232512
Location: Main Kiln Stack
Dale:6120123
Te$ Method: Sorbent Hg (308)
Ho uo/wscm F{ATA
1=accept
0=reject
Tesil
Run
Test
Date
Start
Time
End
Time
RM
ug/wscm
CMMS
ug/wscm
(RMCMMS)
Difference
(di)
(RMCMMS)
Difference2
(di2)
1 1 06t20t23 07:30 08:00 0.496 0.547 4.051 0.003
1 2 06t21t22 08:07 08:37 0.463 0.501 -0.038 0.001
1 3 06120t23 08:43 09:1 3 0.460 0.510 4.050 0.003
1 4 06120t23 09:35 10:05 0.623 0.795 4.172 0.029
1 5 06120123 1O:12 10:42 o.977 1.261 4.2U 0.081
0 6 06t20t23 10:48 11:18 0.985 1.421 4.436 0.190
1 7 06120t23 1 1:38 12:08 0.990 1.100 {.110 o.012
1 8 06t20t23 12:13 12:43 0.806 1.03s 4.229 0.053
1 9 06120123 12:50 13:20 0.655 0.894 4.239 0.057
1 10 06120t23 13:40 14:10 0.677 0.934 4.257 0.066
(0.025)
Mean Reference Method Value
Mean CMM Value
Sum of Differences
Mean Difference
Sum of Differences Squared
Standard Deviation
Confi dence Coefficient 2.5oh Error (1 -tail)
Relative Accuracv{PS
9
2.306
0.683 RM avq
0.u2 CMM avq
-1.430 di
{.159 d
0.305 di2
0.098 Bd
0.076 GG
0.234 RAA
A Relative Accuracy based on rrean difference of +A1 .0 ug/w scm plus @ f or enission sources <5.0 ug/w scm of rercury
Project No. M232512A
Main Kiln Stack
12 of '166 @Mostardi Platl
Client: Ash Grore Cernent Company Location: Main Kiln Stack
Facility: Leamington Cement Plant Test tUlethod: 321, 34
Project #: t/€32512
Applicable Standard: 3
HClppmvd @7% 02 RATA
1=accept
0=rejec-t
Test
Run
Clinker
ton/hr fest Date Start Tirne End Time
RM HCI
ppmvd@7%
02
CEM HCI
pprvd @ 7%
02
(RM-CEM)
Difference
(di)
(RM-CEM)
Difference2
(di2l
1 1 117.5 06t20t23 7:30 7:59 0.7 0.3 0.4 0.16
1 2 118.4 06t20t23 8:07 8:36 0.3 0.2 0.1 0.01
I 3 114.7 06t20t23 8:43 9'.12 0_5 0.4 0.1 0.01
0 4 119.'t o6t20t23 9:35 10:M 0.7 0.3 0.4 0.16
1 5 119.1 06t20t23 1O:.12 1O:41 0.4 0.4 0.0 0.00
1 6 119.3 06t20t23 10:48 11:17 0.0 0.4 -0.4 0.16
1 7 1't9.3 06t20t23 11:38 12:07 0.6 0.3 0.3 0.09
1 8 119.5 06t20t23 12'.13 12:42 0.'l 0.4 -0.3 0.09
1 I 119.0 06120t23 12:50 13:19 0.1 0.3 -0.2 0.04
I 10 118.6 06t20t23 13:40 14:09 0.6 0.4 o.2 0.04
n 9
(0.975)2.306
Illlean Refurence lJlethod Value 0.367 RM avq
Ittuan CEM Value 0.344 CEM avg
Sum of Differences 0.200 di
Mean Difierence 0.022 d
Sum of Difierences Squared 0.600 di2
Standard Deviation 0.273 sd
Confidence Goefficient 2.5% Error (l-tail)0.210 cc
Relative Accuracv - APS 7.73 RA
A Relatire accuracy based upon +l- 15o/o of applicable standard of 3 ppnM @7% 02
Project No. M2325124
Main Kiln Stack
'l 3 of 166 @Mostardi Platt
Client Ash Grow Cement Company Test Location: Main Kiln Stack
Facility: Leamington Cement Plant Test Date: 612012023
Project #: M232512 Test Method: 2, D2H WAF: 0.995
Volunrctric Eow RATA - tSrnnl Load
1=accept
0=reject
Tes{
Run
Test
Date
Start
Time
End
Time
Wall Effect Adjusted
Reference Method
Flow SCFH CEM Flow SCFH
(RM4EM)
Difference
(di)
(RMCEM)
Difference 2 (di2)
0 1 06120t23 07:30 07:59 1 t,473,000 10.821,600 651,400 424.321.960.000
1 2 06120123 08:07 08:36 11.245.000 10.877.200 367.800 13s.276.840.000
1 3 06120t23 08:43 09:12 11.02S.000 10.907.800 121.200 14.689.440.000
1 4 o6t20123 09:35 1O:04 10.948.000 1 .1 1 't .000 -163,000 26.569.000.000
,|5 o6t20t23 10:12 1O:41 11,297.000 11,247,400 49,600 2.460.160.000
,|6 06t20t23 10:48 11:17 11,019,000 1 'l ,196,200 -177,200 31.399.840.000
1 7 06120123 11:38 12:07 11.032.000 11,236,400 -204.400 41.779.360.000
1 8 06t20123 12:13 12:42 11.082.000 11.236.200 -1il.200 23.777.640.000
1 I 06120t23 12:50 13:19 'fi.270.000 11.235.800 34.200 1.169.640.000
1 10 06120123 13:40 14:09 11.282.000 11.242.OOO 0 0
n 9
(0.025)2.306
Mean Reference Method Value 11133777.778 RM avq
Mean CEM Value 11147777.778 UEM AVO
Sum of Differencer -126000.000 di
Mean Diffurence -14000.000 d
Sum of Differences Souared 277121920000.000 di2
Standard Deviation 185525.578 ed
]onfi de nce Coefficie nt 2.5o/o Enor 11 -Lail 142607.327
Relative Accurac!1.41 RA
Project No. M232512A
Main Kiln Stack
14 of '166 @Mostardi Platt
4.0 CERTIFIGATION
Mostardi Platt is pleased to have been of service to Ash Grove Cement Company. !f you have any
questions regarding this test report, please do not hesitate to contact us at 630-993-2100.
As the program manager, I hereby certify that this test report represents a true and accurate
summary of emissions test results and the methodologies employed to obtain those results. The
test program was performed in accordance with the test methods and the Mostardi Platt Quality
Manual, as applicable.
MOSTARDI PLATT
(al
"/= S{t- prosram Manaser
Richard J. Sollars ll
*J,w
Eric L. Ehlers
Project No. M2325124
Main Kiln Stack
Quality Assurance
15 of 166 @Mostardi Platt
APPENDICES
Project No. M2325124
Main Kiln Stack
'16 of 166 @Mostardi Platt
Appendix A - Test Section Diagrams
Project No. M2325124
Main Kiln Stack
17 of 166 @Mostardi Platt
GASEOUS TRAVERSE FOR ROUND DUCTS
(Oz, COz, NOx, CO, THC, Hg, HCI)
Project:Ash Grove Cement Company
Leamington Cement Plant
Leamington, Utah
Main Kiln Stack
June 20,2023
3
132 lnches
94.99 Square Feet
4.09
5.45
Length
> 1l2Dia.T
Length
> 2Dia.I
Test Location:
Test Date:
No. Sample Points:
Stack Diameter:
Stack Area:
Upstream Diameters:
Downstream
Diameters:
Project No. M2325124
Main Kiln Stack
18 of 166 OMostardi Plaft
EQUAL AREA TRAVERSE FOR ROUND DUGTS
(Volumetric Flow Rate)
Length
> 112Dia.T
Length
> 2Dia.I
Test Date:
Test Location:
Stack Diameter:
Stack Area:
Upstream Diameters:
Downstream Diameters:
Ash Grove Cement Company
Leamington Cement Plant
Leamington, Utah
June20,2023
Main Kiln Stack
132 lnches
94.99 Square Feet
4.09
5.45
Project No. M2325124
Main Kiln Stack
4
3
2
1 1234
1
2
3
4
@Mostardi Platt
Appendix B - Sample Train Diagrams
Project No. M232512A
Main Kiln Stack
20 of 166 @Mostardi Platt
7.62 cm (3 in.).
1.90-2.54 cm
(0.75 -1.0 in.).
Flexible
Tubing
(0.25 in.)
USEPA Method 2-Type S Pitot Tube Manometer Assembly
"Suggested (lnterference Free)
Pitot tube/ Thermocouple
Spacing
ATD-001 USEPA Method 2 Rev. 1.2 'U1t2021
Project No. M2325124
Main Kiln Stack
21 of 166 @Mostardi Platt
USEPA Method 4- Moisture Content Sample Train Diagram
Vacuum Gauge
ATD-032 USEPA Method 4
Project No. M232512A
Main Kiln Stack
Rev. 1.2
22 of '166 @Mostardi Platt
USEPA Methods 3A, 25A, and3201321 - Sample Train Diagram
r -+-- III5ffi1 I
lg:'J-
ATD-081C USEPA Method 3/2SA/320
Project No. M2325124
Main Kiln Stack
Rev.0.1
23 of 166
7/tl2O2t
@Mostardi Platt
USEPA Method 30B- Mercury Sorbent Trap Sampling Train
ATD-071 USEPA Method 308
Project No. M232512A
Main Kiln Stack
24 of 166 @Mostardi Platt
Appendix C - Galculation Nomenclature and Formulas
Project No. M232512A
Main Kiln Stack
25 of 166 OMostardi Platt
Cliont: Ash Grove Cement Company
Faclllty: Leamington Cement Plant
Prcleca*t M232512
Tost Lo€tlon: Main Kiln Stack
Oalet 6120123
FTIR Samole CalculaUons
Dircct Recovory % ot Calibr.lion Tmnsisr Standard
DRo= Dr x100
Cma
Cma- 100.2
DR6= 99.E%
Rocovory % with Calibration Transfer Standard Systom Purge
Rd= SYrd x 100
Dd
Syr*= 100.0
Rcn = 1OO'/.
Direct Recovory % of Analyte Spiko Gas
sF6
D&ir Ds x100
Cma
D&t' 96.7'/o
Dllutlon Factor for AnsMe Splking
DFr Spks
D6
Spkd. 0.3!t6
DF = 0.082
R.covery'/6 forAnah e Splko Wth HCI
&= sPk,
sp& = 2.8
DF = 0.082
MGtardi Platt
Project No. M232512A
Main Kiln Stack
Da= 100.0
Dor = 100.0
Do- 4.8
D.r= 4.833
&e 101.5
wherc:
DRd = Recovery % ofthe clibration transfer sbndard direcdy to the aml}rzs
Cma = certified @ncentrauon of clibratim gas, ppm
D6 = Concfibation of the calibraton tansfer standard gas dire€tly to the analfzer. ppm
&b. Recovery % of the callbration kansfer standard hrough the smpling q/Sm
Sysa = Concenbation ofthe clibration Earder standard gas through the system, ppm
DF . Dilution Factor of analyte spike gas
Spk.c r SF6 @nentrauon in effiuent during spiking
Spk, - 53y" -n."nb'afion in emuent during spiklng
Dq = Concentration of the analyte spike gas direcuy to tfie anatfzer, ppm
Ds r Concentration of the SF6 dkectly to the anal)raer, ppm
R, . Rtrorery % of the analyte spike gas
N, = NaWe effluent (HO) concentrauon prior to analyte spike
Nr=
Dq'29.1
v5.0
26 of 166
RATA Extractive 4/16/20
@Mostardi Platt
Client: Ash Grove Cement ComPany
Facility: Leamington Cement Plant
Project#: M232512
Test Location: Main Kiln Stack
Oale:6120123
Run: 1
Sample Calculations
( 11.30 o/o - 0.00 o/o) x
O2o/o (dry)
Lt.06 o/o
= 11.31 o/o
11.05 o/o - 0.00 o/o
THC ppmvd @ 7o/o 02
7.7 ppmvw / (1- 0.188) x ((20.9 -7.0)1Q0.9 - 11.3) = 13.7 THC ppmvd @7o/oO2
HCI ppmvd @ 7o/o 02
0.4 ppmvw / (1- 0.188) x ((20.9 - 7.0)l(20.9 - 11.3) = 0.7 HCI ppmvd @ 7o/o 02
NOx lb/hr
197.6 NOx ppm x (1.194*E10^-7) x 11473000 = 270.63 NOx lb/hr
SO2lb/hr
0.2 SO2 ppm x (1.66*E10^-7) x 11473000 = 0.40 SO2 lb/hr
CO lb/hr
1,021.0 CO ppm x (7.266*E10^-8) x 11473000 = 851.15 CO lb/hr
Q*=(C-Q) x C,"
C,-Co
where:
Q", = Effluent gas concentration, dry basis, ppm or 0/o
C = Average gas concentration indicated by gas analyzer, dry basis, ppm or o/o
Q = Average of initial and final system calibration bias check responses for the zero gas, ppm or 0/o
C, = Average of initital and final system calibration bias check responses for the upscale calibration gas, ppm or 7o
C,a = Actual concentration ofthe upscale calibration gas, ppm or o/o
Mostardi Plaft
Project No. M2325124
Main Kiln Stack
v5.0
27 ot 166
RATA Extractive 41 16120
oMostardi Platt
Volumetric Flow Rate
Client: Ash Grove Cement Company
Plant Leamington Cement Plant
Location: Main Kiln Stack
Run: Normal Load, Run 1
Date: 06120123
Moisture Content
Bws = e' - AP (t-t')
P
where: e' = saturated vapor pressure of water, in. Hg,
at the wet bulb temperature, t'
A = 3.67 x 10-4(1+0.00064 (t'-32))
P = absolute pressure/ in. Hg, in the duct
t = dry bulb temperature, oF
t'= wet bulb temperature,oF
Bws = 0.188
Dry Molecular Weight
Md=0.44x(o/oCoj + 0.32x(o/ooj + 0.28xoloN2
o/oCO2 = 15.6 o/oO2= 11.3 o/oN2 = 73.1
Md = 30.95
Wet Molecular Weight
Ms = Md x (1-Bws) + (18.0 x Bws)
Md = 30.95 Bws = 0.188
Ms = 28.51
Average Duct Velocity
Vs = 85.49 x Cp x Sqrt AP (avg) x (Ts (avg) + 460/ (Ps x Ms))1/2
Cp = 0.840 Ts (avg) = 206.6 Sqrt AP avg: 0.736
Ps = 24.84 Ms = 28.51
Vs = 51.25
Volumetric Flow Rate
Q (Actual Basis)= Vs x A x 60
vs= 51.25 [= 95.030
Q= 292,229 acfm
Qs (Standard Basis;= t7.647 x a x Ps
460 + Ts (avg)
Q = 292,229 Ps = @ Ts (avg) = 206.6
Qs = 19&170 scfm
Qs (Standard Basis)= scfm x 60 min/hr
Qs = 11,530,221 sdtr
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
vl3.1
28 of 166
11t6t2020
OMostardi Platt
Mercury Meter Volume at Standard Conditions (Liters)
Pbar
Vm=
Tm=
Tm
30.026
517.67
25.436
(ng of Hg /1xl0e) x (0.002046226/Vm(std)*0.0353)"385x1061200.59*1000
15.4 Vm(std) =25.435792
0.073
(total ng of Hg on trap/l000)/Vm(std)/1000
0.605
ug/dscm*(1-Bws)
0.491
B = (ng ofsection 2 / ng ofsection 1) x 100
l= 2.67%
Paired Trap Agreement:
RD=
RD=
Test Location: Main Kiln Stack
Glient:
Plant:
Run:
Date:
Vm(std) =
Vm(std) =
Hg Concentration:
PPb Hg =
Total ng Hg =
ppb Hg =
ug/dscm =
ug/dscm =
ug/wscm =
ug/wscm =
% Breakthrough:
FT-008 Hg Template
Project No. M2325124
Main Kiln Stack
Ash Grove Cement Company
Leamington Cement Plant
1A
6t2012023
17.647xYxVmx
f = 0.996
v5.0
29 of 166
10131117
@Mostardi Platt
ontraoa-total of
0.9 %
MOSTARDI PLATT
Method 30B Determination of Vapor Phase Mercury Nomenclature
B = Breakthrough (%).
Bws = Moisture content of sample gas as measured by Method 4, percenV1OO.
Ca = Concentration of Hg for the sample collection period, for sorbent trap "a" (pg/dscm).
Cb = Concentration of Hg for the sample collection period, for sorbent trap "b"(pg/dscm).
Cd = Hg concentration, dry basis (pg/dscm).
Crec = Concentration of spiked compound measured (pg/m3).
Cw = Hg concentration, wet basis (pg/m3).
m1 = Mass of Hg measured on sorbent trap section 1 (pg).
m2 = Mass of Hg measured on sorbent trap section 2 (pg).
mrecovered= Mass of spiked Hg recovered in Analytical Bias or Field Recovery Test (pg).
ms = Total mass of Hg measured on spiked trap in Field Recovery Test (pg).
mspiked = Mass of Hg spiked in Analytical Bias or Field Recovery Test (pg).
mu = Total mass of Hg measured on unspiked trap in Field Recovery Test (pg).
R = Percentage of spiked mass recovered (%).
RD = Relative deviation between the Hg concentrations from traps "a" and "b" (7o).
vs = Volume of gas sampled, spiked trap in Field Recovery Test (dscm).
Vt = Total volume of dry gas metered during the collection period (dscm); for the purposes of
this method, standard temperature and pressure are defined as 20" C and 760 mm Hg,
respectively.
vu = Volume of gas sampled, unspiked trap in Field Recovery Test (dscm).
CN&F-043 308 Nomenclature Rev. 1.2 1l'U2021
Project No. M232512A
Main Kiln Stack
30 of 166 @Mostardi Platt
MOSTARDI PLATT
Volumetric Air FIow Calculations
vm (std) = 17 .647 x vm xl%P-l "'
Vw (std) = 0.047LxVlc
r Vw (std\ IBws=lffia*n*r"all
Md = (0.44xo/oC}) + (0.32 x0/oO2) + [0.28 x (100 -o/oC)z-o/o0)]
Ms : Md x (1- Bws) + (18 x Bws)
(rs + a60)
MsxPs x tlDF x Cp x 85.49
Acfm = 7s x Area(of stack or duct) x 60
Scfm: AcfmxL7.647 t [nufu]
mtn
Scf h -- Scfm x 60 ttr
Dscfm=Scfmx(1-Bws)
CN&F-031 Volumetric Flow Calcs
Project No. M2325124
Main Kiln Stack
Rev. 1.2 1t112021
31 of 166 @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)
DH= Static pressure of gas, in.H2O
Ps = Absolute pressure of gas, in. Hg = Pbar + Pg
Pstd = Standard absolute pressure, 29.92 in. Hg
Acfm = Actual volumetric gas flow rate
Scfm= Volumetric gas flow rate, corrected to standard conditions
Dscfm = Standard volumetric flow rate, corrected to dry conditions
R = ldeal gas constant, 21.85 in. Hg-ft3/'R-lb-mole
Ts = Average stack gas temperature, 'F
Tm = Average dry gas meter temperature, oF
Tstd = Standard absolute temperature, 528"R
vs = Gas velocity, fUsec
Vm(std)= Volume of gas sampled, corrected to standard conditions, scf
Vw(std) = Volume of water vapor in gas sample, corrected to standard conditions, scf
Vlc= Volume of liquid collected
Y = Dry gas meter calibration factor
Ap = Velocity head of gas, in. H2O
K1 = 17.647 'R/in. Hg
o/oEA = Percent excess air
%COz = Percent carbon dioxide by volume, dry basis
o/oO2 = Percent oxygen by volume, dry basis
%N2 = Percent nitrogen by volume, dry basis
0.264 = Ratio of 02 to N2 in air, v/v
0.28 = Molecular weight of N2 or CO, divided by 100
0.32= Molecularweight of 02 divided by 100
0.44 = Molecular weight of CO2 divided by 100
13.6 = Specific gravity of mercury (Hg)
CN&F-024 Nomenclature Pitot Rev. 1.2 1t1t2021
Project No. M2325124
Main Kiln Stack
32 of 166 OMostardi Platt
MOSTARDI PLATT
Pollutant Concentration CorrectionToh for Percent Orygen
20.9 - 70/o
uadj - Ld
20.9 - o/o02
where:
C"oi = Pollutant concentration corrected to percent Oz
20.9 -7o/o = Percent Oz, the defined Oz correction value, percent
20.9 = Percent Oz in air
o/oO2= Measured Oz concefltration dry basis, percent
Co = Pollutant concentration measured, dry basis, ppm.
CN&F-007 Correction of Pollutant to %O2 Rev.2.2 1t1t2021
Project No. M2325124
Main Kiln Stack
33 of 166 @Mostardi Platt
1.
2.
3.
4.
5.
MOSTARDI PLATT
ppmv to lb/hr Conversion Calculations
- lbs /SO"ppm 502 x 1.660 x L0-' = +scI
lbs SOz scf 60 min lbs SO2
scf min hr hr
- lbs/NO-"ppmNOrxl.t94x10-l=#scl
lbs NO* scf 60 min lbs NO,
scf min hr hr
^ lbs/COppmCO x7.266 x 10-u scf
lbs CO scf 60 min lbs CO
scf min hr hr
- lbsC"H"ppm qHs x 1.742 x 10-/ = --#scI
lbs qHs scf 60 min lbs CsHs
scf min hr hr
- lbs /CH^ppmCHax4.164x10-u =
-
scl
lbs CHa scf 60 mtn lbs CHav_v_scf min hr hr
ppmNMHC as C3Hsx9.3427 X 10-8 =
lbs C lbsscf 60 min lbs C
-v
v_scf min hr hr
lbs C
trf6.
CN&F-028 ppmv to lb per hr conv form
Project No. M232512A
Main Kiln Stack
Rev. '1.2 1t1t2021
34 of 166 @Mostardi Platt
MOSTARDI PLATT
Relative Accuracy Test Audit (RATA) Calculations
Mean Difference
IL1st4=_) di
TL /-t
i=1
Standard Deviation
,o=l-"'q;ff|'''
Sd
l,u - Lo,g75-
vn
Gonfidence Goefficient
Relative Accuracv
*=Wx1oo
CN&F-029 Part 60 RA Calcs Rev. 1.2
35 of 166
1n/2421
@Mostardi PlattProject No. M2325124
Main Kiln Stack
Appendix D - Reference Method Test Data
Project No. M232512A
Main Kiln Stack
36 of 166 OMostardi Platt
NN
,(E
=(LTLE<Etso<od=
@
lEtr.ECL(! ElEE.u
Es=io -(, ll,()6:=I E,t EI E= EEJ P
l
ootIlt
ooo-
(f)i..
sf_
ooo-
rosfo{
ooo-
o)(\lo-
ooq
@to)o
ooo
'riO)N"
ooortF-
o)-o
oo
c>_
N(.,o-
ooo_
(\t
@o_
ooqot-N.
ooo-
N@o{
s
o
:,
,9o
=
s*q
@
so)ao)
s
ro
ot
slr)ao)
soao)
s
O)ro
ot
sro
c?
o)
ssf(o
ot
s
@|r)
ot
sono,
@.,
6EoE ESo. t-
.L
\o a?o lt)
ci \o ao qo (.o
ci c;o qo
t,> c.lEO
C-ao.a
HeF
Nri o?o (o
<'i
c?
(')
q
CO
c?
(f)
q
(t,
ol
c\t
(o
ai
N
N
i
Eoo
o
IF
t-
F-c,N
l.-
ro
F-
ro
t-
it
l'-
ro
F.
(f,
l-at-o
F-
ilI c,{
O)
s
o
a?
o)
q
o,Io o (\
o
Co o)
q
O)
S6
NOo3o-
F-
6i
C
6
q
c\l
u?
N
rJ)
c.i
ro
6i
lr)
6,i
ro
c.i
u?
N
ro
N
.C
s
oo
roI
lo
@
('jq€
@o
oG oc?
sf
@
N
a?
slN$
N\
ro
(f,
o)
d(0
(f)
N
u?tF-(o
lr)
u?
(ooro
F.
o?
\tt
.ct
xoz
(oq
F-N
N\o,NN
o
dIrN
$\lr,loN
@qo@N
$c\l
slt\N
q
(Y)(o
N
o
e.i(o
N
c\tq
(.,
@N
!r)I
(oN
,
Eoo
oo
6to
cod@
\(Y'
ro
N
od@t
ol
F.t-r.()
I
rtt
(od|f)ltt
d(o{
(od
(o
-q
@
(f)
tr)
5Ezd
q
Fo,
c?ooN
\o)oN
q
loo,
oq
N
O)
cot-oN
c;
(\,t
@
O)
o?o
N
o?
(o
o)
o
E
F
tE
UJ
o,lr)
r-
@(r,(;
C\
o
tIo sfo
F.F-9(\t
c\I(\
o,
fi
o)I$
o
E
t(!
o
oq?
I-
F-I
@
(isc
!o(.)
o;
N
o
@to
@e (9
N
orr)
N
os
(f)
o
a!a
(f)No6loN
@
(f)(\toc\to(\I
(o
(\
Cnc(\
G
r,NoNo(\t
6
(oNoNo(\l
(o
(f)NoNoN
(o
(o(\to6loN
(o
C(\c6
(\
(l
C(\
C
C\c(\
(c
(f)NoNoN(o
pi (\(i s 6 (o t\d o o
@(o
Oeri=>:
(?,
N
ta)N(')-N7i>EooEz=
= o!r (Da
! 9(E(5 L=
ao
Ns
=dts
EE<EFL<(Et-ao
(9it>t
EI
=IOoANOS F r @ r @@@6o FNN F@FO-OON O OOrilo{ o{ q \ .: q q n I q c':':': q q? q \ \ a? oq n q u?': oq u? n 9 a
* gf--@ @o@ @o @@6@@NroN NtsN NN @N@@ @@@ N
oit
oN
EE
d lloooo ooo ooo ooooooooo ooooooooooo-:c? c? a?.q a a? - c! ol a c? a,: q.: a? a? qq a2 c q q u? a c?.t a u? q? 1xt F F -
ol
(o(o
o-
9borJ
u
G
6ot
tsr
cq-
E6o-
!Cqq
Eo X.qo H
oot a
: -oN c
5EnY8
PJSSS
:5# i.!io=;-9 Ga$ $E"rJ
oF
N
1r)
No-Ni
=Eou)zcs .i3Y
_qo-4o;Et=g
o
NN
s
tr6
EE<E
#f;o
olt>t
El - - - o N + @ o !Q \ x N o o + o o @ @ $ N @ o @ N 6 o o @ @9{6 a F @ di ri 6 6 \9 q.l o ci @ N cO @ o o o N o o o o o @ N F N o
* g"la - r{ F d d d * 3 R oi @i ci ci <i d <j o o @ d d d d <t d @ @ @ @
ofl
oN
EE;Eloooooo oooooo ooo aoooooooa0ooooo-qN'b6@@a @N F oo; oots ts -oo@ooo@otsN@o@:sl- -,j - - - - - d - 6i 6i 6i - - - ni - - - - - 6i - 6i - - - - -Bl---
(o(o
oFgb
o)(a
N
3t
o
Got
tsL
c
EOOFo:
tCcootrEo I39 Eob o
(5 ERYN
;:YN 6N{i>>b
# 5# i.uo=;.9 oE$bE"
rJ
oF
N
lr)
N(Ov
N;>E
oa2C
E tj=
-Q o-c 6'=
E i=g
o
Ns
o.E
f,E<E
k(E
LA o
o
=t>t
EI
=l- @ @o N o@OOts NVNFNN O SOFON ON oOO F@
dq a c? \': q q \ R a q q \ q c? \ oj c? \ a? .: .: e? I q c? r? q c
!?]*
- ts ts@@@@ @N NN@N66 6NNN N6No@ts ts@@
:FroN
EE
dEloooooo ooooo oooooooo oooooooo oo- YC q 0q q? q q \ q q q u? q o! q q q \ q a q ol a? a s? c? a a s? q
xtFFF ---N
ol
t
G
Go
dFL
6
EO
3E
!Etrooc
-QO H
ob a
:6,N c
.i.E'bVI?I CN -\
?.{SES
t >* e oo=-.9G
6 E TE "
rJ
ooF
@(oord=>U
$
N
lo
N
N7i>E
aA
7C
E 6v-9 or: 9'6P d>g
o
Nqs
E6IE<E
#go
oit>t
El-- *No6oNNo6o@No@ <s F 6N@tsNrN oFNFxlg q \ q q q.: a q q a o? q c! q a.: q q q q q \ - q 9': q q a
*Cl* *NFN ts @o@@6@o@oo@6 @oN@b NN@@6NN
oil
oN
EA;rloo oooo ooooooooo ooooooooooooooo- <{oF +oN- F- oo$NoONNoN oNoNN --- O-No
Sl - F ? - F - O F F -l,l- - -ol
@tF
o.!
(o(o
oF
9b
t
!d
G
6on
FL
c6
EOo;
rCcootr
Eo Y39 Eob ct,
o Ell:s
; \YN GNii=>a
t 5# i.uo=;.9 (
E E iE "
AJ
oF
N
lr)N(?)v
Ni>E;a
r 6!-Q o.l -10'aPd>
.E
NN
a(6
Id<E
k(u
LA
oit
Elo- =o so@o@F oNNoooooo Nao@ N s s o sN o5.: c! a': e? .: q - q q q q q c? q u? q q \ c? \ \ q a .: q? c! a \,:
* g]*-@N N N NF@N AN@tstsN@@N NN6ts ts@N @ NO@
otl
oN
EiJ
Sllooo ooo ooooo a oooc ooooaoaaaaoooo-:c! c a? c!,.,. c! c!,: n n -.:61 c! e? q q c? g o? - c! a c! 6l c! c?': e?
i<lr r r F o E r
NIol
(o(o
or
9b
Ns
o
t
G
oot
Fr
qP=
to.aE
-ccoqFE6 {.qo Hob u)
> J-N C
5 EnY{
;:!N 6N{i>>D
t5#ii.{o=x.!46
5 E.iE oqy6
CJ
noF
N
(o
c{r)-N?i>E
oazs
= 6Yso-4'6-'=
E i=
E
o
=
NN
s
dE
Ed<E
fip.o
oil
El--*o oN o o tsoo < or @ F s@ r tsNo voo@ - NN
Hq $.c? q a q q a \ qutq.. q q \ qq q \ \ \\ \ a \ a'. s?
-S,ilNNoN tsts ts @ ts tsNNN@N NNF tsF ts@ @ @N ts@FN
6=totl
oN
EA;Blooooooo oooo oooo oooaooooo0o ooo- iq q q r c! C - c?.! ol c! ol c?.\ q q q C c,l c? c! a q q \ q q u? q
>sl- - -*l---ol
o
t
o
6o
E
FL
ca-
Edo^-():
dCcooc
F.ql txv 6
:ENS
5 EnY{
;:YN oN<i>>6t tr# i.uo=ti-Yo
EE $E"o.J
ooF
(o
@
oe
e=>v (flt
N
lr)
N(.)v
N7i>E
ci 0)
7C
r E9-Eo:-0- 6'.;Et5g
o
NN
s
tr6I o--<E
dGd6o
oit>t
EI:lN@O@ Ot @OOF o oOF NO oN 6 NO@@ON@ F6O
d9 q a .. a? ..1 c! q o? c? q c! a .: .,1 cj q \ \ q a,: \ \ \ \ ol c q
{l gl-* Fts tsts N NN N NNNNNN NN N N NNN NN NN6o
oil
oN
Efl
<llooo oooa a a ooo ooooooooooooooooo--lN @o N Ots @@ S 6N6o@t $ $oNoNONNON rNN
o\lr r -
ol
ts
d
o
6ot
Fr
6
E6
6E
coocEO I,qo H
: -oN c
5 ERYS
;:YN 6N<:>>a
iiEr#!Eo=ti.go6E6E"
o.J
oF
@(o
oFgb
$<t
N
|r)
N
(f)
-N;i>E;a
r 69!o-r o.;Et=g
N!
qEId<E
kGd-a
o
oO@-tsO@Oo@oO@-N@oNOONF@ONNO-OON;*NO$$$NOOOO@OtsONNN@FNtstsNNNNtstsNNtstsNNNFtsNN
oooooooooaaooooooaaooooo
-'. q * c! a? q q q c!.:.q 9 q q q a? 6? n':.: q ol qa
il
El - - o - -xlo o o o o
S;lci@<t@d
?ir
8.
EAd !l o o o o o
-9NoFFo
sl '_ - - - -
ol
(o
@
oF
9blr)$
(
do
E,
Fr
C6
E6.sd
-ccooctro +Xv 6
ob a
: -oN c
5 EpY&
;:!N 6N<i>>aii5#!r@='i.!ao6&tE"
a-J
oF
N
lr)N(t-Ni>E
oa7C
r ii?!or1p.8po->
g
o
Nq
trtId<EFL#g
o!t>t
Elra oe o@ os@@@ NFoaN @ s N ooF r@-r @@NHu? q 9 -t n,: a? .! q q a? u.l a u? u.l a a c? q s? q 1 a q q a 1 a a
*|9I**
NN N tsNts NN NNNNN N NN N N NN NN N N N NN
oil
oN
EEi€loooooo oo ooo ooooo ooo ooooaooooo- :\ o? q a? q a c? a c? c? c? u? a c? c!': c? a u'l v? a? o? q c? e? q c? 9 .::<lo o -
ol
@(o
oF
9b
@t
o
ft
G
ottrL
cq-
bo
3E,ccoocEo I39 Eob a
EE'E={
PESSS: 5# i.uo=;-!ao
3 E TE "
GJ
F
N
lr)
N(.)vSE2S
du)2C
s E9-qo-a d'=E i=
.E
NN
s
EEf,E<tFL<(E
LA o
(a
oaoNq.!c?ry
NNFN
ooooqac?c!
N
]l
El*-- Fr 66@ o@FN@ rNs@Nots-@Ns9{O@ O O N N F n - F F O ts @ O OO@ N S O @ O O
o slrcidN tsN d@ tsFN N N ts o<i ii@@tsN dNE9loit
oN
EA<qqqqqqqqEBqqqq?Eqq?aEeqEq
Sl- - e- t- - -NIot
o
,
d,
o
oo
dFL
ii=EEoio:eCcooc
EO ;39 Eob o
:ENc
5 Ee:8
P}SSSi 5# !.uo=;.:ao6$BE"
o-J
6oF
(o(o
oFri!>UFt
N
tr)
NRx>5
oa7C
r ijY,Q oaI O'6E o->G
o
Glient:
Facility:
Test Location:
Project #:
Test Method:
Test Engineer:
Test Technician:
Temp lD:
Meter lD:
Pitot lD:
Pitot Type:
Pitot Tube Coefficient:
Probe Length:
Sample Plane:
Port Length:
Port Size (diameter):
Port Type:
Duct Shape:
Diameter:
Duct Area:
Upstream Diameters:
Downstream Diameters:
Number of Ports Sampled:
Number of Points per Port:
Total Number of Traverse Points:
Operating Level:
Moisture Balance lD:
Stack Liner Material:
Default WAF:
Type of WAF Applied:
ActualWAF Applied to all runs:
Point Markings (including port length):
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
M232512
2 (RArA)
TWM
BAA
F4
F4
4036
S-Type
0.84
8.0
Horizontal
7.00
6.00
FIange
Circular
11
95.03
4.100
5.500
4
4
16
Normal
FTIR
S
0.995
D
0.995
Point #
1
2
3
4
tn.
ln.
lnches
11.224
20.86
32.608
49.636
ft
Sq. Ft.
11t6t2020
@Mostardi Platt
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
v13.1
48 of 166
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
I
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
1
6t20t2023
7:30
7:59
TWM Test Tech: BM
7
Port Point
11
12
13
14
DP
(in. H2O)
0.58
0.63
0.55
0.35
Sqrt.
DP
0.7616
0.7937
0.7416
0.5916
Temp
("F)
208.0
209.0
208.0
207.0
Veloclty
M
53.12
55.40
51.73
41.23
55.94
53.90
55.32
47.82
Point
1
2
3
4
DP
(in. H2O)
0.58
0.55
0.51
0.40
0.63
0.60
0.57
0.42
Sqrt.
DP
0.7616
0.7416
0.7141
0.6325
0.7937
0.7746
0.7550
0.6481
292,229
'155,965
192,170
11,530,221
11.472,570
Port
3
3
3
3
Temp Velocity
fF) (v)
202.0 52.88
206.0 51.65
207.0 49.77
207.0 44.08
0.65
0.60
0.63
0.47
0.8062
0.7746
0.7937
0.6856
Test Parameters
P6", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
! - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M2325124
Main Kiln Stack
2
2
2
2
1
2
3
4
201.0
205.0
207.0
208.O
o/o CO2 15.60
o/o 02 11.30
% Nz 73.10
Md - dry basis lb/lb mole 30.95
Ms - wet basis lbilb mole 28.509
Bws . Moisture content fraction
Moisture determined by wb/db?
55.32
54.03
52.66
45.17
't1t6t2020
@Mostardi Platt
4
4
4
4
,|
2
3
4
207.0
208.0
208.0
207.0
24.88
-0.60
24.84
206.6
Circular
11
95.03
0.5450
0.7356
51.252
0.'t884
N
O -ACFM
Qsd - DSCFM
Os - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
v13.1
49 of 166
METHOO 2 VOLUMETRIC FLOW DATA
Proiect Number:
Glient:
Facility:
Test Location:
Pitot lD:
Pitot Goefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
8
Operating Level:
Run No,:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
2
6t2012023
8:07
8:36
TWM TestTech: BAA
7
Port Point
11
12
13
14
DP
(in. H2O)
0.57
0.59
0.46
0.35
0.61
0.58
0.52
0.44
Sqrt.
DP
0.7550
0.7681
o.6782
0.5916
Temp
(oF)
207.0
208.0
208.0
203.0
206.0
207.0
207.0
206.0
Veloclty
M
52.65
53.60
47.33
41.13
54.42
53.11
50.29
46.22
DP
(in. H2O)
0.58
0.55
0.45
0.37
Sqrt.
DP
0.7616
0.7416
0.6708
0.6083
0.7937
o.7874
0.7550
0.6928
286,508
151,645
188,356
't't,301,u2
11,244,83s
285,O76
1
2
3
4
0.7810
0.7616
0.7211
0.6633
Test Parameters
P6"r - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
I
2
3
4
4
4
4
4
2
2
2
2
Port Point
31
32
33
34
0.63
0.62
0.57
0.48
Q - ACFM
Qsd. DSCFM
Qs - SCFM
Os - SCFH
Qs - WAF adjusted SCFH
Q - WAF adjusted ACFM
Temp Velocity
fF) M
205.0 53.03
206.0 51.68
208.0 46.81
207.0 42.42
207.0
208.0
208.0
207.0
55.35
54.95
52.69
48.31
11t6t2020
@Mostardi Platt
24.88
-0.60
24.84
206.8
Circular
11
95.03
0.5231
0.7207
50.249
o/o CO2 15.90
o/o 02 11.70
% Nz 72.40
Md - dry basis lb/lb mole 31.01
Ms - wet basis lb/lb mole 28.476
Bws - Moisture content fraction 0.1949
Moisture determined by wb/db (Y or N) N
v13.1
50 of 156
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
8
Operating Level:
Run No,:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
3
6t20t2023
8:43
9:12
TWM TestTech: BAA
7
Port Point
't1
12
13
14
DP
(ln. HrO)
0.61
0.58
0.54
0.33
0.57
0.55
0.53
0.43
Sqrt.
DP
0.7810
0.7616
0.7348
0.5745
Temp
("F)
208.0
208.0
208.0
203.0
Velocity
(v)
54.51
53.15
51.29
39.94
52.58
51.72
50.81
45.70
DP
(in. H2O)
0.57
0.54
0.46
0.37
Sqrt.
DP
0.7550
0.7348
0.6782
0.6083
0.7681
0.7483
0.6928
0.5916
281,054
148,694
184,736
11,084,133
11,028,713
279,649
2
2
2
2
0.7550
0_7416
0.7280
0.6557
Test Parameters
P6", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t" - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M2325124
Main Kiln Stack
1
2
3
4
4
4
4
4
1
2
3
4
205.0
207.0
208.0
206.0
Port Point
31
32
33
34
0.59
0.56
0.48
0.35
O - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
Q - WAF adjusted ACFM
Temp Velocity
('F) (v)
208.0 52.69
208.0 51.29
208.0 47.U
207.0 42.42
208.0
208.0
208.0
202.0
53.61
52.23
48.36
41.',t1
11t6t2020
@Mostardi Platt
24.88
-0.60
24.84
206.9
Circular
11
95.03
0.5038
0.7068
49.292
% co2 15.90
Yo Oz 11.60
% Nz 72.50
Md - dry basis lb/lb mole 31.01
Ms - wet basis lbilb mole 28.470
Bws - Moisture content fraction 0,1951
Moisture determined by wb/db (Y or N) N
v1 3.1
51 of 166
METHOD 2 VOLUMETRIC FLOW DATA
Project Numberz M232512 Operating Level: Normal
Client: Ash Grove Cement Company Run No.: 4
Facility: Leamington Cement Plant T6st Dat6: 612012023
Test Location: Main Kiln Stack Start Time: 9:35
Pitot lD: 4036 End Time: 10:04
Pitot Coefficient: 0.840 Test Engineer: TWM Test Tech: BM
Probe Length, Feet: 8 Port Length, lnches: 7
DP Sqrt. Temp Velocity DP Sqrt. Temp Velocity
Port Point (in. H2O) DP CF) M Port Point (in. H2O) DP fF) M
1 ',t 0.59 0.7681 209.0 53.70 3 I 0.59 0.7681 208.0 53.66
1 2 0.56 0.7483 209.0 52.32 3 2 0.52 0.7211 210.0 50.46
1 3 0.47 0.6856 209.0 47.93 3 3 0.48 0.6928 210.0 48.48
1 4 0.30 0.5477 202.0 38.09 3 4 0.40 0.6325 209.0 44.22
2 1 0.62 0.7874 205.0 54.83 4 1 0.60 0.7746 208.0 54.'t2
2 2 0.56 0.7483 208.0 52.28 4 2 0.52 0.7211 209.0 50.42
2 3 0.52 0.7211 209.0 50.42 4 3 0.50 0.7071 210.0 49.48
2 4 0.37 0.6083 202.0 42.31 4 4 0.35 0.5916 208.0 41.33
Test Parameters
Po,, - Barometric pressure, inches Hg 24.88 o/o CO2 15.50
Pn - Stack Pressure, inches of H2O -0.60 o/o 02 11.20
P" - Absolute stack pressure, inches Hg 24.84 % Nz 73.30
t" - Average stack temperature, oF 207.8 Md - dry basis lb/lb mole 30.93
Duct Shape: Circular Ms - wet basis lb/lb mole 28.4'14
Diameter, Feet 11
Bws - Moisture content fraction 0.1945
cross sectional Area of stack, Ft2 95.03 Moisture determined by wb/db (y or N) N
Method 2 Resuhs
Average DP 0.4969 Q - ACFM 279,399
Average Sqrt DP 0.7015 Qsd - DSCFM 147,720
Average Velocity Vs (fUsec) 49.002 Qs - SCFM 183,389
Os-SCFH 11,003,364
Qs - WAF adjusted SCFH 10,948,348
Q - WAF adjusted ACFM 278p02
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
v13.'l
52 of 166
11t6t2020
@Mostardi Plaft
METHOD 2 VOLUMETRIC FLOW DATA
Proiect Number:
Glient:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
8
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
5
6t20t2023
10:12
10:41
TWM TestTech: BAA
7
Port Point
11
12
t3
14
1
2
3
4
DP
(in. HrO)
0.58
0.60
0.54
0.36
Sqrt.
DP
0.7616
0.7746
0.7348
0.6000
Temp
cF)
210.0
210.0
210.0
203.O
209.0
209.0
209.0
205.0
Veloclty
(v)
53.29
54.20
51.42
41.76
54.16
53.25
52.32
42.97
DP
(in. H2O)
0.56
0.60
0.52
0.37
4
4
4
4
2
2
2
2
Port Point
31
32
33
34
1
2
3
4
0.58
0.61
0.59
0.42
Q - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
Q - WAF adjusted ACFM
Sgrt.
DP
0.7483
0.7746
0.7211
0.6083
0.76't6
0.7810
0.7681
0.6481
288,397
152,420
189,225
11,353,482
1',t,296,714
286,955
Temp Velocity
fF) (v)
207.0 52.24
208.0 54.12
209.0 50.42
206.0 42.43
208.0
209.0
209.0
208.O
0.60
0.58
0.56
0.38
0.7746
0.76't6
0.7483
0.6164
Test Parameters
Pp", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H20
P" - Absolute stack pressure, inches Hg
t" - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area ofStack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M2325124
Main Kiln Stack
24.88
-0.60
24.84
208.1
Circular
11
95.03
0.5281
0.7239
50.s80
o/o CO2 15.50
o/o 02 11.20
o/o N2 73.30
Md - dry basis lb/lb mole 30.93
Ms - wet basis lb/lb mole 28.414
Bws - Moisture content fraction 0'1945
Moisture determined by wb/db (Y or N) N
53.21
54.61
53.70
45.28
1'16t2020
@Mostardi Platt
vl3. t
53 of 166
METHOD 2 VOLUMETRIC FLOW DATA
Project Number: M232512 Operating Level: Normal
Client: Ash Grove Cement Company Run No.: 6
Facility: Leamington Cement Plant Test Date: 612012023
Test Location: Main Kiln Stack Start Time: 10:48
Pitot lD: 4036 End Time: 'l'l:'17
Pitot Coefficient: 0.840 Test Engineer: TWM Test Tech: BAA
Probe Length, Feet: 8 Port Length, lnches: 7
DP Sqrt. Temp Velocity DP Sqrt. Temp Vetoclty
Port Polnt (in. H2O) OP fF) M porr poinr (in. HrO) Dp ('F) M
1 1 0.60 0.7746 210.0 54.21 3 I 0.59 0.768.t 209.0 53.72
1 2 0.58 0.7616 210.0 53.30 3 2 0.55 0.7416 210.0 51.90
, 3 0.54 0.7348 210.0 51.43 3 3 0.47 0.6856 210.0 47.98
1 4 0.33 0.5745 208.0 40.14 3 4 0.26 0.5099 200.0 35.42
2 1 0.57 0.7550 209.0 52.80 4 I 0.60 0.7746 205.0 54.01
2 2 0.57 0.7550 209.0 52.80 4 2 0.63 0.7937 209.0 55.51
2 3 0.54 0.7348 209.0 51.39 4 3 0.52 0.7211 209.0 50.43
2 4 0.34 0.5831 200.0 40.50 4 4 0.39 0.6245 206.0 43.58
Test Parameters
Ps", - Barometric pressure, inches Hg 24.88 o/o CO2 15.50
Pn - Stack Pressure, inches of H2O -0.60 o/o 02 1 1.30
P" - Absolute stack pressure, inches Hg 24.84 % Nz 73.20
t - Average stack temperature, oF 207.7 Md - dry basis lb/lb mole 30.93
Duct Shape: Circular Ms - wet basis lb/lb mole 28.399
Diameter, Feet 11
Bws - Moisture content fraction 0.1959
cross sectional Area of stack, Ft2 95.03 Moisture determined by wb/db (y or N) N
Method 2 Results
Average DP 0.5050 Q - ACFM 2A1j57
Average Sqrt DP 0.7058 Osd - DSCFM 148,419
Average Velocity Vs (fusec) 49.310 Qs - SCFM 1U,578
Qs - SCFH 'l 1,074,696
Qs - WAF adjusted SCFH I 1 ,019,323
Q - WAF adjusted ACFM 279,752
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
v13.1
54 of 166
11t6t2020
@Mostardi Platt
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
8
Temp
("F)
210.0
210.0
2',t0.0
206.0
208.0
209.0
210.0
207.0
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
7
6120t2023
11:38
12:37
TWM TestTech: BAA
7
Port Point
11
12
l3
14
Sqrt.
DP
0.7874
0.76'16
0.7000
0.5831
1
2
3
4
0.62
0.58
0.60
0.36
0.7874
0.7616
0.7746
0.6000
Test Parameters
P6", - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
P, - Absolute stiack pressure, inches Hg
L - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M2325124
Main Kiln Stack
2
2
2
2
DP
(in. H2O)
0.62
0.58
0.49
0.34
Velocity
(v)
55.07
53.27
48.96
40.66
54.99
53.23
54.1 8
41.87
DP
(in. H2O)
0.57
o.52
0.48
0.27
Port Point
31
32
33
34
0.60
0.55
0.55
0.38
O - ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
O - WAF adjusted ACFM
Sqrt.
DP
0.7550
0.7211
0.6928
0.5196
0.7746
0.7416
0.7416
0.6164
281,791
149,031
1U,787
11,087,216
1 I ,031,780
280,382
Temp Velocity
fF) (v)
208.0 52.73
211.0 50.48
211.0 48.50
200.0 36.07
209.0
210.O
210.0
206.0
24.88
-0.60
24.84
208.4
Circular
1'.!
95.03
0.5069
0.7074
49.421
4
4
4
4
1
2
3
4
o/o CO2 15.50
o/o 02 11.40
% Nz 73.10
Md - dry basis lb/lb mole 30.94
Ms - wet basis lb/lb mole 28.433
Bws . Moisture content fraction 0.1935
Moisture determined by wb/db (Y or N) N
54.14
51.87
51.87
42.95
11t6t2020
@Mostardi Platt
v13.1
55 of 166
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
8
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
8
6t20t2023
12:'13
12:42
TWM TestTech: BAA
7
Port Point
11
12
13
11
,|
2
3
4
DP
(ln. H2O)
0.60
0.58
0.55
0.43
Sqrt.
DP
o.7746
0.7616
0.7416
0.6557
Temp
("F)
211.0
211.0
211.0
210.0
209.0
210_O
210.0
202.O
Velocity
(v)
54.22
53.31
51.92
45.87
55.04
53.73
s',t.40
36.79
Port Point
3l
32
33
34
DP
(in. H2O)
0.57
0.51
0.48
0.35
0.60
0.57
0.52
0.38
Sqrt.
DP
0.7550
0.7141
0.6928
0.5916
o.7746
0.7550
0.7211
0_6164
283,313
149,728
185,628
11,137,694
11,082,005
281,896
Temp Velocity
fF) M
209.0 52.77
209.0 49.92
210.0 48.46
208.0 41.32
0.62
0.s9
0.il
0.28
0.7874
0.7681
o.7348
0.5292
Test Parameters
P6u, - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of HrO
P" - Absolute stack pressure, inches Hg
t" - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fVsec)
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
I
2
3
4
2
2
2
2
4
4
4
4
207.0
209.0
210.0
208.0
54.06
52.77
50.44
43.06
11t6t2020
@Mostardi Platt
24.88
-0.60
24.84
209.0
Circular
11
95.03
0.5'106
0.7109
49.688
o/o CO2 15.50
o/o 02 11.20
% Nz 73.30
Md - dry basis lb/lb mole 30.93
Ms - wet basis lb/lb mole 28.428
Bws - Moisture content fraction 0.1934
Moisture determined by wb/db (Y or N) N
O -ACFM
Qsd - DSCFM
Qs - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
O - WAF adjusted ACFM
v'13.1
56 of 166
METHOD 2 VOLUMETRTC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot !D:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
4036
0.840
I
Operating Level:
Run No.:
Test Oate:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
9
6t20t2023
12:5Q
13:19
TWM TestTechl BM
7
Port Point
't1
12
13
14
DP
(ln. H2O)
0.61
0.56
0.58
0.39
Sqrt.
DP
0.7810
0.7483
0.7616
0.6245
Temp
("F)
210.0
210.O
211.O
211.0
208.0
210.O
211.0
210.O
Velocity
ry)
54.66
52.37
53.34
43.74
54.13
52.U
52.41
44.26
DP
(in. H2O)
0.59
0.56
0.52
0.37
2
2
2
2
1
2
3
4
4
4
4
4
1
2
3
4
Port Point
31
32
33
34
0.63
0.57
0.56
0.36
O - ACFM
Osd - DSCFM
Os - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
Q - WAF adjusted ACFM
Sqrt.
DP
0.7681
0.7483
0.721',!
0.6083
o.7937
0.7550
o.7483
0.6000
288,511
15't,809
188,770
11,326,197
11,269,566
287,069
Temp Velocity
fF) (v)
206.0 53.60
211.0 52.41
211.0 50.50
21't.0 42.60
21',t.0
211.0
211.0
206.0
0.60
0.57
0.56
0.40
0.7746
0.7550
0.7483
0.6325
Test Parameters
P6", - Barometric pressure, inches Hg
P, - Stack Pressure, inches of H2O
P" - Absolute stack pressure, inches Hg
t" - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M2325124
Main Kiln Stack
24.88
-0.60
24.84
209.9
Circular
11
95.03
0.5269
0.7230
50.600
o/o CO2 15.50
o/o 02 11.30
% Nz 73.20
Md - dry basis lb/lb mole 30.93
Ms - wet basis lb/lb mole 28.400
Bws - Moisture content fraction 0.1958
Moisture determined by wb/db (Y or N) N
55.59
52.88
52.41
41.87
11t6t2020
@Mostardi Platt
v13.1
57 of 166
METHOD 2 VOLUMETRIC FLOW DATA
Project Number:
Client:
Facility:
Test Location:
Pitot lD:
Pitot Coefficient:
Probe Length, Feet:
M232512
Ash Grove Cement Company
Leamington Cem6nt Plant
Main Kiln Stack
4036
0.840
8
Operating Level:
Run No.:
Test Date:
Start Time:
End Time:
Test Engineer:
Port Length, lnches:
Normal
10
6t20t2023
13:40
14:09
TWM TestTech: BAA
7
Port Point
11
12
t3
14
2
2
2
2
DP
(in. H2O)
0.61
0.57
0.5'l
0.36
Sqrt.
DP
0.7810
0.7550
0.7141
0.6000
Temp
fF)
211.O
211.0
211.0
207.0
Velocity
M
54.68
52.85
49.99
41.88
55.48
53.77
51.92
43.55
Port Point
31
32
33
34
1
2
3
4
DP
(in. H2O)
0.60
0.53
0.54
0.40
0.62
0.59
0.56
0.40
Sqrt.
DP
0.7746
o.7280
0.7348
0.6325
0.7874
0.7681
0.7483
0.6325
288,699
152,319
188,981
1 1,338,876
1',t,282,18'l
287,256
Temp Velocity
fF) M
209.0 54.14
210.0 50.93
2'.t1.0 51.44
210.0 44.24
0.63
0.59
0.55
0.39
0.7937
0.7681
0.7416
0.6245
Test Parameters
Pbar - Barometric pressure, inches Hg
Pn - Stack Pressure, inches of H2O
Ps - Absolute stack pressure, inches Hg
t - Average stack temperature, oF
Duct Shape:
Diameter, Feet
Cross Sectional Area of Stack, Ft2
Method 2 Results
Average DP
Average Sqrt DP
Average Velocity Vs (fUsec)
FT-004 MP Pitot
Project No. M232512A
Main Kiln Stack
4
4
4
4
1
2
3
4
209.0
211.0
211.0
206.0
210.0
211.O
211.0
205.0
55.08
53.77
52.39
44.08
11t6t2020
@Mostardi Plaft
24.88
-0.60
24.84
209.6
Circular
11
95.03
0.5281
0.7240
50.633
o/o CO2 15.50
o/o 02 11.40
o/o N2 73.10
Md - dry basis lb/lb mole 30.94
Ms - wet basis lb/lb mole 28.426
Bws - Moisture content fraction 0.1940
Moisture determined by wb/db (Y or N) N
O - ACFM
QSd. DSCFM
Qs - SCFM
Qs - SCFH
Qs - WAF adjusted SCFH
Q - WAF adjusted ACFM
v13.1
58 of '166
Test No,Date Start Time End Time
Vm (standard
L)nq detected DOb uq/dscm ug/w3cm
paired trap
agrO€mentl o/o
difference Breakthrouqh ol
1A 612012023 7:30 8:00
25.436 15_4 0.073 0.605 0.491 2.67
1B 25.47'l 15.7 0.074 0.616 0.500 5.37
Averag6 25.453 15_6 0.073 0.611 0.496 o.90
2A 6t2012023 8:07 8:37
25.310 14.9 0.071 0.589 0.474 2.76
28 25.337 14.2 0.067 0.560 0.451 1.43
Averaqe 25.324 14.6 0.069 0.575 0.463 2.46
3A 6t20t2023 8:43 9:13
25.146 14.6 0.070 0.581 0.467 0.69
3B 25.225 14.2 0.067 0.563 0.453 4.4',1
Averaqe 25.186 14.4 0.069 0.572 0.460 1.55
tlA
6120t2023 9:35 10:05 2s.059 21.0 0.100 0.838 0.675 '1.94
4B 25.',t47 17.8 0.085 0.708 0.570 0.23
Average 25.103 19.4 0.093 0_773 0.623 8.42
5A 6DO12023 10'.'t2 10:42
25.O22 30.2 45 1.207 0 973 1.68
5B 25.056 30.5 0.46 1.217 0.981 1.09
Average 25.039 30.4 0. 45 1.212 0.977 0.43
6A 6t2012023 10:48 11:18
24.935 32.3 0. 55 1.295 't.o42 0.94
6B 24.953 28.8 0.38 1.154 0.928 0.94
Averaqe 24_944 30.6 0. 47 1.225 0.985 5.76
7A 6t20t2023 1 1:38 12:08
24.837 29.8 0.44 1.200 0.968 0.34
7B 24.859 31.2 0.50 1.255 1.012 '1.63
Average 24.848 30.5 0.47 '1.227 0.990 2.25
8A 6t20t20?3 12:13 12:43 24.717 24.6 0.19 0.995 0.803 0.41
8B 24.748 24.8 20 1.002 0.808 0.00
Average 24.732 24.7 0.120 0.999 0.806 0_34
9A 612012023 12:50 13:20
24.656 19.5 0.095 0.791 0.636 1.04
9B 24.685 20.7 0.101 0.839 0.a74 0.49
Averaqe 24.671 20.1 0.098 0.8't5 0.655 2.93
10A 6t20t2023 13:40 14:10 24.626 20.4 0.099 0.828 0.668 2.s',i,
't0B 24.655 21.0 0.102 0.852 0.687 1.45
Averag€24.640 20.7 0.101 0.840 0.677 1.39
FT-008 Hg Template
Project No. M2325124
Main Kiln Stack
Method 30B (Sorbent Trap) Mercury Test Results Summary
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
v5.0
59 of '166
10131117
@Mostardi Platt
Proiect#: M232512
Client: Ash Grove Cement Company
Faclllty: Leamlngton Cement Plant
Analyzer lD: 1423
METHOD 3OB TEST RESULTS
Hs (ns):
Meter Temperature (oF):
Meter lD:
Meter Calibratlon (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
He (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
Location: Main Kiln Stack
Condition: Mill On
DataTaken By: SMCG
15.4
57.67
MM2A
0.996
0
30.026
25.436
0.073
0.605
0.491
Start Timo:
End Time:
Pressure, Barometric(Hg"l:
Water Vapor lh Flue Gas (Bws):
7:30
8:00
24.950
0.188
Meter Temperature (oF):
Metor lD:
Meter Callbratlon (Y):
lnitial Volume (liters):
FinalVolume (liters|:
Mote, Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
15.7
57.67
MM2B
0.997
0
30.037
25.471
0.074
0.616
0.500
rap
Start Time:
End Time:
Pressure, Barometric(H g"):
Water Vapor ln Flue Gas (Bws):
Hs (ng):
Meter Temperalure (oF):
Meter lD:
Meter Callbratlon (Y):
lnitial Volume (liters):
FinalVolums (liters):
Meter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
Hg (ng): 14.2
MeterTemperature(oF): 60.50
Meter lD: MM2B
Meter Calibration (Y): 0.997
lnitial Volume (liters): 0
Final Volume (liters): 30.043
Meter Volumo (Standard liters): 25.337
Hs (ppb): 0.067
Hg (ug/dscm): 0.560
Hg (ugArscm): 0-451
8:07
8:37
24.950
0.195
14.9
60.50
MM2A
0.996
0
30.041
25.310
0.071
0.589
0.474
Start Time:
End Time:
Pressure, Barometric(Hg"):
Waler Vapor in Flue Gas (Bws):
8:43
9:'13
24.950
0.195
Hs (ns):
Meter Temperature (oF):
Meter lD:
Meter Callbratlon (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard litersl:
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscml:
14.6
64.00
MM2A
0.996
0
30.047
25.146
0.070
0.581
0.467
Hg (ns): 14.2
MeterTomperaturo(oF): 63.00
Meter lD: MM2B
Meter Callbratlon (Y): 0.997
lnitialVolume(literc): 0
Final Volume (liters): 30.054
Meter Volume (Standard liters): 25.225
Hg (ppb): 0.067
Hg (ug/dscm): 0.563
Hg (ugirscm): 0.453
FT-008 Hg Template
Project No. M232512A
Main Kiln Stack
v5.0
60 of 166
10131117
OMostardi Platt
METHOD 3OB TEST RESULTS
Project#: M232512
Client: Ash Grove Cement Gompany
Facility: Leamington Cement Planl
Analyzer lD: 1423
Location: Main Kiln Stack
Gondition: Mill On
Data Taken By: SMCG
Dato:
Start Time:
End Time:
Pressuro, Barometric(Hg"):
Water Vapor in Flue Gas (Bws):
4A Trap
Hs (ns):
Meter Temperature fF):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
6t20t2023
9:35
10:05
24.950
0.195
21.0
65.50
MM2A
0.996
0
30.029
25.059
0.100
0.838
0.675
oLcl 561 89
17.8
64.50
MM2B
0.997
0
30.046
25.147
0.085
0.708
0.570
25
48 Trap lD:
Hg (ng):
Meter Temperaturs fF):
Metsr lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
Spikod Trap Run:
Splke Concentration:
Start Time:
End Time:
Pressure, Barometric(Hg"):
Water Vapor in Flue Gas (Bws):
Date: 612012023
10i12
10i42
24.950
0.194
Hs (ng):
Meter Temperature fF):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
30.2
66.50
MM2A
0.996
0
30.041
25.022
0.145
1.207
0.973
o1c156360
30.5
66.5
MM2B
0.997
0
30.052
25.056
0.'t46
1.217
0.981
25
58 Trap lD:
Hg (ng):
Meter Temperature fF):
Meter lD:
Meter Calibration 00:
lnitial Volume (liters):
Final Volume (liters):
M6ter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
Spiked Trap Run:
Spike Concentration:
Start Time:
End Time:
Pressure, Barometric(Hg"):
Wator Vapor in Flue Gas (Bws):
6A Trap lD:
Hs (ng):
Met6r Temperature fF):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
10:48
11:18
24.950
0.196
o1607149
32.3
68.50
MM2A
0.996
0
30.051
24.935
0.155
1.295
1.042
Trap lD:oLcl 75835
Hg (ng): 2B.a
Meter Temporature fF): 68.50
Meter lD: MM2B
Meter Calibration (Y): 0.997
lnitialVolume(liters): 0
Final Volume (liters): 30.042
Meter Volume (Standard liters): 24.953
Hg (ppb): 0.138
Hg (ug/dscm): 1.154
Hg (ug/wscm): 0.928
Spiked Trap Run: Y
Spike Concentration: 25
FT{08 Hg Template
Project No. M2325124
Main Kiln Stack
vs.0
61 of 166
10131117
OMostardi Platt
METHOD 3OB TEST RESULTS
Project#: M232512
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Analyzer lD: 1423
Location: Main Kiln Stack
Condition: Mill On
Data Taken By: SMCG
Start Time:
End Time:
Pressure, Barometric(Hg'):
Water Vapor in Flue Gas (Bws):
7A Trap ID:
Hg (ns):
Meter Temperature ("F):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Flnal Volume (llters):
Meter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
78 Trap tD:
Hs (ng):
Meter Temperature (oF):
Meter lD:
Meter Calibration (Y):
!nitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
6t20t2023
1 1:38
12:OB
24.950
0.194
o1C182607
29.8
70.50
MM2A
0.996
0
30.046
24.837
0.144
1.200
0.968
oLc122435
31.2
70.50
MM2B
0.997
0
30.042
24.959
0.150
1.255
1.012
Start Time:
End Time:
Pressure, Barometric(Hg"):
Water Vapor in FIuo Gas (Bws):
Hs (ns):
Meter Temperature fF):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard liters):
Hs (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
Hg (ng): 24.8
Meter Temperature (oF): 73.00
Meter lD: MM2B
Meter Calibration (Y): 0.997
lnitial Volume (liters): 0
Final Volume (liters): 30.049
M6ter Volume (Standard llters): 24.748
Hg (ppb): 0.120
Hg (ug/dscm): 1.002
Hg (ug/wscm): 0.808
12:13
12:43
24.950
0.193
24.6
73.00
MM2A
0.996
0
30.041
24.717
0.1 19
0.995
0.803
Start Time:
End Time:
Pressure, Barometric(Hg"):
Water Vapor in Flue Gas (BrYs):
Hg (ng):
Meter Temperature fF):
Meter lD:
Meter Calibration 04:
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard Iiters):
Hg (ppb):
Hg (ug/d3cm):
Hg (ug/wscm):
98 Trap lD:
Hs (ns):
Meter Temperaturo f F):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard literc):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
'12:50
13:20
24.950
0.196
oL607249
19.5
74.50
MM2A
0.996
0
30.052
24.656
0.095
0.791
0.636
o1607096
20.7
74.50
MM2B
0.997
0
30.057
24.685
0.101
0.839
0.674
FT408 Hg Template
Project No. M232512A
Main Kiln Stack
vs.0
62 of 166
10131117
OMostardi Platt
METHOD 3OB TEST RESULTS
Project#: t1232512
Client: Ash Grove Cement Company
Facility: Leamington Cement Planl
Analyzer lD: 1423
Location: lrain Kiln Stack
Condition: Mill On
Data Taken By: SMcG
Date:
Start Time:
End Time:
Pressure, Baromotric(Hg"):
Water Vapor in Flue Gas (Bws):
Hg (ng):
Meter Temperature fF):
Meter tD:
Meter Galibration (Y):
lnltlal Volume (litorc):
Final Volume (llters):
Meter Volumo (Standard liters):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
v5.0
63 of 166
6t20t2023
13:40
'14:10
24.950
0.194
20.4
75.00
MM2A
0.996
0
30.043
24.626
0.099
0.828
0.668
oL607247
21.0
75.00
MM28
0.997
0
30.048
24.65s
0.102
0.852
0.687
108 Trap lD:
Hg (ns):
Meter Temperature fF):
Meter lD:
Meter Calibration (Y):
lnitial Volume (liters):
Final Volume (liters):
Meter Volume (Standard lite6):
Hg (ppb):
Hg (ug/dscm):
Hg (ug/wscm):
FT{08 Hg Template
Project No. M2325124
Main Kiln Stack
10131117
@Mostardi Platt
Appendix E - CEMS and Plant Operating Data
Project No. M2325124
Main Kiln Stack
64 of 166 @Mostardi Platt
NN
Ss
-ouo-trELL6
<E
KBt-
IEI
.Eo
Eo-Er AcL(E;-EO- cOsl'E(JtrOO
E H# EE6E=6 sY Pg -g,fi '*0.==ii
,nEe;E 'no-J o
o
J
L.E
co(J
Il!oo
i
-9l!
oo(o-
N
@-o
oo
N^t\
F-
@-o
oo
@-
F*o
Or-o
ooo-
-
oo
$_t-*N.
ooc\l
@o,--
oo\f_
(o(9o{
oool
@
(f)
c\l
oo
@-
1r)(t
e\l
ooo_
Noc\t
o
Eso
=
O)a
@
sod
o,rr)
ci
F-q
o,
o,q
@
(f)F
@
o,n
@
F-d
N6
6
(o
@
@
Q)N630rEs
o- Fr
EL
c?o c!o no c?o no -to
(o
ci ao c?o ao
t,>NEO
CL -oaL o\
9E
(o
q
@
oq
N
oq
N
N
c.j
ro
c'j
t\
c.i
(o
ci n
(f,
6l
(t)
ils O
o,
q
@
oq
co
q
O)o,o, o; o;
c\l
O)6)
sc
NOoi
(o
d lJ)
(o
F-
(f)
(o
c.j
(f)ri t
(f)
(f,
ai
C9
crt
c)
c.j
n
cf,
€
xoz
oeo
oqo
oqo
oqo
oqo
oqo
oco
oco
oqo
oqo
=Eqo
oo
ro
@o,
q
rONN
oq
(o6N
a(o
@r()
(\t
ooira
$
$(Y)$
o
oO(os
aoIr*
oqt-o)(o
\ro
O)rO
*lOFzdo
@dNN
o?
@(f)N
qosN
Ir{)N(\t
q
c!N(\l
o
@(o(\I
(f)
o,N(\T
F*
(oNN
qo$N
oNN
o
E
i=
Ec
UJ
o)
Y?N
(o
(Y)
dd
N .t?o *o
t*:t-IN
N1N
o,
c.i
o,Ito,
o
.EFt.llo
o
q?
t-
t-I
@
(f)
T
@
rr)eo)
N
o
@so
@e (o
c.,i
o
Y?N
on
(f)
o
(lto
(f)
NoNoN
(o
cf)NoNoN
(o
(r)NoNoN
(o
(f,NoNoN(o
NCNcN
(c
(f)NoNoN
@
(o
NoNoN
@
(oNoNoN
(o
(r)NoNoN
(o
(oNoNoN(o
3e N cf)I rO @ I\@ o)o
(ooPrri x>;(o
N
66t(?) -SEfr ^U,(E;-
L tY
EFgao
Date/Time
CLINKER
(TNHR)
Expression
Value
KILN: CO
(PPM)
Raw
Value
KILN: CO2
(PCT)
Raw
Value
co_MAss
(LBHR)
Expression
Value
law
:uGscM)
:xpressiOn
y'alue
(LN: NOX
,PPM)
J(pression
/alue
\ox_MAss
:LBHR)
lpression
y'alue
KILN: 02
(PCr)
Raw
Value
)6/20/2023 07:30 1 7.6 1262.8 3.53 1003.2 0.470 200.6 261.8 9.01
)6/20/2023 07:31 1 7.6 1174.7 3.40 929.1 0.560 192.5 250.2 8.92
16/20/2023 07:32 7.2 935.6 3.80 737.6 0.630 200.0 259.1 9.03
)6/20/2023 07:33 t8.2 740.7 3.22 58r'.2 0.680 223,2 289.3 9.00
)G120/2023 07:34 1 7.1 645.4 3.59 507.1 0.620 230.4 297.4 9.10
X612012023 07:35 7.3 948.9 3.8s 747.2 0.550 204.6 2U.7 9.01
)6/20f2023 O7:36 1 7.1 1361.3 4.03 1073.7 0.470 206.0 267.0 8.96
)6/20/2023 O7:37 1 8.5 1309.3 4.08 1027.0 0.420 216.4 278.9 8.85
)6/2012023 07:38 1 8.0 823.2 3.60 641.8 0.500 224.1 287.1 8.99
)6/2012023 O7:39 7.6 584.8 3.24 460 0 0.580 241.5 312.1 8.98
)6/20/2023 07:40 7.7 1008.2 3.39 797.9 0.560 254.6 33'1.0 8.96
)6/20/2023 07:41 1 7.3 1305.3 3.27 1034.1 0.530 258.4 336.4 9.00
)6/2012023 07:42 1 7.3 1288.2 3.40 1026.2 0.490 246.3 322.4 8.99
)6/20/2023 07:43 1 6.9 1 123.9 3.56 897.3 0.470 223.5 293.2 8.93
)6/20/2023 07:44 1 6.1 8s3.6 3.68 673.7 0.540 219.7 284.9 8.88
)6/20/2023 07:45 1 6.4 596.3 3.70 467.2 0.590 231.1 297.5 8.95
)6/20/2023 07:46 1 7.3 565.4 3.19 440.5 0.530 271.6 347.7 9.02
06/20/2023 07:47 1 7.6 M5.0 3.67 s00.9 0.470 279.1 3s6.1 9.08
06120/2023 07:48 1 7.6 1067.7 3.34 838.0 0.470 276.1 356.0 9.16
A6/20/2023 07:49 1 7.4 1597.4 3.59 1269.0 0.500 261.O 340.7 8.90
06/20/2023 07:50 1 7.1 1483 4 4.48 1172.0 0.660 222.2 288.4 8.78
06/20/2023 07151 1 7.7 1048.9 4.08 824.1 0.770 203.3 262.s 8.89
06/20/2023 07:52 1 7.3 312.6 3.98 245.2 0.620 225.2 290.2 9.08
06/20/2023 07:53 1 7.4 508.5 3.50 397 1 0.490 258.3 331.4 905
06/20/2023 07:54 1 7.8 1357.3 4.06 1 061 .1 0.420 239.4 307.5 9.02
06/20/2023 07:55 1 8.4 1542.7 3.63 1204.7 0.380 218.3 280.1 8.8s
O6/20/2023 07:56 1 8.1 1121.7 4.29 869.6 0.s60 187.5 238.8 8.96
06/20/2023 07:57 1 8.5 698.4 3.16 542.0 0.700 192.0 2M.B 8.99
06/20/2023 07:58 1 8.2 597.8 3.18 470.2 0.630 228.1 294.8 9.05
)6/20/2023 07:59 I 7.7 1044.3 3.42 824.2 0.550 228.7 296.6 8.99
AVERAGE L1 7.5 985.1 3.53 775.s3 o.547 224.8 295.62 8.98
Project No. M2325124
Main Kiln Stack
66 of 166 @Mostardi Platl
7.0 11.28 10932000.0 7.2 13.0
7.0 11.21 10884000.0 7.2 12.9
7.O 1 1.35 10848000.0 7.3 13.4
7.0 1 1.33 10854000.0 7.3 13.4
7.0 't1.44 10812000.0 7.1 't3.1
7.0 11.32 10836000.0 7.1 12.9
7.O 11.25 10854000.0 7.1 12.8
7.0 1 1.10 10794000.0 7.3 13.0
7.0 1 1.28 1 0728000.0 7.4 13.4
7.0 11.27 10824000.0 7.2 13.0
7.0 11.24 1 0890000.0 7.3 13.2
7.0 1 1.30 10902000.0 7.1 12.9
7.0 11.27 1 0962000.0 7.1 12.8
7.0 11.17 1 0985000.0 7.4 13.3
7.0 11.11 10850000.0 7.4 13.2
7.0 11.26 1 0782000.0 7.2 13.1
7.0 1 1.36 10722000.0 7.3 13.4
7.0 11.43 10686000.0 7.2 13.4
7.0 1't.52 10800000.0 7.2 13.5
7.0 11.15 10932000.0 7.1 12.7
7.0 1 1.00 10872000.0 7.2 12.6
7.0 11 16 10812000.0 7.4 13.3
7.0 11.41 10794000.0 7.2 13.2
7.0 11.40 10746000.0 7.1 13.0
7.0 11.34 10758000.0 7.0 12.8
7.0 1 1.08 10746000.0 7.0 12.5
7.0 11.26 10558000.0 7.2 13.1
7.0 11.25 10580000.0 7.3 13.1
7.0 1 1.35 10824000.0 7.1 13.0
7.0 11.28 10860000.0 7.1 12.9
7.0 1,-.27 10821600.0 7.2 13.1
Project No. M2325124
Main Kiln Stack
67 of 166 @Mostardi Plaft
Date/Time
:LINKER
:TNHR)
ixpression
y'alue
KILN:CO
(PPM)
Raw
Value
KILN: CO2
(PCT)
Raw
Value
CO-MASS
(LBHR)
Expression
Value
Raw
(uGscM)
Expression
Value
KILN: NOX
(PPM)
Expression
Value
!ox_MAss
,LBHR)
xpression
/alue
KILN:02
(PCr)
Raw
Value
)6/2012023 O8:O7 117.2 1393.7 3.9s 1088.4 0.620 222.6 28s.6 8.73
)6/20/2023 08:08 116.7 981.2 3.92 760.2 0.620 210.3 267 7 8.80
)6/2012023 08:09 118.2 613 2 3.67 478.1 0.620 228.s 292.7 9.05
)6120/2023 08:10 1 17.0 79s.6 3.02 625.1 0.540 241.6 3'l 1.9 8.97
06/20/2023 08:11 118.4 1343.1 3.01 1059.4 0.480 227.2 294.4 8.95
06/20/2023 O8:12 1 18.9 1574.3 3.25 1241.1 0.500 207.9 269.3 8.90
06/20/2023 08:13 1 18.8 1398.8 3.M 1097.8 0.s30 212.6 274.2 8.98
06/20/2023 08:14 1 19.8 1222.3 3.38 96s.7 0.520 203.2 263.8 8.90
06/20/2023 08:15 119.2 1 31 3.3 3.60 1038.2 0.s20 2149 279.1 844
06/20/2023 08:16 1 18.5 1454.O 3.68 1129.7 0.570 252.7 322.6 7.87
06/20/2023 08:17 1 19.5 1590.9 3.33 1227.1 0.500 270.7 343.1 8.82
06/20/2023 08:18 117.9 1409.3 3.46 1098.7 0.520 2s0.2 320.5 9.22
X6/20/2023 08t19 117.1 1431.4 3.46 1 134.0 o420 234.0 304.6 9.26
16/20/2023 O8:20 117.5 17?2.6 3.07 1370.7 0.320 237.3 31 0.3 9.02
X6/20/2023 08:21 117.0 1622.6 3.1 6 1288.3 0.260 225.2 293.8 8.90
)6/20/2023 08:22 1 18.0 1334.3 3.79 1055.9 0.400 198.6 258.2 8.95
)6/20/2023 08:23 1 18.2 758.9 3.66 603.9 0.520 205.4 268.5 9.03
)6124/2023 08:24 117.9 796.9 3.52 638.6 0.480 228.9 301.4 9.O4
)6/20/2023 08:25 1 17.8 1196.7 3.22 958.0 0.450 230.5 303.2 9.02
)5/2012023 08:?6 1 19.0 1203.2 3.17 964.3 0.530 236.9 311.9 8.96
)6/20/2023 08:27 118.2 101 5.4 13.54 812.0 0.600 228.5 300.2 9.00
)6/20/2023 08:28 118.7 916.5 3.46 725.7 0.620 227.5 296.O 8.9s
)6/20/2023 08:29 1 19.0 1 1 16.0 3.02 887.1 o.620 240.6 314.2 9.00
)6120/2023 08:30 1i9.0 1439.0 3.16 1148.2 0.500 246.1 322.6 8.99
06/2012023 08:31 1 18.3 1332.3 3.92 1061.9 0.400 2767 362.4 9.03
06/20/2023 08:32 1 19.6 1235.5 3.43 98s.8 0,410 272.5 357.3 8.96
)6/20/2023 08:33 119.4 1239.0 3.46 9897 0.430 268.0 351.7 8.82
06/20/2023 08:34 119.4 1245.2 3.9s 989.5 0.M0 270.1 352.4 8.76
06/20/2023 08:35 119.8 1014.2 3.72 800.4 0.470 284.3 368.5 8.76
)6/20/2023 08:36 119.1 1056.5 3.79 832.9 0.520 312.8 405.2 8.85
AVERAGE 118.4 L225.6 3.47 968.55 0.501 238.9 310.25 8.90
Project No. M232512A
Main Kiln Stack
68 of 166 @Mostardi Platl
oz_coRR_7
(PCI)
Raw
Value
)2-DRY
:PCT)
:XpreSSlOn
,/alue
STK-FLOW
(scFH)
Expression
Value
KILN: THC
(PPM)
Ritw .1:,: .
Value
rHc_coRR
:PPM)
:xpression
/alue
7.0 10.95 0746000.0 7.4 13.0
7.0 11.07 0662000.0 7.4 13.2
7_O 11.41 0728000.0 7.2 13.3
7.0 11.28 081 2000.0 7.2 13.1
7.0 11.22 0854000.0 7.1 12.8
7.0 11.14 0848000.0 7.2 12.8
7.0 11.23 0800000.0 7.2 12.9
7.0 11.1s 0872000.0 7.2 12.8
7.0 10.57 1 0878000.0 8.2 13.9
7.O 9.89 1 0592000.0 89.9 142.5
7.0 13 10514000.0 24.1 43.3
7.0 .62 1 0728000.0 9.7 8.3
7.0 61 1 0902000.0 7.5 4.1
7.0 .27 1 09s0000.0 7.3 3.1
7.0 12 1 0926000.0 7.4 3.1
7.0 20 1 0890000.0 7.5 3.5
7.0 34 1 0950000.0 7.4 3.s
7.0 36 1 1 028000.0 7.1 3.0
7.0 .29 11016000.0 7.2 3.0
7.0 21 1 1028000.0 7.2 2.9
7.0 26 1 1004000.0 7.2 3.0
7.0 21 1 0896000.0 7.3 3.1
7.0 .29 1 0938000.0 7.2 3.0
7.0 26 1 0980000.0 7.3 3.1
7.0 32 1 0968000.0 7.2 3.1
7.0 24 1 0980000.0 7.2 3.0
7.0 .05 1 0992000.0 7.3 2.8
7.0 0.98 1 0925000.0 7.4 3.0
7.0 0.99 1 0860000.0 75 3.2
7.0 12 1 0848000.0 7.3 3.1
7.O tL.2 LOA77200.0 LO.7 18.5
Pro.iect No. M2325124
Main Kiln Stack
69 of 166 @Mostardi Platt
Date/Time
CLINKER
ONHR)
Expression
Value
(lLN: CO
:PPM)
law
y'alue
KILN: CO2
(PCr)
Raw
Value
co_MAss
(LBHR)
Expression
Value
law
:uGscM)
!xpression
y'alue
KILN: NOX
(PPM)
Expression
Value
NOX_MASS
(LBHR)
Expression
Value
KILN: 02
(PCT)
Raw
Value
)6/20/2023 08:43 7.3 481.8 14.05 382.5 0.590 259.8 338.9 8.90
16/20/2023 08:44 8.2 11 10.8 14.11 883.9 0.490 265.5 347.1 9.05
)6/20/2023 08:45 8.3 131 3.1 3.41 1043.7 o.420 251 8 328.9 9.09
)6/20/2023 08:46 18.0 1073.6 3.47 854.3 0.460 243.9 318.9 8.98
)6/20/202308]r'.7 8.5 948.2 3.75 754.5 0.490 254.7 333.0 8.82
)6/20/2023 O8:48 8.6 693.4 3.93 548.1 0.580 270.6 351.5 892
)6/20/2023 08:49 7.3 806.6 3.36 639.0 0.630 295.2 384.3 8.92
)6/20/2023 08:50 8.9 1420.6 3.6s 1129.2 0.500 291.3 380.4 9.01
)5/20/2023 08:51 8.8 1s83.3 3.44 1257.1 0.400 264.5 345.1 8.91
)6/20/2023 08:52 8.4 1527.1 3.39 1208.5 0.s20 254.3 330.7 8.80
)6/20/2023 08:53 8.5 1527.2 3.38 1202.6 0.610 246.5 31 8.9 8.74
)6/20/2023 08:54 8.0 1342.0 3.76 1062.0 0.530 231 300.s 8.8s
)6/20/2023 08:55 8.3 1121.4 3.80 889.4 0.470 2M.3 31 8.4 8.67
06/20/2023 08:56 63.0 9928 414 781.8 0.530 268.1 346.9 8.62
06/20/2023 08:57 59.2 866.7 4.04 680.6 0.580 263.5 340.0 9.00
06/20/2023 08:58 6.9 1264.1 3.46 1008.6 0.490 255.5 335.0 9.05
06/20/2023 08:59 7.5 1993.7 3.04 1593.4 0.430 242.1 317.9 8.97
06/20/2023 09:00 83 1622.1 3.42 1281.6 0.480 222.2 288.4 8.82
06/20/2023 09:01 9.6 1128.4 3.50 892.5 0.530 21't.5 274.9 8.85
06/20/2023 09:02 9.0 1374.3 3.15 1082.8 0.540 210.7 272.8 8.63
06/20/2023 09:03 9.5 1737.7 3.78 1 366.1 0.s60 200.3 258.7 8.M
05/20/2023 09:04 9.1 1857.0 3.90 1476.9 0.540 184.7 241.4 8.47
06/20/2023 09:05 9.5 1657.6 13.61 1324.1 0.s30 184.9 242.7 8.73
06/20/2023 o9:06 20.1 1 307.1 3.60 1043.0 0.550 196.2 257.2 8.68
06/20/2023 09:07 9.0 1320.4 3.76 1 051.3 0.570 202.1 264.4 8.73
)6/20/2023 09:08 9.0 1 63s.1 3.96 1290.4 0.s00 209.2 271.3 8.60
)6120/2023 09:09 8.2 1721.2 3.91 1355.4 0.420 215.7 279.1 880
)6120/2023 09:10 8.4 1 1 99.1 3.70 951.6 0.450 227.4 296.5 8.73
)6/20/2023 09:11 9.3 1078.8 3.71 855.6 0.460 252.6 329.2 8.80
)6/20/2023 09:12 19.4 898.3 3.80 712.1 0.440 279.6 364.2 8.98
AVERAGE L.t4.7 1286.8 3.67 1020.09 0.510 240.0 3L2.57 8.83
Project No. M232512A
Main Kiln Stack
70 of 166 @Mostardi Platt
)2_CORR_i
:PCI
{aw
r'alue
O2-DRY
(PCr)
Expression
Value
;TK-FLOW
scFH)
:Xpression
/alue
KILN: THC
(PPM)
Raw
Value
THC-CORR
(PPM)
Expression
Value '
7.0 11.2s 1 0926000.0 7.1 13.0
7.0 1 1.38 1 0950000.0 7.0 12.8
7.0 11.37 1 0938000.0 7.0 12.8
7.0 11.26 1 0950000.0 7.2 13_0
7.0 1 1.04 1 0950000.0 7.3 12.8
7.0 11.21 1 0878000.0 7.2 12.9
7.0 11.20 1 0902000.0 7.1 12.8
7.0 1 1.33 1 0938000.0 6.9 12.6
7.0 1 1.18 1 0926000.0 7.0 12.6
7.0 1 1.05 1 0890000.0 7.0 't2.4
7.0 1 1.00 1 0836000.0 7.O 12.4
7.0 11 14 1 0890000.0 7.2 13.0
7.0 10.91 10914000.0 7.3 12.8
7.0 10.84 1 0836000.0 7.4 12.8
7.0 1 1.33 1 0806000.0 7.1 12.9
7.0 11.39 1 0980000.0 7.0 12.9
7.0 11.27 1 0998000.0 6.8 12.3
7.0 1 1.08 1 0872000.0 7.1 't2.6
7.0 11 14 1 0884000.0 7.O 12.5
7.0 10.89 1 0842000.0 7.2 12.6
7.0 10.90 1 081 8000.0 7.1 12.5
7.0 10.58 10944000.0 7.4 12.6
7.0 11.00 1 0992000.0 7.3 12.9
7.0 10.93 10980000.0 7.2 12.7
7.0 11 00 10955000.0 7.3 12.9
7.0 10.84 1 0860000.0 7.3 12.7
7.0 'l 1.08 1 0836000.0 7.2 12.9
7.0 10.99 10920000.0 7.4 13.0
7.0 11.07 10914000.0 7.2 12.9
7.0 11.34 1 0908000.0 7.1 13.1
7.O 11.1 10907800.0 7.L L2.8
Poect No. M2325124
Main Kiln Stack
71 of 166 @Mostardi Platt
Date/Time
CLINKER
ONHR)
Expression
Value
KILN: CO
(PPM)
Raw
Value
KILN: CO2
(PCT)
Raw
Value
co_MAss
(LBHR)
Expression
Value
Raw
(ucscM)
Expression
Value
KILN: NOX
(PPM)
Expression
Value
NOX_MASS
(LBHR)
Expression
Value
)6/20/2023 09:35 18.6 167s.1 13.60 1338.1 o.720 261.8 343.6
X6/20/2023 09:36 19.2 16s4.8 13.71 1321.1 0.740 235.6 309.0
J6/2A/2023 09:37 18.6 1568.7 13.39 1252.4 0.760 233.0 30s.5
X6/20/2O23 09:38 19.4 1594.4 1 3.31 1280.5 0.760 228.1 301.0
X6/20/2023 09:39 '18.4 1620.2 '13.84 1305.5 0.770 217.6 288.1
X6/20/2023 09:40 19.0 2306.4 13.70 1859.4 0.770 217.8 288.s
J6/2012023 09:41 18.s 2086.0 13.46 't 670.8 0.770 225.4 296.6
J6/20/2023 09:42 19.0 708 5 13.27 1357.3 0.810 236.4 308.6
)6/20/2023 09:43 18.6 362.4 13.15 108s.3 0.840 245.8 321.7
)6DA/2O23O9:M 18.6 453.5 13.O2 1171.2 0.790 241.0 3 19.1
X6/20/2A23 09:45 20.1 858.3 13.08 1528.1 0 730 227.1 306.8
)6/20/2023 09:46 20.0 781.4 12.80 1451.8 0.760 221.2 298.2
)6/20/2023 09:47 19.8 710.5 1 3.10 387.2 0.780 222.4 296.3
)6/20/2023 09:48 19.3 677 9 13.38 3s8 6 0 820 212.7 283.0
)6/20/2023 09:49 18.7 677.8 13.45 362.2 0.860 200.6 267.6
)6/20/2023 09:50 18.6 595.s 13.33 299.5 0.820 202.6 271.1
)6/20/2023 09:51 19.1 369.4 13.26 111.2 0.780 200.9 267.8
)6/20/2023 09:52 18.4 263.2 13.08 022.2 0.840 209.4 278.4
)6/20/2023 09:53 19.0 445.O 13.20 1624 0.890 220.6 291.6
)6120/2023 09:54 18.8 731.6 13.33 399.0 0.800 214.4 284.6
)612O/2023 09:SS 19.2 691.4 13.14 374.7 0 720 214.0 285.8
)6/20/208 A9:56 18.9 461.5 12.94 187.8 0.750 218.6 291.9
06120/2023 09:57 19.4 380.6 13.17 122.7 0.780 220.2 294.2
06120/2023 09:58 18.6 3U.6 13.61 126.5 0.790 228.6 305.5
06/20/208 A9:59 19.4 32s.6 13.57 073.3 0.790 239.0 318.0
06/20/2023 10:00 18.8 377.6 13.M 'l t 1.8 0.800 236.7 31 3.9
06/20/202310:01 19.4 468.7 13.52 184.1 0.810 226.3 299.8
06/20/202310:02 19.7 171.2 13.50 941.2 0.860 225.2 297 3
06/20/202310:03 19.2 1 15.0 13.33 897.5 0.900 238.1 31s 7
06/20/202310:04 19.7 476.3 12.99 1192.8 0.830 239.0 317 3
AVERAGE ,19.1 1566.4 L3.32 L264.87 o.795 225.4 298.89
Project No. M2325124
Main Kiln Stack
72 of 166 @Mostardi Plaft
KILN: 02
(PCD
Raw
Value
o2_coRR_7
(PCr)
Raw
Value
O2-DRY
(PCr)
Expression
Value
STK-FLOW
(scFH)
Expression
Value
(lLN: THC
,PPM)
law
y'alue
tHc_coRR
,PPM)
:xpression
/alue
8.86 7.0 1 14 1 0992000.0 7.0 2.s
8.83 7.0 1 13 1 0986000.0 7.1 2.7
8.80 7.0 1 10 1 0985000.0 7.2 2.9
9.03 7.0 1 39 1 052000.0 7.O 2.9
8.84 7.0 1 13 1 088000.0 7.3 3.1
8.85 7.O 1 17 1 094000.0 7.1 2.9
8.85 7.0 1 17 1 022000.0 7.O 2.6
8.89 7.0 1 21 1 0932000.0 7.2 31
8.89 7.0 1 ,22 1 0962000.0 7.2 3.1
8.96 7.O 1 .30 1 088000.0 7.1 3.0
9.12 7.0 1 .47 1 316000.0 3.1
9.11 7.0 1 .40 1 292000.0 7.0 2.9
9.00 7.0 1 .26 1 1 60000.0 7.0 2.7
9.10 7.0 1 .43 1 142000 0 7.0 2.9
9.09 7.0 1 41 1 172000.0 7.0 29
9.06 7.0 11.35 1 1 208000.0 7.0 2.8
9.08 7.0 1 .39 1 1 56000.0 AA 2.9
9.08 7.0 1 .41 1 135000.0 6.9 2.7
9.03 7.0 1 35 1 070000.0 7.1 3.0
8.94 an 11.24 1 1 1 18000.0 7.1 2.8
9.07 7.0 1 .39 1 184000.0 7.0 2.9
9.11 7.0 1 42 1 184000.0 7.1 3.0
9.09 7.O 1 .39 1 1 90000.0 6.9 2.6
9.06 7.0 1 37 1 196000.0 7.0 2.8
8.93 7.0 11.22 1 142000.0 7.1 2.8
8.93 7.0 1 .23 1 106000.0 AA 2.6
8.85 7.0 1 16 1 094000.0 7.0 2.6
8.85 7.0 'I 17 1 0s8000.0 70 2.6
8.93 7.0 1 29 1 076000.0 7.0 2.7
9.00 7.0 1 38 ,l
1 18000.0 71 3.1
8.98 7.O L 1.3 11111000.0 7.L 2.8
Project No. M2325124
Main Kiln Stack
73 of 166 @Mostardi Platt
)atefime
:LINKER
:rNHR)
:xpression
y'alue
(lLN: CO
:PPM)
law
r'alue
(LN: CO2
:PCT)
law
y'alue
:o_MASS
:LBHR)
:xpression
y'alue
law
,uGscM)
*pression
/alue
(LN: NOX
:PPM)
lpression
/alue
!ox_MAss
,LBHR)
:xpreSsiOn
/alue
)6120/2023 1O:12 19.4 529.0 3.21 433.6 .080 201.1 271.7
05/20/2023 10:13 19.1 725.4 3.09 594.6 .070 193.6 260.7
06/20/2023 10:,14 19.2 403.0 2.80 328.9 120 205.0 274.9
06/20/2023 10:15 19.2 588.3 3.18 481.2 170 219.4 294.9
06/20/2023 10:16 19.3 758.3 3.04 625.2 160 188.9 255.9
06/20/2023 10:17 18.9 471.9 3.19 386.8 140 199 8 269.1
06/20/2023 10:18 20.3 539.8 3.26 439.0 130 199.5 266.5
06/20/2023 1O:19 18.2 3847 3.71 310.8 110 178.2 236.6
O5/20/2023 10:20 19.1 312 3 3.51 254.5 150 198.3 265.5
06/20/2023 1O:21 18.1 5s3.0 3.15 454.0 190 222.5 300.1
06/20/202310:22 '18.8 312.4 3.M 254.4 170 235.9 315.7
06/20/202310:23 19.0 595.7 2.74 485.0 150 231.9 31 0.8
06/20/?023 '.10:'24 19.2 587.6 3.sB 481.7 .350 199.7 269.0
06/20/202310:25 19.0 417.7 3.86 340.8 550 222.1 297.7
i6/20/202310:26 19.2 382.4 3.M 310.6 470 232.0 309.6
J6/20/202310:27 21.8 369.4 3.70 302.3 .400 219.7 295.4
X6/20/2023 10:28 18.5 525.5 3.38 431.0 .400 220.9 297.7
)6/2012023 10:.29 20.0 583.6 3.86 558.6 .400 250.2 335.9
)6/20/202310:30 19.4 483.4 3.48 394.1 .270 250.3 33s.3
)6/20/20?310:31 19.1 367.1 3.46 299.2 1.140 260.4 348.7
)6/20/2023 10:32 18.0 565.8 3.50 462.1 1.150 258.6 347.0
)6120/2O23 1O:.33 18.4 591 2 3.24 484.1 1.170 238.0 320.2
)6/20/2023 10:34 19.4 471.6 3.3s 385.3 1.200 236.2 317.1
)6/20/2023 1435 '18.5 351.2 13.21 285.6 1.220 253.1 338.2
16/20/2O23 1O:36 188 538.9 13.53 438.2 1 210 258.7 345.6
06/20/202310:37 19.2 714.3 13.41 584.9 '1.200 242.6 326.4
06/20/2023 10:38 19.6 866.5 13.32 711.8 1.370 215.6 291.0
06/20/2023 1O:39 19.7 65s.0 13.51 536.9 1.540 200.s 270.0
A6/20/2023 10:40 '18.9 533.4 13.26 437.5 1.560 215.7 290.7
06/20/2023 10:41 18.9 598.2 12.86 491.9 1.580 228.4 308.6
AVERAGE 19.1 529.2 13.35 432.85 t.267 222.6 298.88
Project No. M232512A
Main Kiln Stack
74 of 166 OMostardi Platt
(lLN: 02
PCD
law
/alue
)2_CORR_7
PCT)
law
/alue
O2-DRY
(PCT)
Expression
Value
STK-FLOW
(scFH)
Expression
Value
(lLN: THC
:PPM)
law
y'alue
rHc_coRR
:PPM)
:xpreSsion
y'alue
8.96 7.O 1.33 1280000.0 6.9 12.6
9.04 7.0 1.47 1 280000.0 7.1 13.3
9.18 AA 1.59 1232000.0 6.9 13.0
9.08 ai 1.47 1256000.0 6.9 12.8
9.05 7.0 1.40 1346000.0 7.0 12.9
9.03 7.0 1.38 1280000.0 7.1 1 3.1
9.07 7.0 1.44 1 190000.0 7.1 13.2
9.12 7.0 1.47 1118000.0 7.1 1 3.1
9.04 7.O 1.40 1214000.0 7.0 12.9
9.08 7.0 1.47 1 298000.0 7.0 13.0
9.09 7.0 147 1 208000.0 7.1 13.3
9.05 7.0 1.40 1 226000.0 7.2 13.3
9.13 7.O 1.50 1 280000.0 7.0 13.0
9.04 7.0 1.43 1 226000.0 7.2 13.4
9.12 7.0 1.48 1 178000.0 7.1 13.1
9.09 7.O 1.46 1262000.0 7.0 13.0
9.08 7.0 1.45 1286000.0 7.2 13.4
9.07 7.0 1.42 1244000.O 7.1 13.0
9.05 7.0 1.43 1220000.0 7.2 13.4
9.11 7.O 1.50 1214000.0 7.0 13.0
9.17 7.0 1.58 1238000.0 7.1 13.4
8.90 7.O 1 .19 1268000.0 7.4 13.3
9.0s 7.0 1.38 1244000.O 7.2 13.3
9. 16 7.0 1.56 1 190000.0 7.2 13.5
9.25 7.O 1.65 1 190000.0 7.2 137
9.08 t.u 1.42 1268000.0 7.2 13.3
9.07 7.0 1.40 1304000.0 7.3 13.5
9.10 7.0 1.43 1280000.0 7.2 13.2
9.14 ai 1.50 1 1286000.0 7.3 13.6
9.11 7.0 1.49 1316000.0 7.2 13.4
9.08 7.O 1.5 L247400.O 7.L Lt.2
Project No. M2325124
Main Kiln Stack
75 of 166 @Mostardi Platt
Date/Time
:LINKER
JNHR)
:xpression
/alue
(lLN: CO
PPM)
law
/alue
KILN: CO2
(PCI
Raw
Value
co_MAss
(LBHR)
Expression
Value
law
uGscM)
upression
/alue
KILN: NOX
(PPM)
Expression
Value
NOX_MASS
(LBHR)
Expression
Value
06/20/202310:48 119.3 s82.1 13.57 476.4 1.410 232.5 312.6
06/20/2023 10:49 1 19.8 509.3 13.39 414.6 1.490 200.4 268.0
06/20/2023 1O:50 119 2 379.2 13.06 307.5 1.460 207.0 275.8
06/20/2023 10:51 1 18.9 294.7 13.66 238.0 1.430 225.2 298.8
)6/20/2023 10:52 1 18.8 457.8 13.81 369.1 1.380 218.7 289.7
X6l2Ol2O23 10:53 118 4 643.6 13.83 522.0 1320 213.0 283.8
)6/20/2023 1O:54 1 19.9 539.3 13.95 439.0 1.260 213.3 285.3
)6/20/2A2310:55 1 18.5 460.1 13.75 374.5 1.210 194.2 2s9.7
)6/20/2023 10:56 1 19.0 396.4 1 3.16 322.5 1.360 182.5 2M.0
)612012O23 10:57 1 19.9 321.0 13.38 261.3 1.5 10 '185.7 248.4
)6/20/2023 10:58 1 19.0 416.4 13.89 339.s 1.510 19s.2 261.5
)6/20/2023 fi:59 119.1 325.9 13.1 5 266.2 1.510 205.1 275.2
)6/20/2023 11:00 119.1 318.1 13.27 257.0 1.560 201.3 267.2
)6/20/2023 11:41 1 19.8 287.8 't3.06 231.4 1.620 219.2 289.6
)5/20/202311:02 1 18.8 326.1 13.32 263.9 1.550 219.1 291.3
)6/20/2023 11:03 120.4 358.4 13.64 291.0 1.480 264.0 352.2
06/20/2023 11:M 119.2 216.0 12.99 175.6 1.520 272.6 364.2
)6/20/2023 '11:05 118.9 157.1 13.55 128.6 1.550 308.8 415.5
X6/20/202311:06 120.0 233.s 13.97 193.0 1.290 334.4 454.2
)6/20/2023 11:07 1 19.8 382.8 13.69 3r3.0 1.010 326.0 437.9
)6/20/202311:08 119.2 419.3 13.28 340.2 1.140 31 s.5 420.8
)6/20/2023 11:09 1 18.8 435.6 13.35 354.6 1.270 321.4 429.9
)6/20/202311:10 1 19.3 397.5 13.37 325.0 1.310 293.2 393.8
)6/20/2023 11:11 120.2 690.3 13.68 560.4 1.350 255.5 340.8
)6/20/2023 11:12 1 19.0 466.8 13.15 3784 1.660 188.9 251.6
)6/20/202311:13 119.2 675.7 13.10 551.5 1.960 212.3 2U.7
06/20/2O23 1'l:14 1 19.5 765.6 12.96 627.9 1.620 217.3 292.8
06/20/?023 11:15 119.8 606.3 13.06 4949 1.280 221.8 297.5
06/20/2023 11:16 1 18.6 525.6 13.70 426.7 1.300 243.0 324.1
06/20/2023 11:17 1 19.1 M5.1 13.45 362.1 310 252.5 337.5
AVERAGE 119.3 434.4 13.44 353.53 t.42L 238.0 318.28
Project No. M232512A
Main Kiln Stack
76 of 166 @Mostardi Platt
(lLN:02
:PCT)
law
y'alue
l2-coRR_7
,PCT)
law
/alue
C2-DRY
(PCr)
Expression
Value
STK-FLOW
(scFH)
Expression
Value
(LN: THC
:PPM)
law
y'alue
IHC-CORR
(PPM)
Expression
Value
9.09 7.0 1.44 11262000.0 7.4 3.7
9.1 6 7.0 1.54 1 1202000.0 7.4 3.8
9.05 7.O 1.38 11150000.0 7.3 34
9.10 7.0 1.45 111 12000.0 7.3 3.5
9.06 t.u 1.41 'I 1094000.0 7.3 1.5
9.14 7.O 1.51 1't 160000.0 7.2 3.5
9.12 7.0 I.48 1 1 202000.0 7.2 3.4
9.12 7.0 1.47 1 1 202000.0 7.1 3.1
9.18 7.0 1.57 1 1 1 96000.0 7.3 3.7
9.06 7.0 1.39 1 1 202000.0 7.2 3.3
9.'10 7.0 1.45 1 1 220000.0 7.3 3.5
9.16 7.0 1.55 1 1 238000.0 7.2 3.5
924 7.0 1.65 1 1 1 18000.0 7.1 3.4
9.19 7.0 1.58 1 1064000.0 7.2 3.6
9.12 7.0 1.45 1 1 135000.0 7.3 3.5
9.07 7.O 1.42 1 1 t72000.0 7.3 3.5
9.12 7.0 1 .51 1 1 1 90000.0 74 5.O
9.13 7.0 1.52 1 1268000.0 7.3 3.6
9.26 7.0 1.67 1 1375000.0 7.2 ).t
9.32 7.0 1.74 1 1 250000.0 7.3 4.0
9.34 7.0 1.74 1 1 166000.0 7.2 3.7
9.36 7.0 1.75 1 1202000.0 7.2 1.7
9.08 7.0 1.43 1 1 250000.0 7.2 3.4
8.79 7.0 1.10 1 1 172000.0 7.4 3.2
8.97 7.0 1.33 1 1154000.0 7.4 3.5
908 7.0 1.49 1 1232000.0 7.2 3.4
9.07 7.0 1.45 1 1286000.0 7.2 3.4
9.01 7.0 1.37 1 1232000.0 7.3 3.4
8.97 7.0 1.33 11172000.0 7.4 3.5
9.02 7.0 1.42 1 'l 196000.0 7,4 3.8
9.L2 7.O 11.5 11196200.0 7.3 13.5
Project No. M2325124
Main Kiln Stack
77 ot 166 @Mostardi Platt
Date,/Time
CLINKER
ONHR)
Expression
Value
KILN: CO
(PPM)
Raw
Value
KILN: CO2
(PCD
Raw
Value
co_MAss
(LBHR)
Expression
Value
Raw
(uGscM)
Expression
Value
KILN: NOX
(PPM)
Expression
Value
NOX_MASS
(LBHR)
Expression
Value
16/20/202311:38 1 18.8 575.3 13.48 468.1 1.000 252.4 337.4
)6/2012023 11:39 1 19.1 454.7 13.61 369.4 1.000 254.4 339.s
16/2012023 11:40 1 19.3 432.2 1 3.51 349.2 1.020 271.8 350.8
)6/20/202311:41 119.2 508.1 1 3.19 414.1 1.030 261.1 349.6
)6/20/2023 11:42 120.1 626.9 13.76 511.7 1.240 212.6 285.'l
)6/2012023 11:43 120.2 526.9 13.89 425.2 1.M0 181 .3 240.9
J6/20/202? 11:44 1 19.3 398.7 13.43 32s.3 1.230 203.0 272.1
)6/20/2023 11:45 1 19.5 477.7 13.15 394.9 ''t.030 189.0 2s6.7
)6/20/202311:46 1 18.8 608.3 '13.09 500.5 1.120 201.8 272.8
)6/20/2023 11:47 1 18.9 721.6 13.24 587.7 1.210 225.0 301.1
)6/20/2023 11:48 119.2 440.2 13.72 358.3 1.250 227.6 304.4
)6/20/2023 11:49 1 19.5 327.8 13.26 268.8 1.300 228.7 308.2
)6/20/2023 11:50 119.1 3s2.2 12.97 288.9 1.180 226.0 304.5
06/20/20?311:51 120.1 270.s 13.33 222.'l '1.070 234.4 316.2
06/20/2023 11:52 119.1 602.4 13.24 494.3 1.170 224.1 302.1
06/20/2023 11:53 1 '19.5 699.3 12.89 571 4 1.280 241.1 323.7
06/20/2023 11:54 'I 19.5 526.9 13.38 430.1 1.1?0 248.1 332.7
06/20/2023 11:55 117 8 363.3 13.26 296.1 0.950 248.8 333.1
06/20/2023 11:56 1 18.8 244.2 13.67 197.6 1.080 254.3 338.1
06/20/2023 11:57 1 18.6 236.9 13.63 19'1.8 1.200 223.2 296.9
06/20/202? 11:58 119.1 390.7 12.81 31 8.6 1.200 195.3 261.6
06/20/2023 11:59 119.1 378.3 13.43 309.4 1.200 209.0 280.9
16/20/202312:00 120.0 642.2 13.46 526.4 1.180 198.0 266,7
J6/20/2023 12:01 120.7 687.5 12.86 5M.8 1.160 202.5 273.3
)6/20/202312:02 119.1 581.8 12.88 476.9 1.160 213.6 287.7
)6/20/202312:03 1 19.0 327.4 13.57 268.4 1.1 50 234.4 315.7
)6120/2023 12:,04 'I 18.5 533.7 1315 437.0 1.050 245.6 330.4
)6120/2023 12:OS 1 19.6 426.9 13.16 347.3 1.050 245.9 328.7
)6/20/202312:06 119.2 31 6.5 13.26 258.1 1.050 263.s 353.0
)6/20/2023 12:07 1 19.5 362.2 13.01 296.3 1.050 262.5 352.8
AVERAGE 119.3 458.0 13.3 382.32 1.139 229.3 307.s5
Project No. M232512A
Main Kiln Stack
78 of 156 @Mostardi Platt
KILN: 02
(PCT)
Raw
Value
f,2_CORR_7
:PCT
law
y'alue
O2-DRY
(PCT}
Expression
Value
;TK-FLOW
:scFH)
:xpression
y'alue
KILN: THC
(PPM)
Raw
Value
THC_CORR
(PPM)
Expression
Value
9.26 7.0 .66 1 96000.0 7.3 3.8
9.18 7.0 56 1 78000.0 7.2 3.5
9.16 7.0 56 1 18000.0 7.3 3.7
8.92 7.0 .25 214000.0 7.4 3.4
8.88 7.0 .22 232000.0 7.4 3.5
9.09 7.0 50 1 1 130000.0 74 3.9
9.25 7.0 71 226000.0 7.2 3.8
9.26 7.0 .67 376000.0 7.2 3.7
9.1 5 7.0 .49 1 1 322000.0 7.2 3.3
9.08 7.0 .41 208000.0 7.2 3.2
9.11 7.0 45 202000.0 7.3 3.5
9.10 7.0 .48 285000.0 7.3 3.5
9.20 7.0 59 286000.0 7.3 3.7
9.13 7.0 .49 298000.0 7.5 3.Y
9.18 7.0 56 292000.0 7.2 3.5
9.10 7.0 .43 244000.0 7.3 3.5
9.17 7.O 52 232000.0 7.3 3.6
9.10 7.0 48 214000.0 7.4 3.7
9.04 7.0 1 1.40 136000.0 7.5 3.9
9.04 7.0 .43 142000.0 7.4 3.8
9.05 7.O 45 220000.0 74 3.7
9.11 7.O .49 2s6000.0 7.4 5.t
9.'t4 7.0 52 280000.0 7.4 3.8
9.07 7.0 .45 304000.0 7.4 3.7
9.18 7.0 56 280000.0 7.4 3.8
9.17 7.0 54 280000.0 7.3 3.7
9.11 7.0 .45 268000.0 7.4 3.7
9.10 7.0 .46 1 96000 0 7.5 3.8
9.15 7.0 54 220000 0 7.5 4.1
9.20 7.0 .61 256000.0 7.6 4.4
9.L2 7.O .1.5 I r.235400.0 7.4 L3.7
Project No. M2325124
Main Kiln Stack
79 of '166 @Mostardi Platt
)atelTime
:LINKER
,rNHR)
ixpression
y'alue
(lLN: CO
:PPM)
law
r'alue
(LN: CO2
:PCT)
law
y'alue
co_MAss
(LBHR)
Expression
Value
Raw
(uGscM)
Expression
Value
(LN: NOX
:PPM)
ixpression
r'alue
NOX_MASS
(LBHR)
Expression
Value
)6120/202312:13 't 19.0 425.4 13.29 348.7 1.130 212.9 286.7
)5/2012023 12:14 1 18.9 493.5 13.22 405.8 1 140 199.8 270.0
)5/20/2023 12:15 119.2 747.5 12.91 616.0 1.150 198.5 268.9
)6/20/2023 12:16 1 15.6 703.2 13.69 574,9 1.220 199.4 267.8
J6/20/2023 12:17 120.2 525.8 13.62 425.3 1.290 201.2 267.4
)6/24/2023 12:18 119.4 400.1 13.18 323.6 1.160 209.3 278.1
)6/20/202312:19 1 18.9 453.8 13.25 370.6 1.030 219.8 294.9
)6/20/202312:20 119.6 511.4 13.34 419.6 1.040 223.9 301.9
)6/20/202312:21 1 19.8 348.4 13.77 2U.4 1.040 210.9 282.8
)6/20/202312:22 1 19.6 235.4 13.82 191.5 1.120 202.5 270.7
)6/20/202312:23 1 19.6 277.4 13.48 225.5 1.200 210.7 281.4
06/20/2023 12:24 120.3 444.4 13.59 359.2 1 130 211.8 281.3
06/20/2023 12:25 1 19.5 560.5 13.20 453.3 1.070 206.9 275.0
06/20/20?312:26 120.4 584.4 '13.58 473.9 0.990 224.8 299.5
06/20/2023 12:27 1 19.3 402.7 13.55 326.2 0.910 229.6 305.5
06/20/2023 12:28 1 18.9 259.3 13.08 208.9 0.970 229.7 304.1
06/2Q/2023 12:29 1 19.6 290.8 13.32 234.7 1.020 243.7 323.2
)6/201202312:30 1 18.8 456.8 14.07 371.9 1.000 241.4 322.9
J6/20/2023 12:31 119.s 618.2 13.51 509.2 0.980 246.1 333.0
)6/20/202312:32 119 4 599.6 13.07 493.6 0.870 243.8 329.8
)6/20/202312:33 1 19.5 655.4 13.1 5 539.2 0.770 231.2 312.s
)6/20/2023 12:34 1 19.5 599.2 13.55 494.6 0.900 2413 331.3
)6/2012023 12:35 1 19.3 409.6 13.27 339.3 1.040 252.7 3M.0
J6/20/202312:36 1 18.8 369.8 12.66 304.1 0.980 276.2 373.2
)6/20/2023 12:37 1 16.0 374.9 13.15 305.7 0.920 273.1 355.9
)61201202312:38 114.3 445.6 13.22 3il.3 0.940 263.5 3s3.9
06/20/202312:39 123.9 590.'r '12.74 4U.0 0.9s0 254.4 342.8
06/20/202312:40 122.9 602.9 13.32 490.5 1.010 207.1 276.9
06/20/2023 12:41 122.9 2M.3 12.89 1 99.1 1.050 217.1 290.7
06/20/2023 12:42 121.5 483.0 13.64 397.2 1.030 215.9 291.7
{VERAGE 119.5 470.4 t3.34 384.49 1.035 226.1 304.26
Project No. M232512A
Main Kiln Stack
80 of 166 @Mostardi Platt
KILN: 02
(PCr)
Raw
Value
o2_coRR_7
(PCT)
Raw
Value
O2-DRY
(PCT)
Expression
Value
STK-FLOW
(scFH)
Expression
Value
(lLN: THC
PPM)
law
/alue
THC-CORR
(PPM)
Expression
Value
9.13 7.0 1 .49 280000.0 7.4 3.7
9.15 7.0 1 52 316000.0 7.3 3.6
911 7.0 1 ,48 340000.0 7.4 ].7
9.02 7.0 1 .38 2s0000.0 7.2 3.3
9.09 7.0 1 130000.0 7.4 3.7
9.08 7.0 ,l .46 1 1 1 30000.0 7.3 3.5
9.19 7.O 1 58 238000.0 7.2 3.6
9.08 7.0 1 .43 292000.0 7.4 3.7
9.01 7.0 1 36 232000.0 7.3 3.4
8.97 7.0 1 34 1 1 1 96000.0 74 aa
9.09 70 1 .50 r 84000.0 7.3 3.6
9.10 7.0 1 50 124000.0 7.2 3.5
9.10 7.0 1 51 1 30000.0 7.3 3.6
908 7.0 1 .50 1 60000.0 7.3 3.6
9.09 7.0 .49 148000.0 7.3 3.6
9.04 7.0 1 39 088000.0 7.4 3.6
9.09 7.0 1 .45 1 1 1 06000.0 7.2 3.4
9.12 7.O 1 .49 202000.0 7.3 3.6
9.28 7.0 1 .58 334000.0 7.2 3.7
9.1 5 7.0 1 50 328000.0 7.2 3.3
9.03 7.0 1 33 322000.0 7.2 3.1
9.17 7.O 1 54 3s8000.0 7.3 3.7
9.04 7.0 38 400000.0 7.4 3.6
9.26 7.0 1 .64 31 6000.0 7.2 3.7
9.24 7.0 1 .62 220000.0 7.2 3.6
9.27 7.0 1 .63 250000.0 7.2 3.5
9.04 7.0 35 286000.0 7.2 3.1
9.09 7.O 45 196000.0 7.4 3.7
9.06 7.0 .39 214000.0 7.4 3.6
9.14 7.0 1 52 316000.0 7.2 3.5
9.LL 7.O 1.5 1 236200.O 7.3 r3.5
Project No. M2325124
Main Kiln Stack
81 of 166 OMostardi Platt
)ate/Time
CLINKER
GNHR)
Expression
Value
KILN: CO
(PPM)
Raw
Value
KILN: CO2
(PCD
Raw
Value
co_MAss
(LBHR)
Expression
Value
Raw
(uGscM)
Expression
Value
KILN: NOX
(PPM)
Expression
Value
NOX-MASS
(LBHR)
Expression
Value
16/20/202312:50 18.s 951 .5 14.40 771.7 1.000 237.1 31 5.9
)6/20/202312:51 18.6 453.2 14.44 366.6 1.140 254.3 337.9
)6/20/2023 12:52 18.9 282.7 13.34 229.3 0.940 270.5 360.4
06/2OD023 12:53 18.0 197.O 13.04 159.9 0.740 287.8 383.9
06/20/2023 12:94 18.7 155.6 13.16 126.8 0.730 283.9 380.1
06/2012023 12:55 17.6 380.3 13.05 311.2 0.720 277.1 372.6
05/20/202312:56 17.9 420.5 1 3.16 341.8 0.720 269.0 3s9.2
)6/20/202312:,57 17.8 651 .9 13.12 s30.1 0.710 251 .8 336.4
06/20/202312:58 18.5 581.9 12.95 478.O 0.810 233.7 31 5.4
)G12012023 12:59 19.3 661.7 r 3.05 543.0 0.900 241.5 325.6
)Gl2O/2023 13:O0 20.3 724.2 13.06 589.5 0.880 237.0 317.0
)6/20/2023 13:01 19.2 538.5 1 3.31 439.1 0.870 234.4 314.O
)6/20/202313:02 19.5 678.3 13.43 556.5 0.870 240.7 324.5
)6/20/202313:03 19.6 8946 13.07 732.9 0.880 243.3 327.5
J6/20/202313:M 18.9 i 053.6 13.14 860.4 0.870 228.5 306.6
)6/20/202313:05 18.4 1214.1 13.41 992.0 0.850 224.4 301.3
06/20/202313:06 18.8 827.6 '13.57 675.9 0.930 232.2 31 1.6
06/20/202313:07 19.9 51 9.8 13.54 424.5 1.010 240.1 322.2
06/20/202313:08 19.2 499.5 13.63 410.5 0.910 239.6 323.6
06ftA/202313:09 18.5 724.8 13.s3 593.5 0.820 226.0 304.1
06/20/2023 13:'10 18.s 1096.9 13.29 895.8 0.830 223.4 299.8
06/20/2023 13:11 20.o 1197.3 1 3.31 981.4 0.840 230.6 31 0.6
06/20/2023 13:12 20.5 822.7 13.42 676.2 0.890 230.2 310.9
C6/2A/2023 13:13 18.s 591.3 13.53 485.0 0.950 229.7 309.5
16/20/2023 13:14 19.5 840.5 13.08 686.0 0.9s0 237.4 318.4
J6/20/2023 13:15 18.7 1057.8 13.00 857.4 0.930 224.7 299.3
)G120/2023 13:16 18.8 808.5 13.45 659.2 ''t.000 214.9 287.9
)6/20/2023 13:17 20.0 539.8 13.32 442.2 1.100 215.4 290.0
)6/2O/2023 13:18 199 740.0 13 19 60s.6 't.040 222.3 298.9
)6/2012023 13:19 19.5 829.2 12.93 676.5 0.970 217.2 291.1
AVERAGE 19.0 597.8 13.33 569.95 0.894 240.O 32t.87
Project No. M232512A
Main Kiln Stack
82 of 166 @Mostardi Platt
KILN: 02
(PCD
Raw
Value
o2_coRR_7
(PCT)
Raw
Value
O2-DRY
(PCD
Expression
Value
STK-FLOW
(scFH)
Expression
Value
KILN: THC
(PPM)
Raw
Value
tHc_coRR
:PPM)
:xpression
y'alue
8.74 7.0 10.94 1 1 60000.0 7.5 3.1
881 7.O 1 1.08 1 1 30000.0 7.5 3.3
8.93 7.0 11 22 1 1 60000.0 7.4 3.4
9.10 7.0 11,46 1 172000.0 7.3 3.5
9.22 AA 1 1.63 1 214000.0 7.4 3.9
9.27 7.0 11.64 1 262000.0 7.3 3.8
9.32 7,0 11.71 'I 184000.0 7.3 3.9
9.23 7.0 11.61 1 190000.0 7.2 3.6
9.23 7.0 11.61 1 304000.0 7.2 3.6
9.20 7.O 1 1.55 1 292000.0 7.2 3.4
9.23 7.0 11.58 1 202000.0 7.2 3.4
9.26 7.0 11.64 1 220000.0 7.1 3.4
9.26 7.0 11.63 1 292000.0 7.1 3.3
9.30 7.0 1 1.69 1 274000.0 7.1 4.4
9.1 0 7.0 11.43 1 238000.0 7.2 3.2
9.1 5 7.0 1 1.50 11244000.0 7.2 3.3
9.11 7.0 11.45 1 238000.0 7.1 3.1
9.20 7.0 11 57 1 238000.0 7.1 3.3
9.33 7.0 11.77 1 310000.0 7.1 ).t
9.32 7.0 11.73 1 268000.0 7.0 3.3
9.23 7.O 1 1.58 1 238000.0 7.0 3.1
9.23 7.O 1 1.58 1 280000.0 6.9 3.0
9.27 7.0 1 1.53 310000.0 7.2 3.5
9.25 7.0 11.60 1 286000.0 7.1 3.3
9.15 7.0 11.46 1 232000.0 7.0 3.0
9.13 7.0 11.46 'I 154000.0 7.1 3.1
9.11 7.0 11.46 1 220000.0 7.2 3.4
9.18 7.0 11.54 1 274000.o 7.2 3.5
9.19 7.0 1 1.54 1 262000.0 7.2 3.4
9.01 7.0 11 31 1 226000.0 7.O 2.8
9.L7 7.O 11.5 11 235800.0 7.2 3.4
Project No. M2325124
Main Kiln Stack
83 of 166 @Mostardi Platt
Date/Time
CLINKER
ONHR)
Expression
Value
KILN: CO
(PPM)
Raw
Value
KILN: CO2
(PCI
Raw
Value
co_MAss
(LBHR)
Expression
Value
Raw
(ucscM)
Expression
Value
(LN: NOX
IPPM)
:xpression
y'alue
\ox_MAss
:LBHR)
ixpression
r/alue
X6/20/202313:40 17.6 1026.4 3.32 837.3 0.920 202.8 271.8
)6/20/2023 13:41 18.5 736.3 3.55 599.1 0.920 210.2 281.0
)6/2012023 13:42 18.8 768.4 3.99 624.2 0.910 211.9 282.8
)6/20/2023 13:43 19.3 695.5 3.58 568.6 0.900 211.9 2U.6
16/20/2023 13:4 '19.0 417.7 3.49 342.9 0.970 213.1 287.5
)6/20/2023 13:45 18.4 674.0 3.74 550.7 1.040 229.3 307.8
)612012023 13:46 19.2 68s.3 3.s2 558.2 1.030 228.7 3 06.1
)6/20/202313:47 18.4 729.3 3.s2 59s.3 1.000 223.4 299.6
)6/20/2023 13:48 19.2 783.s 3.54 u2.9 1.020 214.4 289.1
)6/2O12023 13:49 18.2 545 7 3.27 448.7 1.040 206.4 278.9
)6/20/2023 13:50 18.0 489.3 3.60 404.7 1.060 210.8 286.s
)5/20/202313:51 18.2 583.0 3.77 482.2 1.080 219.7 298.6
)6/20/202313:52 18.9 473.7 2.84 389.s 1.030 229.9 310.6
)6/20/2023 13:53 19.2 u6.7 2.86 528.1 0.970 228.7 306.9
)6/20/202313:54 18.5 647.8 2.89 527.6 0.910 217.9 291.6
)6/?0/2023 13:55 17.9 u1.7 3.12 517.9 0.840 210.7 279.4
06120/2023 13:56 18.4 546.1 3.36 441.7 0.900 216.9 288.2
06/20/2023 13:57 18.3 420.6 3.67 342.8 1.000 237.5 318.0
06/20/2023 13:58 18.4 375.0 3.34 308.0 1.000 245.1 330 8
06/20/202313:59 19.2 397.6 2.85 327.8 1.000 246.8 334.3
06/2012023 M:ao 19.4 532.8 3.03 435.4 0.910 2M.1 327.7
06/20/202314:01 19.2 635.7 2.97 517.5 0.790 221.5 296.3
06/20/202314:02 18.5 573.6 3,25 470.9 0.840 210.7 284.2
o5/20/202314:03 18.4 401.4 3.56 329.4 0.930 217.1 292.7
06/20/2023 14:04 18 5 508.8 3.46 418.2 0.890 217.5 293.7
06/20/202314:05 18.5 661.2 3.s1 545.7 0.820 211.3 286.6
06/20/2023 14:06 18.3 631.5 3.30 522.1 0.810 209.7 2U.8
06/20/2023 14:07 18.5 546.1 3.15 454.1 0.820 221.3 302.3
06/20/2023 14:08 19.0 631.6 3.5 5 527.1 0.830 223.9 307.0
06/20/202314:09 18.s 464.0 3.50 384.0 0.850 210.3 286.0
AVERAGE 18.6 595.7 3.37 488.09 0.934 220.L 296.5L
Project No. M2325124
Main Kiln Stack
84 of 166 @Mostardi Platt
KILN: 02
(PCr)
Raw
Value
02_coRR_7
(PCT)
Raw
Value
O2-DRY
(PCT
Expression
Value
STK-FLOW
(scFH)
Expression
Value
KILN: THC
(PPM)
Raw
Value
THC-CORR
(PPM)
Expression
Value
8.90 7.0 1.25 1 226000.0 7.2 3.1
8.97 7.0 1.35 1 '196000.0 7.1 3.1
9.02 7.0 1.42 1 1 78000.0 7.0 3.0
9.07 7.0 1.45 1 2s0000.0 7.2 3.4
9.10 7.0 '1.48 1 298000.0 7.0 3.0
9.22 7.0 1.60 1 24/'000.0 7.0 3.2
9.1 3 7.0 1.49 1 208000.0 71 3.1
9.18 7.0 1.55 1 232000.0 7.0 3.1
9.07 7.0 1.41 1 292000.0 7.2 3.3
9.05 7.0 1.38 1 316000.0 71 3.0
9.04 7.0 1.39 1 382000.0 7.1 3.0
9.22 7.0 1.63 1 382000.0 7.1 3.5
9.1 3 7.0 1.50 1 31 6000.0 7.1 3.2
920 7.0 1.58 1 238000.0 7.0 3.1
9.11 7.0 148 1 208000.0 7.0 3.0
9.15 7.0 1.54 1 106000.0 7.O 3.1
9.17 7.0 1.55 1 130000.0 7.1 3.2
9.24 7.O 1.63 1 214000.0 71 3.3
9.24 7.0 1.62 1 304000.0 7.1 3.3
9.33 7.0 1.73 1 346000.0 an 3.3
9.28 7.0 1.67 1 244000.0 7.0 3.3
9.17 7.O 1.53 1 202000.0 7.0 3.1
9.09 7.0 1.42 298000.0 7.3 3.5
9.13 7.0 1.47 1 292000.0 7.1 3.1
9.19 7.0 1.57 1 310000.0 7.1 3.3
9.15 7.0 1.48 'I 3s8000.0 7.1 f-I
9.27 7.0 1.64 1 376000.0 7.1 3.4
9.22 70 1.56 11442000.0 7.1 3.2
9.13 7.0 1.45 t484000.0 7.1 3.1
9.09 7.0 1.45 388000.0 7.1 3.1
9.14 7.O 1.5 11282000.0 7.L .3.2
Project No. M2325124
Main Kiln Stack
85 of 156 @Mostardi Platt
RUN 1
Datefiime
lCL_CORR
,PPM)
:xpression
,/alue
)6/20/2023 07:30 0.0
)6/20/2023 07:31 0.4
)6/20/2023 07:32 01
)6/20/2023 07:33 0.6
)6120/2023 07:34 0.1
)6120/2021 07:35 0.1
)6/20/2023 07:36 0.7
)6/20/2023 07:37 o4
)6/20/2023 07:38 00
)6/20/2023 07:39 0.1
)6/20120z-3 07:40 -0.1
)6/20/2023 07:41 0.0
)6f20/2023 07:42 0.9
)6/2012023 O7:43 0.9
)6120/2023 07:44 0.9
)612012023 07:45 1.2
)512017021 07:46 0.0
\6/20/2023 07:47 0.4
t6/20/2023 07:48 t.5
l6/2Q/2023 07:49 09
16120/2O23 07:5O 0.0
t6/20/2023 07:51 0.1
t6/20/2023 07:52 0.7
t6/2O/2023 07:33 -0 1
)6120/2023 O7:54 0.0
)6aODO23 07:55 0.4
)G12012023 07:56 -0.4
)G12012023 A7:57 o.4
1612012o23 O7:Sa 0.0
)6/2012023 07:59 0.4
\vera9e
v1 ax
vl in
:ount
0.3
'l.3
-0.4
30
RUN 2
)ate/Time
rcL_coRR
PPM)
lpression
/alue
)6/20/2023 08:07 -0.1
)6/20/2023 08:08 -0.1
)6/2012023 08:09 0.0
)6/20/2023 O8:10 0.1
)6/20/2023 08:11 0.7
)6/20/2023 08:1?0.4
)6/20/?023 08:13 0.0
)6/20t2023 08"14 0.6
)6/20f2023 08:1s 0.5
)6/20/2023 08:.16 0.'l
$124/2023 08:17 0.0
t6/20f2023 08:18 0.0
\6/20/2023 08:19 0.0
)6/20/?02308:20 0.1
t6/20/2023 08:21 0.3
t6/20/2023 08:22 0.4
t6/20/2023 08:23 0.4
t6/20/2023 08:.24 1.2
t6/20/2023 08:2s 0.4
t6/201?023 08.'25 0.0
)6/20/2023 08:27 0.0
)6/20/202308:28 0.4
)6/2012023 O8:29 0.4
)6/20/202308:3a 0.0
,6120/2023 08:,31 0.0
)6/20/2023 08:32 0.0
)6120/202308:33 -0.4
)6/20/202308:34 -0.4
,6/20/202308:35 0.0
\6/20/2023 08:35 0.6
\verage
vlax
v1 in
:ount
0.2
1.2
-0.a
30
RUN 3
)ate^ime
{cL_coRR
PPM)
:xpression
/alue
)6120/2023 08:43 -0.1
)6/20/2023 08:44 -0.1
)6/2012023 08:45 0.7
)6/2012023 08:46 0.4
\6n012023 08:47 0.0
)612012023 08:48 0.7
)6/20t2023 08"49 0.6
)6/2012023 08:50 0.7
\6/20/2023 08:51 0.7
16/2012023 08:52 0.7
\6/2012023 08:53 0.'l
16/2012023 08:54 0.6
15/2012023 08:55 0.6
16/2012023 O8:56 -0.1
16/20/2023 08:57 0.7
16/?0/2023 08:58 0.9
t6120/2023 08:59 0.1
)6/20/2023 09:00 0.0
)6/2012023 09:01 0.6
)6/20/2023 09:0?0.4
)6/20/2023 09:03 0.4
)6/20/?0?3 09:M 0.5
)6/20n023 09:05 o.4
)6/20/2023 09:06 o.4
)6/2012023 09:07 0.4
)6/2U2A23 09:08 0.0
16120/2023 09:09 -0.'1
\6120/2023 09:10 0.4
)G120120?3 09:11 0.6
16/20/2023 09:12 o.7
Average
Max
Min
Count
0.4
0.9
-0.1
30
Project No. M232512A
Main Kiln Stack
86 of 166 @Mostardi Platt
RUN 4
)atelTime
{cL_coRR
.PPM)
xpression
lalue
t6/2o/2023 09i35 -0.1
t6170/2023 09:36 0.4
t6/20/2023 09:37 0.4
16120/2023 09:38 0.4
t6120/2023 09:39 0.4
t6/20/20?3 09:40 0.4
16120/2023 09:41 0.1
t6lZ0/2023 O9:42 0.4
t6120/2O23 09:43 0.1
16/20/2023 09t44 0.6
16120/2023 09:45 0.4
16/20/?023 09:46 0.0
16/20/20?3 09:47 0.4
16/20/2023 09:48 0.4
t6/20/2023 09:49 0.0
16/20/2023 O9:50 0.1
t6/20/2023 09:51 0.6
t6/2012023 09t52 1.2
16120/2023 09:53 0.7
16/20/2023 09:54 0.0
1612012023 09:55 0.0
t6/20/2023 09i56 0.0
t6/20/2023 09:57 0.0
t6/20/2023 09:58 0.0
t6/20/2021 09:59 0.4
t6t20t2021 10..00 0.4
$l2A/202310:01 0.4
t6t2it2023 10:02 0.1
1612012023 10:03 0.6
16/20/2073 10.04 0.0
wera9e
v4 ax
vl in
:ount
0.3
1.2
-0.1
30
RUN 5
)ate/Time
HCL-CORR
(PPM)
Expression
Value
)6/20/2023 0:.12 0.9
t6t20t2023 0:13 0.4
\6/20t7023 0:14 1.5
)6/20/2023 0:15 0.0
)6t20t2023 0:16 0.0
)6not2023 O:17 -0.4
)6/20n023 0:18 0.1
)6/2012023 0:19 0.9
t6/20/2023 0:20 -0.4
,6t20t2023 0'.21 0.1
)6t70/2023 0..22 0.7
,5t20/2023 0:23 0.4
,5/24t2023 0.24 0.'t
)6t20no23 0:25 0.1
,5t?o/2023 0:26 0.7
)6t20t2021 0'.27 0.9
)5/20/2023 0:28 0.1
,6t20/2023 0:29 0.9
)6t20t2023 0:30 0.4
,6t20/2023 0:31 0.0
16t20t2023 0:32 0.1
)6t20t2023 0:33 0.6
)6t20t2023 0:34 0.9
)6/?0t2073 0:35 0.7
,6t?o/2023 0:36 0.6
)6/2012023 0:37 0.7
,6/ZO/?023 0:38 0.6
)6/20t2023 0:39 0.0
)6/?0/2023 0:40 0.0
)6/20/2023 o..41 0.4
Average
Max
Min
Count
Q,4
1.5
-0.4
30
RUN 5
Date/Time
.{cL_coRR
.PPM)
/alue
x6/20/2023 10'.48 0.0
16/20/20?3 '10i49 0.6
)6/20/2023 10:50 1.2
16/20/2023 10:51 0.1
06/20/2023 10:52 0.4
\6/20/2023 10:53 0.6
)6/2012023 10:54 0.6
16/20/2023 10:.55 0.9
\6/20/2023 10t56 06
16/?012023 10:57 0.4
,612012023 10t58 0.6
16/20/2023 10:59 0.7
,6/20/2023 1:00 0.8
t6t20/2023 1:01 -0.4
\6/20/20?3 1:02 0.0
)6t20/20?3 1:03 0.0
)6/2A/7023 1:04 0.1
t6t?0t?02?l:05 -0 1
)6120/2023 1:05 0.0
t6/20/2023 1:07 0.6
)6t20/2023 'l:08 1.5
t6t20t2023 1:09 0.5
t6t20t2023 1:10 0.0
\6/20/2023 l:11 0.4
t6/20t2021 1..12 0.'l
\6t20t2023 1:13 0.4
\6/20t2023 l:14 -0.1
)6t20t2023 1:15 0.9
)6/20t2023 li16 0.6
)6/20t2023 1:17 0.4
\verage
\,1 ax
\,lin
:ount
0.4
1.5
-0.4
30
Project No. M2325124
Main Kiln Stack
87 of 166 OMostardi Platt
RUN 7 RUN 8 RUN 9
Project No. M2325'l2A
Main Kiln Stack
88 of 166 OMostardi Platt
RUN 10
Project No. M2325124
Main Kiln Stack
89 of 166 @Mostardi Platt
Project No. M232512A
Main Kiln Stack
Appendix F - Fleld Data Sheets
AU0 21 M
DIVISION OFAIR QUATITY
90 of 166 @Mostardi Platt
Project Number:
Client:
Test Location:
Source Condition:
Test Engineer:
Test Number
StartTime:
End Time:
Test Tech:
'?z/Z f
tru /Nl/ 4uf
Duct Diamete-r // n Upstream Distufiance, Diamelers ruv !'^FlueArea ffi? t( DilrrnstreaqDisturtance,DiameieflFzu,t SS
Port-Length zrr " Portsize-..16o0t'PottTyp;&*r- PitotlD f"rc pitotGmdent(C) O-OztoPwUlE"Hg COz olo _ Wet Sulb Temp _ Leak C]rqpfs P,ss€d@Statc@"H2O Oz% DryBulbTemp _ pre Sfl tnctresH2O
P. ?,t/.){ "Hg Meter No. Ft Fluke # Umbiticat lD _
a?.4,4 g.*4
Port-
Polnt #AP
Temp.
OF ',8
Null
Polnt
Angle,
Ilegrees
Port-
Polnt#AP
Temp.
OF .IaP
Null
Polnt
Angle,
DegrceE
D.56 zo7 5 ,-t o.ffi 202 v
-7-o.bo 7r)v -?Q.52 706 Z->o..5q tu 7 s"8 zo7 a
-.1 n"a.?n7 -<(rc7 z
Z-/
*;
?ix Z A-l o.bo %:5hz1e)fi5?3
O.SZL zog I -1 D_{7 2oB 44o..15 207 ,-.1 U.'IZ 7D7
Averaqe A,r.U -iL-h
,44 xOOzi| + .32 x Oz% + .28 x tlz% = _ (lld)
Md , _18ws) + (18 x_Bun) =
t;
85-49 x coxE-Y Msx _Ps -(Ms)
-',,F:
sctnx60=_scfi
Rev. 1.3
91 of 166
VSx_FluoAEalSQ= 8cftn
17.641 x acfnr Ps =-TsoR
DS{01 Method 2 Pltot Sheet
Project No. M2325124
Main Kiln Stack
1n*2022
@Mostardi Platt
ft/sec(vs)
Project Number:
Client:
Test Location:
Source Condition:
Test Engineer:
85.49 x
DS{01 Method 2 Pitot Sheet
Project No. M2325124
Main Kiln Stack
VolumeElc Flow Rate Determlna0on Fleld Data Sheet.
Strad Time:
End Time:
Test Tech:
Pfl:i;:ry&# H3ik?[#'Ji$,1lT;i:Trtr"#_t
Port Lengrth ?.do ' ponsizelfuro I eontwe_@_m,iofrlL-p?ffimoe rt(c) o.frloe-* Z'l.lr!'Hg co".h Jl,stati@a,n:o o,%T "Wl:r#iY"-"'"ffi,ffi*
iw;i' kn.& h*-Y- urs,i,carrD
.4 x COz% + .32 x Ozgo + .28 x ilz% = _ (l{d)
Md '_18nrs) + (18 x_Brs) = _ (Ms)
Vsx_FlueAreax60= acfn
17.il7 x acfn' P?=- =_sctrn x60=_sdhTsR
Rar. 1.3
92 of 166
1t2tr202.
@Mostardi Platl
-ru,n
Port.
Point #AP
Temp.
OF .tr
Null
Polnt
Angle,
Degrees
Port.
Polnt #AP
Temp.
OF .laP
Null
Polnt
Angle,
Degrcea
o.{,722
-7-a.<<zob-r A<t LrlZ-1 o.qa .u'7
?_-0.L5 zo7'7-O,/all ZoB--I n <-i 7A4-q 2.e{-7 7)t /1 4 7-o-t
Average
(/sec(vs)
Project Number
Client:
Test Location:
Source Conditbn:
Test Engineen
Date: f ,,' .
TestNumber: T
Stail Time:
0:36T
Duc{ Dameter;L!_! Upstream Disturbanca, Daametem V,(plusArca 'l5a? ff Dorrvnsfeam Disturbance. Olameters7F
lortlgqCtl -r.4o' PortSize_/..rp,. 'PortTypeft.*, pttotiO_111 pFotCoemc1errt(C) s.7vop_w4 "Hg co2o/o tL weteubremp - teakclreqli'paEe-@
Static 'Ho Nz% n { q. o./tu pogt,37tncfies H;o
P, off;Hg- u[ter NoZ Huke # umbnicat tD _
Volumetrlc Flow Rate Determlnatlon Fleld Data Sheet
End Time:
Test Tech:
.44xCOz% + .32xOz0lo + .28 x Nz% = _ (Md)
Md x _18u,s) + (18 x_Burs) =_(Ms)
g5.4ex cprm--.,8F:
_Vs x _ Flue Area x 60 =
17.647 x
-.,pcfin
, Ps =
Ts oR
DS.O01 Method 2 Pltot Sheet
Project No. M2325124
Main Kiln Stack
ar{rrr
scfin x50 =_scfti
Rev. 1.3
93 of 166
1n5n0a2
@Mostardi Platt
Port-
Polnt #AP
Temp.
"F .@
Null
Polnt
Angle,
Degrees
Port-
Polnt #AP
Temp.
"F arE
Null
Polnt
Angle,
Degrces
['/06'7 ba 5-/n.18 905-7 o.lfE UR -,7 ll.L)2oh
-l '../h ,fr <4.45 zot
o.7a 20,-gr'n 3-l 10)
Z--/0,L4 2ltt 4-/0. h'zo'1.,D-58 o-,-7 t) /n?-za9
-7 n.57 ton -3 fr.:4 o.,14 206 n '41
Averaoe
n/sec(vs)
Volumetrlc Flow Rate Determlnaflon Fhld Datahtrzrrz Date:w
tVo- t
as-4ex cp'ffi"
SheetProiect Number:
Client:
Test Locatbn:
Source Conditbn:
Ted Engineer
_Vsx_FlueAreaxd)=
17.il7 x acfrn, PE
=TeoR
D9001 MGthod 2 pnot Shcer
Project No. M232512A
Main Kiln Stack
P#,&:Lffif 8,ffi#Htr*#ffi"€
Port Longth _?.oo " port Size/-q_, port fype:&|*_-pi[i6ffi-'-rut%rnasil (cJ ,.lpePy u-ott "Hs cor%J:!- Eaffi'Terp---+ t"ak clre*;pass€d@Sratic'c.r,c ,Hzo g\ -4 Dry Butb rem;
-
;f -ifil*o ,roh-# kn^,#- Fr";{= - fi*,3#,*esxio
Td Nunbel:
Start Time:
End Time:
TcstTech:
.F:
.4 x Coz% +,32 x Oz% + .28 x Nz% = _ (ilH)
( lld x_t.Brvs) + (18 x Brc) =_(Ms)
scfii x6o =_8dtr
Rov. 1.3
94 of 166
1nq20ia2
@Mostardi Platt
Poil-
Po{nt#AP
Temp..F .m
Null
Polnt
Angle,
Degroes
Port-
Polnt#AP
Temp..F ./aP
Null
Polnt
Angle,
Degrees
, \,1 .bt Z t-/fl-rri zoo7uibn€q 7l .?og ffibttl
%st-q o.?7)i -q 9/
'r -l o.5-l zo5 v-/a.t ?)-?ffi -4D -z o{L qA-t 2t*J zf o"./-r{'/, t/'4 zo?a -.1 o.35 202
_Avenge
n/sec(vs)
Proiect Number:
Client:
Test locafion:
Soure Condition:
Telt Engineen
Vs x _FlueArca x 60 =
'17.47 x ac.fn * PE
=Ts'R
DS-001 Mrthod 2 Pltd Sh6€t
Project No. M2325124
Main Kiln Stack
Volumetrlc Flow Rate lletermlnaton Fleld Data Sheet
hrr.ftz He:
Te$ Number:
StartTime:
EndTime:
TestTech:
ft.l cr*u lr*\LH.
Nr'-l.r4
1l/ttt
Dncl Diameter lt f! Upsteam Etistrbaru, Oiameters 4.t
FlueArca r.or ff Dirnsteam Didubanca, Diamaers-lr
Pod-Langth :-ro r Portsize-341'pqttywJa*f pitotiD ".ra pT6i6moent(ce) arre
7n?q_,Hg coz% wd6hTemp
-
r-ear<crpltir@
.4 xCOz% + .32 xOz% + .28 x Nz% = _ (irH)
( ttd x _18wt) + (18 x_.---..;Bws) =_ (il6)
Es.49x cp-.@-\l Msx Ps .F:
gcfrn x6o =_tcfll
Rorr, t.3
95 of 166
1n*202it
@Mostardi Platt
Port
Pold #AP
Temp.
OF .lAP
Null
Polnt
Angle,
Degraeo
Poil-
Polnt#AP
Temp.
cF .lAP
Null
Polnt
Angle,
Degrceg
l'l 0-51 q-oq t-/n-69-t 5b %g -2 7,?ro
.Y1 zlb9 -?.a zton3,o Lo2 .J ,l 2o9
z-t \.r;4. I lrr 7InD
z l-f tD nf,.-,t-4 Lo?
I eoq J?o6L LO
- arl D^' 7D1L >g rr 3,?,/fr,
Averaqe
n/aec(ve)
Volumetrlc Flow Rate DetermlnaUon Fleld Data Sheet
Projeci Number
Client:
Teet Location:
Source Condition:
Test Engineen
n'Il{ttt
k< co-,- l^*t.+l*k&t
{l"h
StartTime:
End Time:
TeetT€ch:
Wd BulbTerp
q-
Fluke #
Port Lengffr >.o ," Pod SizeJt&_' portTWelfuHrot iD_rbrta p6i6maent $) e,Aw
Dare: //ar'zlt , -, --TcgtNr.rmbcc T
lfr'.t?-
t0:41
3*a
Upotraam Disturbance, Uamaersq,rlt(-tt.\
tlornsfream Disturbance, Dhmeters Xl SS
LeakClteq|s Pass6d@
Pr€ 3.cl narrsn.opa,&tnctreg4o
UrDllklallD_
Dud Diameter t/ ft
Hueeree QfiFif
Py ?ta? ,Hg
Sfrc:!.(a'WStatic 'Hg
P,2l-0!L+tg
co2%_
Ne%
MeterNo.-.fL
Port-
Polnt#AP
Temp.
"F .E
Null
Polnt
Angle,
Degreec
Port
Polnt#AP
Temp..F "rffi
Null
Polnt
Angle,
Degnes
0.fi UO f-r t.1b
fr$zZ AJ-o '.t D '2
W??5U Jt2 -?
-,f '4f n rc5 '&It
7-/i)7.r?7 v -/n{9 ?tn.?01 7t)V -,n.b(7D9
-t €-fr,-,a.E7 tu9-9 /,',b5 -T n4z ZAB
Average
.44xCOz% + .3:l xO2% + .2E x Nz% =_(ilrl)
(_ Md x _l€ua) + (18 x_$rvs) = _ (Ms)
8s.4ex cp'mx-rf,IF:
-Vsx-FlcArsax60=17.&7 x-iacfin * Ps =-gcfrnx60=-gcfrrTs"R
DS{01 lrdlod 2 Ptld Sh.€t
Project No. M232512A
Main Kiln Stack
Rev. 1.3
96 of 166
1n5f2022
@Mostardi Platt
Itlscc(vs)
Prctject Number:
Client:
Test Location:
Source Condition:
Test Engineer:
Volumetric Flow Rate Determinatlon Fleld Data Sheet
h.t"rf)z Date: L
$tq q..t lb-,tVl-
nR Start Time:
End Time:
Test Tech:
P.en./
Vatq
Duct Dameter ll \ Upstream Disturbance, Diameters -'l(( .r.r* r{,r
FlueArea T.g? tr Downstream Disturbance, oiametersEr^ gS
[::iffi 'r"'"nsfT"#_ortrvoe;ffi *i''-to"'t_*'Tili3tffi
Static "Ho N, % B* eost fltncfres H2o
P. LlT"ag' u'"rcr rt Ftuke # UmbiticanD _
Date: b/t/ef
Test Numbec ' Q
fite
Port-
Polnt #AP
Temp.
OF ar6
Null
Polnt
Angle,
Degrees
Port-
Polnt #AP
Temp.
oF .@
Null
Polnt
Angle,
Ilegrees
t-0.bi ?to 3-/o.57 zoq
-Z 0/(c<
Ot tt t/7. <5 2t t)-(?t -5 ().({-l 2p
r? ?l ?o6 -7 o. z(o ?nD
z-l f) <7 2-o1 r-/o.ha zib
zJ s*7 7aQ -z O./"b Za7
vtq -,o.qz ?o7.Y o3r loo -Y o.99 26
Averaoe
.44 x COzolo + .32 x Oz% + .28 x Nz% = _ (tftt)
Md x
-l€nr)
+ (18 x_Brvs) =
as.49x cp-.@-
Y _Ms x _Ps -
(Ms)
scfrn x00 =_scfi'l
Rev. 1.3
97 of 166
',,m:
Vs x_FlueArea x 60 = affi
17.&47 x acfin , PS
=
Ts oR
D$001 Method 2 Pitot Sheet
Project No. M2325124
Main Kiln Stack
1n1nt2:L
@Mostardi Platt
ft/sec(vs)
Proiec't Number
Client:
Test Locatbn:
Source Condition:
Test Engineen
Volumetslc Flow Rate Determlnatlon Fleld Data Shest . .,fi?lZrtc Date: 0''- "
I4A G.a {.htu*L Test Numben ?
StartTime:
End Time:
TestTech:
DrHDiameter ll i UpstrreamDisturtance,Diameters -f*f - q,f
rue a'rla qlTf ff Dirwnsfiea4-Dishrrbance, oiameLrs$ ii
PortLene6h ?-'-i-portsize-.t[-o 'Po1rvw-fi4-PitdtD-fla pr"tco"r6nt(ce) r.atcPvl{-l?l'yg co2yo- weellufemp
-
l-eakchodkjpasseogStratcrse"l-l2o q% DryBulbTemp _ prc 9,1 tn*l€H;OStalic_'Hg Nz% _ B," pogt 8.9 lncfresl-l2oP.21.r'l +19 lbterNo. F? Fluke# UmU[cailD_
llz38
th{'frt I l2:07T1(/t/tu,
Port
Polnt#AP
Temp.
cF .m
Null
Polnt
Angle,
Ihgreeo
Port
Pdnt#AP
Temp.
OF ar6
Null
Polnt
Anglq
Degrees
/s ?**Lto '4-t n5-t 20D
-7 u oto r)D.57-2rt
-?'lw\irto I l-r lf'{0 I z.t 1
-Y ) l)t/7st{o 4.7.?2oo
Z-l 0-o?-k)D / a/il.bo 7D?
, n.4^fr,D- s5 ,70
'S lf) /o2 7tD tJ o- 5<7rOn).4(o z0-7 tU 0-56 7r*-
Averaoe
.4 x COz% + .32 x Oz% + .28 x Nz% = _ (iid)
(_ ird x _18ue) + (18 x_Blr) = _ (Ms)
as.49x c:p'-@* .l;;-:T MEx _Ps
_ Vs x _ Flue Arpa x 60 = acfin
17.647 x acfnr t=P1- =-sclh x6O =-scrhTst
OS.001 M€tlod 2 PltotShod
Project No. M232512A
Main Kiln Stack
R6rr. t.3
98 of 166
1nsnox,
@Mostardi Platt
ttlsec(vs)
Proiect Number:
Client:
Test Location:
Source Conditbn:
Test Engineel:
P. ?itr( "Hg MelerNo'??Fluke #
.4 xCOz%+ .32 x Oz% + .26 x Nz% =
-
(Md)
( iid x
-18tt)
+ ('18 x-Bns) =
StartTime:
End Time:
Test Tech:
Umtillcal lD-
-(Ms)_.l F : _ilsec(vs)
Dud Danrcter lt ft Upstraam Disturbance, Diameters lt!31r"^ {.1-
rueRrea gFer ff Do,rrnstream Disturbance, oiamaers:L(+^rr 55
port teng'th-z.r-' Port Size-.gg' PotlTyp-ft+-Pitoll} Stcr7 pitA-Coefriern.(C) 0.1'top*l(.Eyag cozo/o- wetEulbTemp
-
LeakcjtgxsPassed@
SraUi vca 'rLo o2% Dry Bulb TEmp Pre .lrflnches l-l2O
Static 'Hg Nzo6 B* Pwl .fo!.hdns H2O
85.49 x CP x
Vsr-FlueAreax60= ecfin
11.&47x acfn, Ps =-scfinx60=-scfii
Ts oR
DS401 Method 2 Pitot SlPet
Project No. M2325124
Main Kiln Stack
Rev. 1.3
99 of 166
1n*2022
@Mostardi Platt
TI'/'
Port-
Polnt#AP
Temp.
"F .aF
Null
Polnt
Angle,
Degrces
Port-
Polnt #AP
Temp.
OF .IAP
Null
Polnt
Angle,
Degreee
PI o.@ z((4 0.51 ZU)
.?A <f)zr/.?o.6t za?
rl 0.55 zlt 'a qu-?-to
-4 o h.T 2tt)a 0..r5 2aR
/-/U.GZT,=E
t0/U-(rO ?t
r)lm '7 /t.5-7 Zo9
-l (/,s'4 Zo -?%*#,]o
'7 n1b ?ttL -u 2d9
Averaqe
Volumeklc Flw Rate Determlnatlon Fleld Data Sheet
Proiect Numbcn
Client:
Tqsl Locatbn:
Source Condition:
Tet Engineer
rtt?,rirz Date: fo/Zo/Zq
TestNumber: TStartTime: 1/,:dO
EndTime: TTestToch: tfiA
t{.t
,.e
Pibt Coefidenl (CJ &l{o
L€akGheds Passed@
F[,#;mffi
UmbilkellD_
Upstream Disturbance, Dlametera j{(l-;11r;.
t),ornsream Disturbance, Diameb(fl.on
sc'linx60=_8cfri
Rcv. 1.3
100 of 166
Duct Diarneter / fl
Flue Area x,-tl ff
PsA*8 "Hg caz%_W€[ Bulb Terp _
Dry Bulb Temp
-q.
Fluke #
glgtic'0fo "H2O q%
Stdic "Hg Nz%P,!j:H_,Hg Meter
.44 x COz% + .32 x Oz0lo + .28 x Ne% = _ (ttld)
(_ ttld x _l8rm) + (18 x_Bws) =_ (irls)
Bs.4sx cp-m--1F:
_ Vs x _ Flue Area x 60 - __-_ecfir
ik']
17.847 x acfin , PS =
Ts oR
DS{01 Mctrcd 2 PltctSlEct
Project No. M2325124
Main Kiln Stack
tninoin
@Mostardi Platt
Port-
Polnt#AP
Temp.
OF .laP
Null
Polnt
Angle,
Degreeo
Port
Polnt#AP
Temp.
OF .fi,P
Null
Pdnt
Angle,
Degr€eo
lzf Ol t ?op 7-/u51 '?*^
-c
m z ,-Z 05d al/
-,2t A, .<z zt(
u(l 4,n37 7-Cl
Z-/l-lat zwl ?-/46,)n.€"
?//
-Z '.92 7ro -/Llt
L Z ,-l er.>G
0. ?c
z//
) !/o ?).-{,,,,,,.%,.-
Averaoe
ftlsec(vs)
Volumetrlc Flow Rate Determinatlon Fleld Data Sheet
Project Number:
Clbnt:
Test Location:
Source Condition: ilurnl End Time: 14:09
Test Engineer. 77ffi TestTech:
Vs x _ Flue Area x 60 =
17.647 x acfrnr,,,Ps =-scfrnx60=-scfi1Ts"R
Date: l/t,/zt
TestNumber: T
StartTime: ffi
n/Qr/?wHT
Duc{ Diamete, lL I Upstream Disturbance, Diameters J&f'rr^r". ut.L
FlueArea qtAT-t Dbwnstrsam-Disturbance, Oiarneters&"-. f-9
lortjglglh '?oo t PortSize-jfo 'PortTypeifuaPltdlDtdlL pitoiGmc*ent(Cl tlv.
PvZf.V? "Hg Cozo/o
-
w€{ Bllb Temp
-
Leak Q!e{s Passed@
stiatic-46 "H2o ozo/o DryBulbremp pre o.8 lnchesl-l2o
Static , "Hg Nz o6 8." Posi. q. I lnches H2O
P.2/.3'{ "Hg MeterNo._flf Fhke# UmbiticailD_
.44 xCOz% + .32 xOz% + .28 x Nz% = _ (ttld)
(- Md , _18ns) + ('18 ,_Bws) = _ (Ms)
85.49* cp-!---.,'zF :
-rv'sec(vs)
DS-001 Method 2 Pltot Sheet
Project No. M2325124
Main Kiln Stack
R6v. 1.3
10'l of 166
1nq2022
OMostardi Platt
Port-
Polnt#AF
Temp.
OF .ffi
Null
Point
Angle,
Degrees
Port-
Polnt #AP
Temp.
"F .@
Null
Polnt
Angle,
Degree
tlh I Ltl /1 h0 tu9
-1 n_17 ? tl -?4.55 vto.?o.5l ?tl .,n)_ eq 7JtqONazb-)4 o..{o 7o
4-/0-lo-ZffI q-t D.6t /to
*,4 zu -7 o.57 .Ztrzl/-t o-SG 1t
"t/0.\q zob ry o..{o ,,lr<
Average
Date: l,-2O- V
Source Condition
Run Number:
prssu,", ZEFF-
Notes;
Dry Gas Meter No.lUa:
Traln A:
Traln B:
Ds-02 I
Eeri?gt ffif ffi ffi1 r'o
Main Kiln Stack
i:=Ifi liff l-:#:I;j;::""rff ?,
( M ust be l l 5" H s )
Fr,l;::ltrlfff:l;;::," ,,11r
(u,ustber is"Hg)
testengineer: StacE--r".r y=
Dry Gas ttrebr No. Pl l,l ? y = O g 1-l
102 6ts168.1 or{ffilurl Platt
Ohio Lumex Co., lnc'
Hg Sorbent Trap Chain of Custody Form
Trap lD
ilililllllililll[lil]l
o1647045
QA/QC Signature ffrapAsa,erv)i ,%Z r
EI UNSPIKED
Production Lot U-1128
Carbon Lot 19
QA/QC Signature tsot l:
tr SPIKED AT:
Spike Date:
SpikeTime:
tr High Florr tr FluffyPrefilter El 185mm
tr Static Prefilter tr AGS tr 300 mm
TypeofTraP: 308
tr 240nun
tr 450nm
SAMPLING INFORMATION
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (OPtional):
Sampling Train: eb trB
PRE-Run LeakCheck tr PASS
Run Start Date/Tims
Run End Date/Time:
Run Number (optionaD: . "
POST.RUNLCAKChECK trPASS
tr FAIL
I
". _. t.*. " ."
O FAIL
SAMPLING OONDITIONS AND PARAMETERS
Avg. DuctTemP{F"):
Avg. Trap TemP (F'):
Avg. Flow Rate (cc/min):
TotalVolume (L):or (dscm)
Estimated Avg. Hg Concentration (Ug/dscm]
Event Occuned During Sampling: tr Startup tr Sttutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
REQUIRED IF RETURNTNG TO OHIO LUMEX
lfl€:lnatlar.di,rrtin rar{B nf,0c$rbss.d- o*, J.iJi^z ilne lerrl,rsycsi hJoau*irr*4r"i, Phasecotf,act us f}q',"qilss*{trGatintli{dt/6 t'lp'
CHAIN OF CUSTODY
@bn.is_a maiorcalsc measurerEnt sdb€rlr trap6 and
En-srre sampiffi-condfiions prevent misture corld€nsaton mrE Irap rHB' Mq5turswr*.- Mr E e
$.fiiriil;tffi'cad vap", roscpim v]i rt'plnger spargi'q certried rcruracv t tolt' TtaceaHe to N|S.r
Best Before: June 2025
,\ 30350 Bruce lrcf,icHElUPheu.V Cleveland, oH 44139 USAwwwCIli8fdrQfrx.com
[e-mail]
lf applldPlacechahof
$Jstody seal ttere-
(see secrrity seal instnrtion
sheet)
\rrflfitrlHg'aflgl$::""
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form uttilriiliililtltultl
oL607247
E UNSPIKED D SPIKED AT:
Production Lot U-11DA SPike Date:
Carbon Lot 4C Spike Time:
QA/QC Signature 1sp,rc1:
SAMPLING INFORMATION
QA/QCSignaturecrnpA:*muy)i (\/
tr High Flow tr Fluffy Pre-filter
tr Static Prefilter tr AGS
TypeofTrap: 308
El 185 mm tr 240 mm
O 3fi) mm tr 450 mm
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: O A
SAMPUNG CONDITIONS AND PARAITIETERS
@
PRE-Run LeakCheck tr PASS
Run Staft Date/Time:
Run End Date/Time:
POST-RunLeaKCheck trPASS
I
I
tr FAIL
tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F"):
Avg. Flow Rate (cclmin):
TotalVolume (L):
Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: tl Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAI}.I OF CUSTODY
condilions prerent moislurs ctndensatioo in the lrap media. Mol$ure condensation is E mea9uremenl traps and should be nrev€nted
Spiking Method Cold Vapor Adso.ption Vra ln{ringer Sparglng Certified Accuracy t 1 0%, Traceable to N IST
Best Before: January 2026
30350 Bruce tnffitU$f5'tltBlfll
Cleveland, OH i14139 USA',*r.o1t*6RJ,{rQt..o*[e-mail] ?
lf applicable place chain of
custody seal here.
(see security seal instruction
sheet)
Seal intact as received:
ves E ruo[
\ flEf$t$,ffiffilH.
MERCURY SORBENT TRAP FIELD D4TA SHEET
Project Namer/Number:
23esi 2
Sampling LocaUon:
Dat6: L-)o'a'
Source Condition:
Ory Gas Moter No.
DryGas uebrNo. w\h? v=O,{$F rrap Numberi$Il-Cl _ Spil<e Value ng
Nobs:
Traln A:
Traln B:
Pre-TestLeakCheck-Pass @ lb "Hg (MustbeI l5"Hg)
Poet-Test Leak Check - Pass @-L6 "Hg
Pre-Test Leak Check- Pass O-Tq "Hg (Must be 2 {5"H9)
Pct-Test Leak Gheck - Pass @i-}-"Hg
Sample Traln A ,
tet r Voluma
,v-l lthn
xat rTomp.
(b,
.F
tetarVacuum,
1{q
sbrDeilr6pt ITomP. I'f ____l
Stacl Temp.
rF
g.i D-]tf Eq q zb5 201
q'l ?q.ol?GO ?62 2oLt
8'. r-1 l 6 .6L4 (,O (?f,"1 zo6
9,.a2 lq"o60 bt (7bl ?'c1
n. 7_-I 2,0.o5 r.l 6r s 2(,'0 ?-o t
R --1,2 z( ^ o?(L2 5
"-a
o ?,OG
9.1"-1 '\o- ott t
TdalrAvertge Lo. {205
Sample Traln B
ChckTlme
,lhilr
t brvolum.
,1,-l lll.B
llcbrTemP.
(r.)
.F
XobrVrcuum,
'l{a
5li n-l b 5q 5
8'. l?9.o35 GO S
P'- \-1 io.0?-l 60 S
l{.," z lB.03tD (6l 5
5tz'l -t-O.6:.1 5 (ol 5
l'. "?LS.O\q tu?5
':t-1 10. r":i\
TdaUAvenge [oO.(
os{pvafl sffi ?ff 36rocnt rrap 105 of '16ftEy. 2.1 @Mostd{lill0Et
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
il|liltfliltilililffilt[
o1607094
E UNSPIKED tr SPIKED AT:
Production Lot U-'11D9 Spike Date:
Carbon Lot 19-.. -* _.- ._ Spike Time:
QA/QC Signature oiur:
SAMPLING TNFORMATION
QA/QC Signature rrapAsrcntry)r h4
tr Hph Flow tr Fluffu pre-filter
tr Static Prefilter tr AGS
TypeofTrao: 308
tr 185mm U 240mm
tr 300mm tr 450 mm
a
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time:
tr PASS
--".-.-"..-- _ I.
_ _ "_t.
tr FAIL
SamplingTrain: ttrA/ trB'\-/
SAMPLING CONDTTTONS AND PARAMETERS
POST-RunLeakCheck trPASS tr FAIL
Avg. Duct Temp (F'):Estimated Avg. Hg Concentration (Ug/dscm): _ _
Event Occuned During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
Avg. Trap Temp (F'):
Avg. Flow Rate (cclmin):_ _
IotalVolume (L):---. , __.._.. or (dscm)
#of RAW MILL OFF events during sampling:
REQUIRED IFRETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OFCUSTODY
:i:1 1"_ :Tp,'nl:c?ndr,ons pr
spmng lvtenod cold vapor AdsoQtbn Via lmpinger Sparghg cenrfied Accuracy r t ore, tncreaote to t tist
measureman be treveflted.
106 of 166
www.ohiolumex.com
[e-mail]
@Mostardi Platt
O 30350 Bruce lndustrial Phry.V Cleveland, OH 44139 USA
lf appllcaUc place ctrain of
custody wl here.
(see security seal instnrtion
sheet)
Seal intact as receirred:
ves El No fl
Sample(s) received by lab
\ fffigBffi+HY4ffi""
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
Trap lD
ilililttlilililIililtil
o1c182028
til
A UNSPIKED
Production Lot U-l1DA
Carbon Lot 4C
QA/QC Signature Fpik ):
SAMPLING INFORMATION
tr SPIKED AT:
Spike Date:
Spike Time:
QA/QC Si gnatu re Orae asccntry):
tr High Flow tr FluffoPre-fitter E 18Smm
tr Static Prefilter tr AGS tr 300 nrn
TypeofTrap: 308
tr240mm
tr 450 mm
Facility / Sourcs
Boiler lD
Sampling Location:
Run Number (Optional):
Sampling Train. tr A
SAMPLING CONDITIONS AND PARAMETERS
PRE.Run LeaKCheck tr PASS
Run Start Date/Time:
Run End Date/Time:
POST.RunLeaKChecK EPASS
I
I
D FAIL
tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F"):
Avg. Flow Rate (cc/min):
TotalVolume (L):or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OF CIJSTODY
measu,efipnt sorbent traps and
Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
107 of 166
www.ohiolumex.com
[e-mail]
Best Before: January 2026
OMostardi Platt
30350 Bruce lndustrial Pkwy.
Cleveland. OH t14139 ti-qAI
lf appficable place chain of
custo{ seal here.
(see security seal instruction
sh€eq
Seal intact as received:
ves El ruo EI
ves E ruoE
intact as receit/ed:
ves EI No El
tffia?fr362611toll free
Sampling Location:
o",". 6-ao_13
Projecl Name/Number
MERCURY SORBENT TRAP F DATA SHEETz
Run Number: 3
Presrure: zqg-T-
TestEngineen Stnccr
-r,"prU-rrnU"t@
Sample Traln A
Clock Tlmc
)/, han*
HeterVolumc
A/-l llhr
lt t tT.mp.(t).c l/htar Vacuum,rl.la
Sodcnt fr.pc
Temp..c Strck Tcmp
.E
R: LIT o b7 5 z 6-t zorl
RiLIg 5,Ozcl furll 26U 20H
8: 6",I O. A?-1 (^Ll q z@l z orl
a : qFt lq ot{I (^Ll s ?(ol 20 t{
(lcq ",0'e
frH#Gr.l q z,60 zott:ort 25.66t t^5 -1 zbo 2-O I
'.la ?0. ott'l
ToleuAvDr.go d"q,U 2.oq
Notes:
Traln A:
Train B: Pre-Test Leak Check - Pass @ l'1 :'Hg (Must be l l6"Hg)
Post-Test Leak Gheck - Pass @[(?]'ttg
Ds-0r'Uacffi0d. 308310 &$ent Trap
Main Kiln Stack
DryGasueerNo.M.Fa v=-Qjsl-rrapNrru", OL{r\1J'}5 sp$<evalrr-..pg
Samole Train B
CbckTimc
2a ho.rr
IetprVolune
lv-l lll.a
t LrTomp.
(r.)
aF
htotVacuum,iUa
x'.Lt?o (oZ g,
8'.r{ I b.Dtlla Io>q
R. ('!ro.os I bi 5
r:sR.1s350 ba Eqi0".2r. ot{?(o3,5q:oP L9_o 3 I (ort q
q'-ta sC).o SLI
TotauAvertgo G),o
Pre-Test Leak Check - Pass @ I Q "Hg (Must be 2 t5"Hg)
Poet-Test Leak Check - Pass @-l-b-"Hg
108 of 1Bv.2.1 @Mostfft292lt
Onr UMEX Ohio Lumex Co., !nc.
Hg Sorbent Trap Chain of Custody Form
B UNSPIKED tr SPIKH) AT:
Production Lot U-11DA SPike Date:
Carbon Lot 4C SPikeTime:
QA/QC Signature (spit et:
SAMPLTNG INFORMATION
QA/QC Signature ffoe Arsnt]v):
tr High Flow tr FluffY Prefilter
tr Static Prefilter tl AGS
TypeofTrap: 308
mmruillfiIiilfttuttttu
o1c181888
E 185mm
tr3fi)mm
tr 240mm
D 450mm
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time: -
tr PASS
_t
I
tr FAIL
SamplingTrain: F
Avg. Duct TemP (F ):
Avg.Trap Ternp (F ):
Avg. Flow Rate (cc/min):
TotalVolume (L):
trB POST-RunLeakCheck trPASS T] FAIL
SAMPLING CONDITIONS AND PARAMETERS
Estimated Avg. Hg Concentration (pg/dscm):
Event Occuned During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:or (dscm)
REQUIRH' IF RETURNI}S TO OHIO LUMEX
Estimated Hg Mass in Section 1 of SorbentTrap (ng): -.-'-.--'iloteAn4arce5rd,r"rgErdbesetb.scda, rr&,oL'&iirg t* 0rl{,tnsyrallhod{r{ffii.a.rrdr Ressmttd'8tr}q',uqi?<*r'-tc!Gsli?ulil9rnbEtr
CHAIN OF CUSTODY
rEa$refirent
Stfiill;fril";ilUil*fi6iio.,ni rmpit'serspatsl"ecertified accurrvt loeLrraceablcto Nlsr
Best Before: January 2026
30350 Bruce r rffi #Ufl P?tnry'
Cleveland, OH 44139 USA
***.t9?i8[,.1&%,..o,
[e-mail] ?
lf ryficaUe Place chain of
custoryseal hre.
(see security seal instruction
sheet)
. Proiect No. M232512At , rAif,40e6Gffioo office*' 1 888 87Gzo1l tollfree
ilffiililrilf,fulurln
oL647LO4
QA/QC Signature firapAss$pry)l ,/ffi f
QA/QC Signature cpir"l:
tr Hiqh Flo/', tr Fluffo Prefilter El 185 mm tr 240 mm
tr Static Pre-filter tr AGS tr 300 mm E 450 mm
TypeofTrap: 30B
SAMPLING INFORMATION
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
E UNSPIKED
Production Lot U--11?B_
"
Carbon Lot 4C
tr SPIKED AT:
Spike Date:
Spike Time:
Facility / Source:
Boiler lD:
Sampling Location:
Run Number(Optional):
Sampling Train: tr A
SAMPLING CONDITIONS
@
PRE-Run Leak Check
Run Start Date/Time:
Run End Date/Timq
Run Number (optionat):
POST-Run Leak Check
tr PASS
tr PASS
tr FAIL
tr FAIL
AND PARAMETERS
Avg. Duct Temp (F'):Estimated Avg. Hg Concentration (pg/dscm):
Avg. Trap Temp (F'):
Avg. Flow Rate (cclmin):
Total Volume (L):
Event Occuned During Sampling: O Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEI(
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OF CT,,STODV
moisture condercation ln the lrap rnedia Moisture condensatbn is a rEuor cause measure{nent
Spiking Method Cold vapor Adsorption via lmpingEr Sparglog Cfiifled AcairBey r 10*. Traceable to NIST
Best Before: June 2025
30350 Bruce t n&lUffikriltB{dl
Cleveland, OH it4139 USA
**r.dt1&RJ,1&.com
[e-mail] I
lf apdcaUe place chain of
custody seal here.
(see security seal instruction
sheet)
Courier/Other (if applicable)
S€al intact as received:
ves E NoE
Seal intact as received:
ves E r.ro I
\ fr'tr$ilnB,l€ffifi1h"
Projecl Name/Number
MERCURY SORBENT TRAP FIELD DATA SHEET
Run Number: t{
Source Gondition:
DryGasMeterNo. l1n?-
Train A:
Train B:
De02 1 0{61€e0 fl $ffin$effi r rnp
Main Kiln Stack
PrdTest Leak Check - Pass @ I (o "Hg (Must be 2 l6',Hg)
Post-Test Leak Check - Pass @j=G_-"Hg
Pre-Test Leak Check- Pass @ | b "Hg (Must be l 15,,Hg)
Poet-Test Leak Check - Pasr @-I-b "Hg
Notes:
Sample Traln A
Glock Tlme
2ilhout
iloter Votum.
lV-l lllnn
Heter T.mp.(t)
.F ilebr Vrcuunq
'tI^
SorDant TrlPa
T.mp.
.F Stack Tcmp.
.Fq'.B5 o b5 5 Z(oO
"-o
sq:qo 5. Oqt b*t;zb0 2oqq.'Ll5 t0. o50 (.5 5 ?r0 2 65q:so l< bql L(^s "lo
C 20Lq:.((,zo,o q\G s L60 ?-o Glo:oo ZE-ot{q Gb 9 '?-t Q '?ab
lo"05 3O. o29
TotaUAverege br-t ZoS.S
DrvcastutebrNo.tlhl- v-!"!8L-Topr.rurr"r OLclS{o181 spkevar,e 25 ng
Samole Traln B
CbctTlme
2{ hour
llctar Volume
lV-l lllna
t brTemp.
(t.).t lLoarYacuun\
'llort 135 o 6r 5
:Ll o 5.o3-r (or{sq:q 5 lo,oz?(rLl
:.qo I 5, O3q ^5 gqigs
"o.oLtG G9 5
,d:,0A zs_o s2 u5 5
lo: Dq 30, otlG
To,teUAvrltge b'1.5
111 oRC852.l oMsftmflflatt
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form iltttilliliifiif,rlttlr
oL6072L0
E 185 mm tr 240 mm
tr300mm tr 450mm
B UNSPIKED tr SPIKED AT:
Production Lot U-t 1DA Spike Date:
Carbon Lot 4C Spike Time:
QA/QC Signature 1sp*e1:
SAT'PLING INFORMATION
QA/QC Signature flropAc*rbry)i A./
tr High Flow O Fluffoprefitta
O Static Prefilter tr AGS
TypeofTrap: 308
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: h
PRE-Run LeakCheck tr PASS
Run Staft Date/Time:
Run End Date/Time:
tr FAIL
Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: tr Startup tr Shutd;;;
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
I
I
P0ST-RunLeakCheck trPASS tr FAIL
s_lMl! NG cO N-D-|_T! ONS AN D PARAMETERS
Avg. Duct Temp (F'):
Avg. Trap Temp (F'):
Avg. Flow Rate (cclmin):
TotalVolume (L):or (dscm)
REQUNEI) IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section I of Sorbent Trap (ng):
CHAIN OFCUSTODY
prevent moishre meas!rafEnt in $rbent lraps andspking Melhod cold vapor Adsorption via lmpinger sparging certiried Acc1mcy r lot, Traceable to Nlsr
Best Before: January 2026
trB
\1BtmeA6get{X}?fir&t
r Ua8'tSe 9tsf[ totl free
www.ohldfuftllfi$om
[e-mail]
lf appllcable place chain of
custody seal here-
(see security seal instnrction
sheet)
O 3o3so Bruce tndu$flftltffiatt? Cleveland, OH 44139 USA
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form mruffiffifiilifirrm
8 UNSPIKED
Production Lot
-U-1
1-28-
Carbon Lot 4C
QA/QC Signature &*o):
SAMPLING INFORMATION
tr SPIKED AT:
Spike Date:
Spike Time:
oL649725
QA/QC Signatu re (rrap Aoarmpty)i 4M(
tr High Flow tr Flufff Pre-filter E 185 mm tr 240 mm
tr Static Prefilter tr AGS tr 3(D mm El 450 mm
Type of Trap: -3,0I
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: tr A
SAMPLING CONDITIONS AND PARAMETERS
PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time: "
Run Number (optionat):
POST-Run Leak Check
T] PASS
tr PASS
I
I
tr FAIL
tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F'):
Avg. Flow Rate (cc/min):
TotalVolume (L):
Estimated Avg. Hg Concentration (U0/dsc1!
Event Occured During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OFCUSTODY
prerrent h the rap media. Md$ure coftlensathn ls a major caus€measuement in sooent traps drd $rorJld be D.e1€oted.
Best Before: June 2025
Spiking Nlethod Cold Vapor Adsorplbn Via rnpinOer SparghO C€rtified Accuracy r t 01. Traceabh b N|ST
113of166
www.ohiolumex.com
[e-mail]
OMostardi Platt
30350 Bruce lndustrial Pkwy.
Cleveland, OH 44139 USAI
lf aptcaHe place chain of
custody seal here.
(see security seal instruction
sheet)
\ I,Hfr{i$ft1ffY#;.
MERCURY SORBENT TRAP DATA SHEET
Projeci Name/Numben
Sampling Location:
Run Numbel:
Source Condition:
Preesure: 2{,
TestEngineer: SF[d(+DryGas*nt*o' ilapnumue,: oLroo
DrvGasiiirebrNo.nh? v= 0-QQJ rr+Nrro"r@spikcvabe 2B ng
Traln A:
Traln B:
Ds{21 }fGlbod n0PltEQcEm rrap
Main Kiln Stack
Sample TralnE
Clock Tlnr.
?.1lratt
llcbrVohm
ru-l llhr
IclarTamp.(t)
}F frterVrcuun,riad
lO: t2 6 (ob sl0:ll 5.06S bG 5l0:zz l0.0Ar2 blo s
10"> r l5.o.q8 G-l s
lo:12 zo.o5 0 b s
r0"31 zs_oq I b'Sio:rl?.a0.o 52
Tot UAvengo bb,5
Notes:
Pre-Test Leak Check-- pass @15_..Hg (llust be I i5,,Hg)Post-Test Leak Check - pass-@-Tg 'ni
Pre-Test Leak Check_- pass eEui ffiust be I tE,,Hg)Post-Test Leak Check - easc-@ T6-Hg '
114 {d0.Q.1 orvlffEfilfratt
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form ilffiulmnffilmlt
oL647L47
A UNSPIKED
Production Lot:
Carbon Lot 4C
tr SPIKED AT:
U-1128 Spike Date:
Spike Time:
eA/ec Signature nrapAsmny)i A# (
tr High Flow tr FluffY Prefilter
tr Static Pre-filter tr AGS
Type of Trap: 3-0_p . .
E 185mm tr 240mm
tr 300 mm El 450 mm
QA/QC Signature ppn.l:
SAMPLING INFORMATION
Facility / Source:
Boiler lD:
Sampling Location:
PRE-Run Leak Check
Run Start Date/Time:
Run End Date/Time:
Run Number (optionat):
POST-Run Leak Check
tr PASS tr FAIL
I
I _"
tr FAIL
Run Number (OPtional):
i
Sampling Train: €)
SAMPLING CONDITTONS AND PARAMETERS
OB tr PASS
Avg. Duct Temp (F ):
Avg. Trap Temp (F"):
Avg. Flow Rate (cc/min):
TotalVolume (L):or (dscm)
_ Estimated Avs. Hg c"i.:"ggps/dscm):
Event Occuned During Sampling: tr Staftup tr Shutdown
CEMENT ONLY:
#of RAW MILL OFF events during sampling:
REQUTRED rF REIUINlN9_T9_oltlo_l9Ig _ "
EstimatedHgMassinSection1ofSorbentTrap(ng):...,.;'-*
ilotsAns4zcror6,eir raF rilb.r.t06rGd- uxr *i.iJi,g u,'s ud*m.yrBut'l otofs6ratbnssin*r plcsaco*act rsifrqrltqi".$rirtte cstiml'v lh's |6t€'
CHATN OF CUST(DY
rEasuremefil taps
Best Before: June 2025
'r*.11t8[J'$Er..o,[e-mail]
30350 Bruce I n9UkFfl#Rta$'
Cleveland, OH 44139 USAI
tf adit$e Place chain of
custodY seal here.
(see security seal instruction
sheet)
Seal intact as received:
ves E ruo El
- Proiect No. M232512A\ . 1AilA0r3€G3F00 office-' 1888 B7o26t7 toll free
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
tr UNSPIKED
Production Lot 9_1F6_7
Carbon Lot 4C
QA/QC Signature 6p,r*1:
SAMPLING INFORMANON
A SHKED AT: 25ns_ _
spike Date: 6t23t2022
Spike Time: 0922
\1 ---
ililtiluiilffiffm!il
o1c155189
QA/QC Signature firap rsranprg:
0 High Flow u Fluffy Prefitter E 185 mm
tr Stath Pre-filter D AGS tr 300 mm
Type of Trap' 99.q_ _
tr 240 mm
O 450mm
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: tr A
SAMPLING CONDITIONS AND PARAMETERS
PRE-Run LeakCheck U PASS
Run Start Date/Time:
Run End Date/Time:
Run Number (opto."D:
POST-RunLeakCheck trPASS
"t
I
E FAIL
tr FAIL
Avg. Duct Temp (F ):
Avg. Trap Temp (F"):
Avg. Flow Rate (cclmin):
Totalvolume (L):or (dscm)
REQUIRE} IF REIURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OF CUSTODY
sampling cofilitiofis preve.t fixisture cmdensatam ln the rap meda. Mc,isture condensation is a measurernenl in sorb€nt traps
Spikino Method Cold Vapor Adsorptbfl Vh lmpinoer Sparging Certified Accuracy t 'l Ot. Tra]Ebte to N|ST
Estimated Avg. Hg Con_centration (pg/dscm):
Event Occrned During Sampling: tr Startup tr Strutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
,r**.otli6r${rffiP.com
[e-mail]
Best Before: June 2A25
30350 Bruce r nu &IhtlT*rfilBtt
Cleveland, OH 44139 USAI
lf applicable place chain of
custody selhere.
(see security seal instnrction
sheet)
Seal intact as received:
ves E HoEf
\ . re+re.r6t0.lgeg5lf,**' rNhlB6ho93oh tor free
MERCURY SORBENT TRAP FIELD DATA SHEET
Sampting Location: I.rl f Sied
Projed Name/Number
Date: 0 -rO-1 Run NunDer: 6
Pressure: 2{.q S
Dry Gas Meter No.
Sample Traln A
Clock Tlmc
2llhout
lllsterVolume
lV-l lftrn
Ueter Tcmp.
(h)
.F iietcrVacuum,
'lla
Sorbant Tttp.
Tcmp.l:St ckTemp.
.F
lo: rt R o G8 s z(0,t 20t
I O'.53 6.031 (og 5 21|*^6 ?-o (oloisSlo,or{?(^g ,?(ah 2o(,.ll:oq t5,oq5 bq 5 ?-(.(\zoltlio8,zo,os-l bq 5 zbo 2-o1
'. lr 26-1\rrt{b\9 ".60 ?-0-7
'.1 *30.()51
TdaUAverage (aa.q ZOtc,g
Notes:
Pre-Test Leak Check - Pass @ ,'Hg (Must be I l5"Hg)
Post-Test Leak Check - Pass
DryGasueerxo.!1ltt'l y=qqf7 rrapr,rumuer OLc t]S&3S spikevarue 25 ng
Sample Train B
Cloct Tlmc
2ll hour
Uet rvolumr
lV-l llhn
inlCf lamp.
(t-)
.F karYacurm,rfan
lo:q8 0 t.o8i 5
I a'^ (n g -0t{ (.68 s
Ir\'-(R lo.o|.lq 6*sll'.o3 l S.oLto bq s
I l'. o8 -LO,OLI 1o (oq 5
ll". r 3 2-5.03 t (,q (.
ll'.lg ?o,oH 2
TotallAvcnge (oq.t>
Train A:
Traln B:
Ds-021il6&Fhe#l*hft!hF0t rrap
Main Kiln Stack
Pre-Test Leak Gheck- Pass @ lJ "Hg (Must be l i6"Hg)
Post-Test Leak Check - Pass ql5 'Xg
1'17 oRH!62.1 oM?rbt6[fratt
il||tiluililil]fiiltil]t
A UNSPIKED
Production Lot _V:11 D9-*
Carbon Lot 4C
QA/QC Signature tsp*cl:
SAMPLING INFORMATION
tr SPIKED AT: .
Spike Date:
Spike Time:
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form 01607152
QA/QC Signature FrapA*sc'nbry)i -,CSo1.
tr High Flow tr Fluffy Pr*filter E 185 mm tr 240 mm
tr Static Pr*filter tr AGS tr 300 mm tr 4S0 mm
TypeofTrap: 308
Facility / Source:PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time:
tr PASS tr FAIL
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: (f,a trB
SAMPUNG CONDITIONS AND PARAMETERS
POST-Run LeakCheck tr PASS tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F"):
Estimated Avg. Hg Concentration (pg/dscm):
Event Occured During Sampling: tr Startup
CEMENT ONLY:
tr Shutdown
Avg. Flow Rate (cclmin):
Total Volume (L): _--_"_---- or (dscm)#of RAW MILL OFF events during sampling:
REQUIRED IFRETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
l./p,tq Wzs @&,alidr rilgE ri, 6. sl bascd fi lh6 Et c torvitg 0& e* ,ra, ,Esul h arada&rsrsl sarFir Pi.asa cs|tact ti6 irf FU Ggt r sssirlae ast nalirg lrrC r,'t,c
CHAIN OF CUSTODY
Ensue samplmg @ndlrcns pruvsrt moasture condensation in the trap media. Moisture condensatbn is a rnaior cause
Spikiog Mclhod Cold Vapor Adsoetion Ma lnpingEr Sparoing hified Acqxacy r t0ith Traeabh to NIST
measuremenl
Prdje0tffi4 eE€0ofre
il88&i768eill tollfree
www.dtbbrm.com
[e-mail]
30350 Bruce lndrtd*8|rou
Cleveland, OH 44139 USAI
lf applhable place chah of
custod seal here.
(see security seal instruction
sheet)
Seal intact as received:
ves E HoE
Sample(s) received by lab
Seal intact as received
ves E noE
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
D UNSPIKED
Production Lot S-4€F,A
Carbon Lot 4C _
QA/QC Signature (spirc):
SAMPLING INFORi'ATION
tr SPIKED AT: _?9""n9
Spike Date: *gg!osA-022* -
SpikeTime 1401
ililtilililrififfirulillil
o1c156360
QA/QC Signature Fr+esccrnpry): fJ
tr High Flow tr Fluffy prefilter
tr Static Prefilter tr AGS
TypeofTrap: 308
tr 185mm tr240nrn
tr 300 mm tl 450 mm
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: D A
SAMPLING CONDTTIONS AND PARAMETMS
PRE-Run LeakCheck fl PASS
Run Start Date/Time:
Run End Date/Time:
Run Number (optionat):
POSTflunLeakCheck trPASS
I
I
tr FAIL
tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F'):
Avg. Flow Rate (cclmin):
TotalVolume (L):or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
No,ie,r1€lyzqcdl&$tirrt {Erilrbes.t6as€da,ddeEht4iudistffimtyrsthanofs{bralrmanrhJrrPh6sccdflci.rrff}6ur,ccuiesssisirE Gtindiudri,}.f:
CHAIN OF GUSTODY
* Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
#of RAW MILL OFF events during sampling:
lf applicaHe place chain of
o.rstody sealhee.
(see seonity seel instrwtlm
sheet)
BestBefore:June 2025
9\1il{pAn62800zt'fgn
1t888 trI5g6eE tollfree
www.ohldflnfrtf,ftom
[e-mail]
30350 Bruce I n d Etf ffitfldhP/3tr
Cleveland, OH 44139 USA
Sampling Location:
Source Condition:
Dry Gas Mebr No,
Run Number
metricPrsssurc, 2{.ol9 -_ -totengtn*r F-
Trap Number OLC I82 (l0'I
Nobs:
Train A:
Traln B:
Pre-Test Leak Check-- pass @__lE_'Hg (Must be 2l5"Hg)Post-Test Leak Check - pass-@ Iil ,i;
Pre-Test Leak Gheck; pSss @-
-tf "x! 6lust be l ls,,Hg)Post-Test Leak Check - paos-@-T5 .,9; '
Ds.021 pr€r'odrirSl[,ilbtgmt rrae
Main Kiln Stack
DryGasttlebrNo.ldh? V=O-C|Q1 TnpN*ra.@Sp*eValrn rU
Samok Traln B
Gtock Tlm.
2llran hrrVolumo
lV-l lbr
ildcrTomp.
(bl
.F Iabrvecuum,rlla
I r'.RA o -to 5
I t'.u\5'.0 r{ 1 -?o Iil .,r{8 lo, oq o -1t\9
I I'. S'{.19.o3 I '1 r S
I t'st ?,,o5z -ll sDiO".2s.o35 -1 r q
l)-'- aQ ?o,b{?
TotaUAy.r.ge -10, I
120 oFw62.r @MSfimflatt
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
ililtiltililililililuilil
01607149
A UNSPIKED
Production Lot:
Carbon Lot: 4C
tr SPIKED AT:
U-l1D9 Spike Date;
QA/QC Signature rspr,el:
SAMPLING INFORMATION
Spike Time:
QA/QC Signatures.pe'emuy)r h& _
tr High Flow tr Fluffo prefilter E .tB5 mm tr 240 mm
tr Static Pr+filter tr AGS tr 3(x) nrn tr 4li0 mm
TypeofTrap: 308
Facility / Source:
Sampling Location:
Run Number (Optional):
PRE-Run LeakCheck tr PASS
Run Start Date/Time: __- _t
Run End Date/Time: -"__. .. _ l-__
POST-RunLeakCheck trPASS
tr FAIL
Boiler lD:
Sampling Train: G) tr BL-,,
SAMPLING CONDTTIONS AND PARAMETERS
tr FAIL
Avg, Duct Temp (F'):-.
Avg. Trap Temp (F"):
Estimated Avg. Hg Concentration fug/dscm):
Event Occuned During Sampling: tr Startup
CEMENT ONLY:
tr Shutdown
Avg. Flow Rate (cc/min):
Total Volume (L): ._-.---_ or (dscm)
REQUIRED IFRETURNING TO OHIO LUMEX
#of RAW MILL OFFevents during sampting:
Estimated Hg Mass in Section 't of Sorbent Trap (ng);
CHAIN OFCUSTODY
Ensure samptng condttions prevent rnoisture condensatrm
spikhg Merhod cord vapff Adsorprion via tmpinger sparling Certih& accuracy t r ot rraceabte ro lt rsr
measurernefit h sorbeflt traps be prg/cnted.
1n&26|flr@Effita
1ffi'8ft fiHgttoil free
www.oni&l8{Jf.to,
[e-mail]
30350 Bruce I nd rglyEltti8l,Pyl'n
Cleveland, OH 44139 USAI
lfapplcabh pbce chah of
oJst@sealhere.
(see security seal instruction
shee$
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form ilffiililffrfinmlttr
o1c175835
tr UNSPIKED
Production Lot S-4FF4
Carbon Lot 4C
QA/QC Signature rser.r:
E SPIKED AT: 2sl!s_
Spike Date: t/15/2OZz
SpikeTime: 1303
Y-
QA/Qc signatureo.pAssnpn: X[4r
tr High Flow tr Ftuffu prefitter El 1BS mm tr 2l() mmtr Stath Prefilter Cl AGS tr 300 mm D 4S0 mm
TypeofTrap: 308
SAMPLING INFORMATION
Facility / Source:
Boiler lD:
Sampling Location:
Run Number(0ptional):
Sampling Train: tr A
Avg. Duct Temp (F'):
Avg, Trap Temp(F'):
Avg. Flow Rate (cclmin):
TotalVolume (L):
PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time:
tr FAIL
*t "
.
t_
tr PASS
POST-RunLeakCheck trPASS tr FAIL
IAMllllglglgtnoNs AND PARAMETERS
Estimated Avg. Hg Concentration (;ig/dscm):
Event Occured Ouring Sampling: tr Startup
CEMENT ONLY:
d Srrutoown
or (dscm)
#of RAW MILL OFF events during sampling:
RFgy-l|Pll-lErg$ltrtg ro oHro LUrrrEx
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):l@e:A*lyt.,cdf'o,,,o'reF''/'rb'sclbtscdaurrwiaic,irg&ttrkrrarayJi-rJdi--"1""-a*r.o,r*r^rr..rre$/i!a$brrceasrinsr*Eo&
yrrrr.
CHAIN OF CUSTODY
i
lf +plixble ptace chain of
custqdy seal here.
(see security seal instruction
street)
Sample(s) prepared
for shipment by
Ensure sarnplino condifi ms Dfewnl mo
spiking Meihod cord vapor Adsorptbn via rmprngei spirlirs d;it &crra"y , r o{, iEiii'itfi ruisr
\1ndOe26{eflEBAfiI2A
1 8B'8f,b S&Et totl free
Best Before:July 2025
o 3o3so srr." rnarr@#3i'F[lfi]"nv Cleveland, OH 44139 USA
15 www.ohiUG8{eif.8o,
'*' [e-mail]
MERCURY SORBENT TRAP FIELD DATA SHEET
Project NameNumber
Sampling Location: t1K Saetk Run Number: A
Source Condition:
Dry Gas Meter No.
p*ssur€: 1ul .f <
TestErgineer: Snz6
TrapNumbff OLOO'I13O
Nobs:
Train A:
Train B:
Pre-Test Leak Check - Pass @ lb "Hg (Must be I {6"Hg}
Post-Test Leak Check - Pass @_jJ "Hg
Pre-Test Leak Check - Pass @ l9 "Hg (Must be 2 l5"Hg)
Post-Test Leak Check - Pass @_19_"Hg
D$02tl[regIl$fo9ffi gffi6arrao
Main Kiln Stack
Samole Traln A
Cbck fime
2a hout
illobrVolume
lV-l lltaa
reror ramp.
(t-)
.F lletarVacuum,
n{a
itorDant I ttpt
T.mp.
.9 Strck Temp.
.F
l2: lq b -7 ?_5 'Lb I 2 oca.
i2.-t 8 6.de I 'rB s 2,Gt 208
l?'.?.3 to , o?tl -?i s >G2 26R
l?',1.8 t5.o3l '1B s 26t 208
l2ig5 20.O3f,1q s LGt ?oa
12138 zs.oqLt -? l.l I zGl zaR
i2ir.l\3r).or{ I
TotaUAvorage l3 2-A I
DryGasMeterNo.@y=0.qq1 TrapNumber OL(oO'?li I Spikevatue_ng
Sample Train B
Clock Time
tebrVolume
lV-lllbn
Meler rtmp.
(t-l
.F mebrVrcuun,rtla
t).la o -'t ?5
t7'.Ig g.o5 t.'-li g
rLzl lo.o 5 0 -7'R S
tz:2R l5.oqD.'?B 5
tz:91 2.o.Obtl -l'i 5
l2'.in z5,osG -1 tt (,
lz:t|)30. oqq
TotaUAverage t.}
rzs offt6 2.1 outd{l#llF0tatt
Our Trao lD
iltIiltffiIiltlilililtililtilt
oLcL82607
UMEX Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
A UNSPIKED tr SPIKED AT:
Production Lot U-11DA Spike Date:
Carbon Lot 4C Spike Time:
QA/QC Signature 6pr4:
SAMPLING INFORMATION
QA/QC Si gnature frrap Asacmbry)i
tr High Flow tr Fluffy Prefiher
tr Static Pre-filter B AGS
TypeofTrap: 30B
E 185mm tr 24omm
tr 300 mm E 450 mm
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
PRE-Run Leak Check:
Run Start Date/Time:
Run End Date/Time:
tr PASS tr FAIL
POST.Run LeaKChecK O PASS tr FAIL
Estimated Avg. Hg Concentration (pg/dscm):
Event Occuned During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
I
I
,\
Sampling Train: qJ trB
SAMPLING CONDITIONS AND PARAT'ETERS
Avg. Duct Temp (F"):
Avg. Trap Temp (F'):
Avg. Flow Rate (cc/min):
TotalVolume (L):or (dscm)
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OF CUSTODY
Ensjre sampling conditions prerrent rnoisture condensatioo ln the trag measuremeot in sorbent traps and sfpuld be
Spikln0 Method Cold v@or Mso$tion yla lmpinoer Sparging Certified Accuracf t 10%, Traceable to NIST
Best Before: January 2026
*rr'r.oilfr1,f&/"98.o,
mail@ohiolumex.c0m
lf appficable place chain of
cust@ seal here.
(see security seal instruction
sheet)
Seal intact as received:
ves E NoE
Seal intact as received:
ves E NoE
\ rffiBff4H{ff#*""
(! 3o3so Bruce rndrglYhsl$f,\f{rttY Cleveland, OH 44139 USA
Trap lD
illllililril]ll]llIllllllll
oLcl2243sSorbent Trap Chain of CustodY Form
Ohio Lumex Co., lnc.
I Unspiked tr Spiked At:
Spiking Method Cold Vapor Adsorptlon vla lmpinger Spar8ln8
Crrtifled Aocufircy i 10t6, Traceable to NIST
Production 1s1; U-FD8 Carbon Lot: 4C
Spike Date:Spike Time:
AA/QC Sign atu re ffrap Assemb[]L
OA/aC Signature (spike)-
Type ofTrap:
trHlBh Flow Dcoil Pre'fllter E2{l mm
Estatic Pr*fiher DaGs 03(E mm
tr Fluffy Pre.fitter 8185 mm E45o mm
308
PlanVSource:
TO BE FIU.ED OUT BY SAMPUNG TECHNICIAN
PRE-Run Leak Check (circle one): PASS FAIL
Boiler lD:Run START:
Sampling Locatlon:
(stock, FGD tnlet, etc,)
Run Number(optional): Run END: .-........-.-."- -----';-
sampringTrain (circte one): A @ posr-Run Leak check (circle one): PAss FAIL
Notes:
SAMPUNG CONDTTIONS AND PARAMETERIi
Ave DuctTemp (F'):
Ave Trap Temp (F"):
Estimated Ave Hg Concentration (Ug/dscm):
Circle Event if Occurred During Sampling:
STARruP SHUTDOI^IN
Flow Rate (cclmin):r For CEMENT KII,NS ONIY
otalVotume (L) or(dscm):No. of RAW Ml l'l- OFF Events Duri ng Sa mpli ng:
REGTUIRED IF REruRNING TO OHIO LUMEX FOR ANALYSIS
Estimated Hg Mass in Section l of Sorbent Trap (ng):
NoteAnotyfrcottbrouonronOcwtttbel,el.bagidonthtswtue. Lavtngthlsbtonkmoyrgljuttlnout'oficoltbfotionanolyslt Pla*Gontoctutil"ou
Oraln Of
lf Appllcable Place Chain
of Custody seal here
(See SecuritY Seal
Seal intact as received
Seal intact as received
Seal intact as received
Seal intact as received
yes ff r.ro EJTrap analyzed by
@. prilari rnobtuna coatdatE fon ln ol. mp lmor, uollru]l qEnxrpr
rnd rhould br prwrntod rt rli co"tr D€actlveted d.3t lnd d.s.t wool lmPrc$a6d Acivrted Catbon - R'fet to SDS
Best Before: June 2024
#?ffl#"#ffiT#,4
1888 876 2611tollfree
***.otfr3?uot{rt99.o*
[e-mail]
30350 Bruce 116$ffiqfl1fi|att
Cleveland, OH 44139 USA?
&vcasrftbrxo'!1hl v=O,Q{J rnp*umber@sprtevahr ng
Sample Traln B
CbcInm.
2ahorr
lh{erVolumc
lV-l lkra
rDrTamp.
(t-)
)F t Ervftllm
't{a
t 2:86 0 -l{5le'. ss 5^OBL 1r{5l'i'-oo lo.bs f{'1 Y g
ta'.o E l5.b 5'l .?S sll'-t 6 2'0, oq-l 'rs 5ri'- t 6 z9.o(. I -?5 st?'.2-6 30,o51
TotalrAwrlgc 1'{.q
tlobs:
Traln A:
Train B:
D$02 1 pf8jBef, ffl .Sffi lgffi r rnc
Main Kiln Stack
rqi*ff:L"#:lJ;::"""=filf,[i'ust be r I E'Hs)
Pre-Test Leak check.- p:cs @E' Hg (Must be I l5,,Hg)Post-Teet Leak Check - pass-g TFr; '
126 oR6002.r @t\4fflaulflatt
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
illliluililililililIiltil
01607130
E UNSPIKED tr SPIKED AT:
Production Lor U-l1D9 Spike Date:
Carbon Lot 4C Spike Time:
QA/QC Signature epu,cl:
SAMPUNG INFORMATTON
QA/QC Signature Fraprssernbry): e" 4
[1 High Florv tr Fluffy prefilter B tBS mm
tr Static Pre-filter tr AGS O 300mm
TypeofTrap: 308
tr 240mm
tr 450 mm
Facility / Source:PRE-Run LeaKCheck tr PASS
Run Start Date/Time:
Run End Date/Time: *.-"_l
POST-Run LeakCheck tr PASS
tr FAIL
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: @
SATT,PLING CONDITIONS AND PARAIUETERS
trB tr FAIL
Avg. Duct Temp (F"):
Avg. Trap Temp (F): _tr Shutdown
Avg. Flow Rate (cc/min): ____*- ___
Total Volume (L): _-------- or (dscm)
# of RAW MILL OFF events during sampling:
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OFCUSTODY
crsuE Errrpug qonol[|ons pracftt moslurt @nden$tion in lhe trap medla. Moisture condensatirn is aspiking lvhhod cord v4or Msorptixr vra l,nplrocr sparging centinea tcuracy t tot, rraceaoCto utsr
Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: tr Startup
CEMENT ONLY:
www.ot{nlumscom
[e-mail]
30350 Bruce lnd@il{el4$ffFtt
Cleveland, OH /t4139 USA9
!f appllcabh place chain of
custod seal here.
(see security seal instruction
sheet)
yes E NoEI
ves E NoE
r hfn#tm;9mtffffi""
Oxt Trap lD
ilililililfi]il]ilt
01607191
UMEX Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form il
A UNSPIKED tr SPIKED AT:
Production Lot U-l1DA Spike Date:
Carbon Lot: 4C Spike Time:
QA/QC Signature eiul:
SAMPLING INFORMATION
QA/QCsignatureonpAsaenrbry)i /
tr High Flor tr Fluffy prefilter E 1BS mm tr 240 mmtr Static Pr+filter tr AGS tr 300 mm tr 450 mm
TypeofTrap: 308
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: tr A
Bnsure samptng condit,ons prsent rnoislure cilEensatioo in@
spiking Method cord vapo, Adso.ptior yra hpinoer sparging cenifiA Accura"y t r orr, iirc.ror"- to Nisi
PRE-Run LeakCheck: tr PASS
Run Start Date/Time:
Run End Date/Time:
D FAIL
t.
I
POST-RunLeakCheck trPASS tr FAIL
SAI,IPLING CONDTTTONS AND PARAilETERS
Avg. Duct Temp (F"):
Av!. rrap Temp (F"):
Avg. Flow Rate (cclmin):
TotalVolume (L):or (dscm)
REQUIRED tF RETURI{ING TO OHIO LUMEI(
Estimated Hg Mass in Section 't of Sorbent Trap (ng): __Nde:An*zet .dffibn ra"g.wifbeselbss€do m niniaiinrrrcur*qyrcoilr;"f*h.r-r;"4"" mr*oorr*r L,rp,lrrgui,reassrsra,ce*tir*hgrtir rdr
CHAIN OF CUSTODY
Estimated Avg. Hg Concentration (pg/dscm):
Event 0ccuned During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
oEaS[rretTEnt in sofbent traps and
I
Best Before: January 2026
@Mostardi Platt
30350 Bruce tndustrial pkwy.
Cleveland, OH 44139 USA
lf applicable placc chain of
custody seal here.
(see security seal instruction
shee0
Sample(s) received by lab
\ lffiffi$ffif#ifl.
128 of 16675 www.ohiolumex,comrj/ [e-mail]
MERCURY SORBENT TRAP FIELD DATA SHEET
Source Condition:
Pressura: z,{ 4(
TestEngln€en SF4CG .DryGasMeterNo. t4h? y= Oiqb
-
Topiu6".@
Semple Train A
Glock Tlne
2l horr
lletrrVdume
lV-l lltnn
ilet r T.mp.
(r.)
.F lletrrVrcuum,
"l{a
soilant Tr.pr
Tcmp.
.F Stack Tcmp.
.Elj:tr I o 16 5 z6b 2 orq
lSirr 5 5.051 '?q 5 260 208l3:50 to.or{'I 14 5 260 20813.56 r5.o3q 1s 5 2-6 0 zoR
l{',O()zo.o 52.-15 5 zLO zo8
tqioS 25, O q(-15 5 z6h zo3;
Itf it (3o,ot{'{
TotauAvgrag€.I5 2on
DrvGasMeterNo.t4lull v= o,dlQJ rraprurro"r oL60?2{J spikeValue ng
Sample Traln B
Clock Tlmc
)l lsrtt
I6t!r Volume
l1/-l liira
tsE?Tsmp.(t)
.F IetcrVrcuum,rlla
l3:\ b 0 -r5 5
l3'.q q 5.06'I -?5 5
i3'- so io.oqq th c)
Its:55 t5.066 'r5 5
irt.,oo
".o.
o5R -?s 5
lLt .'o 5 z(.o5R 'r<\l{'.1b 30.ar{R,
TotaUAverago -16
Notes:
Traln A:
Train B:
Pre-Test Leak ChEck- Pass @ l6 '.Hg (Must be I 15,,Hg)
Poet-Test Leak Check - Pass @JE ,'Hg
Pre-Test Leak ChEck- Pass @ lf, ,,Hg (Must be t iS"Hg)
Post-Test Leak Check- Pass fulla-],Hg
Ds-02 lPMfe*ftTt,'lg ggPt r',"'
Main Kiln Stack
rzs oFS62.l @Mdflfloeplatt
Ohio Lumex Co., tnc.
Hg Sorbent Trap Chain of Custody Form
Trao lD
illliltfltililililr
oL60724
A UNSPIKED tr SPIKED AT:
Production Lot U-11DA Spike Date:
Carbon LoI 4C Spike Time:
QA/QC Signature €pike):
SAMPLING INFORITIATION
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
samplinsrrain: GD
SAMPLING CONDITIONS AND PARAMETERS
Avg. Duct Temp (F'):
Avg. Trap Temp (F'):
Avg. Flow Rate (cc/min):
Total Volume (L):or (dscm)
trHighFlow trFluffypr+filter tr tgsmm tr240mm
tr Static Pre-fitter E AGS tr 300 mm tr 450 mm
TypeofTrap: 308
QA/QCSignaturefinpAssartry):
^/
PRE-Run LeakCheck tr PASS
Run Start Date/Time:
Run End Date/Time: _
I] FAIL
I
I
trB POST-Run LeakCheck tr PASS tr FAIL
Estimated Avg. Hg Concentration (pg/dscm):
Event Occurred During Sampling: u startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
REQUIRED IF RETURNING TO OHIO LUMEX
Estimated Hg Mass in Section 1 of Sorbent Trap (ng):
CHAIN OF CUSTODY
L,nsure sampling conditions pr€l,enl. moislure condensation ln
spiking Method cold vapo.Adsorption \4a lmpinger spa.qlng cenifir'd nccuracy r toji rraceable ro Nisi
,**.otit18,8{e1f.Bo,
[e-mail]
Best Before: January 2026
O 3o3so srr." rnorro#3?ttilli:"tv Cleveland, OH 44139 USA
measufanent in sorbent traps and sharU be
lf apdlcable place chain of
custody seal here.
(see sectrity sed instruction
sheeD
Sample(s) received by tab
\ . r EmztusdutrtffiSA-' 18trdrtsiffif tou free
A UNSPIKED
Production Lot U-l'lDA
Carbon Lot 4C
QA/QC Signature (sp&e):
SA[,lPLlNc INFORMATION
tr SPIKED
Spike Date:
Spike Time:
QA/QC Signature firsp l"snuy)i
tr High Flow tr Fluffy Prefilter
tr Static Prefilter tr AGS
TypeofTrap: 308
ililttttfrffiilfirrtln
o1507096
/::\
E 185mm tr240mm
tr300 nrn tl 450 mm
Ohio Lumex Co., lnc.
Hg Sorbent Trap Chain of Custody Form
Facility / Source:
Boiler lD:
Sampling Location:
Run Number (Optional):
Sampling Train: tr A
SATTIPLING CONDITIONS AND PARAMETERS
6
PRE-Run LeakCheck tr PASS
Run Start Date/Time: I
Run End Date/Time: _ - I
POST-RunLeakCheck trPASS
tr FAIL
tr FAIL
Avg. Duct Temp (F'):
Avg. Trap Temp (F'):
Avg. Flow Rate (cclmin):
TotalVolume (L):or (dscm)
REQUIRED IF RETURNIilG TO OHIO TUMEI(
Estimated Hg Mass in Section 1 of Sorbent Trap (ng): __
CHAIN OF CUSTODY
nrishre cmdensation i8a measurerneflt traps
Spikino
^retEd
Cold Vapo. Adsorpiion Vle tmpinger Spargino CenfEd Accuracy r I 01, Traccable to NtgI
Best Before: January 2A26
Estimated Avg. Hg Concentration (pg/dscm):
Event Occuned During Sampling: tr Startup tr Shutdown
CEMENT ONLY:
# of RAW MILL OFF events during sampling:
\***.onltlr?I199.o,
[e-mail]
30350 Bruce', o 8lf f.Tfil'ifl :t'
Cleveland, OH 44139 USAI
Sample(s) taken by lf apflixHe plaechain of
custody seal here.
(see security seal instnrction
sheet)
Sample(s) received by lab
tQr*rgqe!ffi?ftt&t
1Us8ff BlBf[ torrr'ee @
Appendix G - Galibration and Response Time Data
Project No. M2325124
Main Kiln Stack
132 ot 166 @Mostardi Platt
Cl.nt Ash ODve coment Cmpany
Frdlity: Leamington Comfft Pbnl
Prcr.d* M232512
TBt Ldbn: Main Kih Sb*
O*t 6nU2O23ombr R. solb6
op.6ung condltlon MIN On
S.mpb sfbm:
kob bngffi:
Prcbe Typ:
S.mpl. Pl.n.:
Pon Longlh:
Pd Slz. (dl.mcbr):
PonTr:
Dud Sh.p.:
Dbmataa:
Dudk.r
up.hm Olm.i.B:
OomframDlffih:
Numh.d Poi.8.m9l.d:
iumbr ot Pd6 p.r Pot
Idl NmhrdTd.E. Polnb:
FTIR
8.0
nlR
Hotonhl
3
3
Flangs
Ci@k
11
Polnt*
1
ln. 2
ln. 3
Pold t.ftln$ (lncludlne pod hngth):
lnchat
18.75
il21
a1 71
ft
9c. Ft95.03
4.1
I
3
3
Mlnimum UFEh Ol*ne
Mlnimum Dilmtream Dlsbnca
lded UFtroam Dlsbn6
ld.d tumsham Dblene
5.5 Fs€t
2-0 F*t
22 O Fo6l
S.0 F66t
Callbrallon Gase3
fr Sdlng Cyllndn D Cyllffir Vdu.frdqlndf%dhrgh Fhat Bo&
02
TF Sdlng Cyllnd.r E Cyllnd.r Valu.Pr.dhd V.ls Dil
fHC ppmw
{09
9S2 9I
tm%
30.1 1
Typ.CmFund qdhsr D Cyllnd.r V.tu.kplrilon D&
are Gaa f,tuog.n Zeo Nltw6n 0.0m >500
ESyhn.xc02s592B 1m.2 u112030
cc510322 11t1012023
M6Eda Plat
Project No. M2325124
Main Kiln Stack
v5.0
'133 of 166
MTA flIR IX22
@Mostardi Platt
Client: Ash Grove Cement Company
Facllity: Leamington Cement Plant
Proiect lt M232512
Concentration of Cal Gas C = Average value of test
,erage Pre and P6t Span Cqas = Corected gas value of t6t
Mostardi Platl
Project No. M2325'l2A
Main Kiln Stack
TGst Location: Main Kiln Stack
Dato: 6/20/23
oporator: R. sollars
02 % Corection: 7
Co=Average Pre and Post Zero
CalibEtlon Con€ct6d and Calculatod Oata
v50
134of166
RATA FTIR 1/1/22
OMostardi Platt
-o
4
6 19.95 19.98 19.94 {.01 {.01 -0.01 19.98 8 1.4 0.90 o.00 21 C
/19.95 -0.0'l 5 c o.33 I
6 19.95 20.04 20.08 0.04 o.08 0.08 20.08 I.24 1.3 0.57 o.00 -0.57 0.00
19.95 20.08 20.04 0.08 o.08 0.08 20.08 7.43 7.4 0.57 0.00 -0.57 0.00
10 19.95 20-08 20.o2 0.08 -0.01 0.04 20.05 6.99 7.0 o.77 t).20 -o.27 {.30
Run il Run
Date
Start
Time
End
Tlme NOx ppmw so2
ppmw co co2%
(drv)O2oh ldtyl lf,olsturc Y.THC ppmw HCI ppmw Flow, SCFtI
6t20t23 7:30 197.6 o.2 1021.O 7.7 0.4
8:07 8:36 204.3 0-3 1 185.8 10.1 o.2
6t20t23 8:43 12 209.7 o.2 1253.7 7.2 o.2
4 6t20123 9:35 1O:04 1S5.6 -0.3 1 484.8 7.5 0.4
6120t23 1O:12 10:4'1 192.4 .0.4 577.9 7.5 o.2
6 6not23 10:48 11..17 207 A 4.4 M1.1 7.4 0.0
6120t23 1 1:38 12'.O7 200.'l -0.6 455.6 03
E 6not23 12'.42 1 98.1 -0.5 465.1 7.3 0.1
6120t23 12:50 13:19 210.3 "0.5 518.6 7.4 0.0
10 6120t23 '13i40 14:09 193 I -06 538 4 70
Run *Run
Data
Start
Time
End
Time
Clinker
Production
Rate NOx lb/hr co rbrhr 02v"
(wet)
co20/.
(wet)
TtlC ppmvd
@7o/o02
HCI ppmvd @
7v6 02
r':1o
2 6DOt)3 807 8l l1a 4 g4 1'3
3 6DND3 Ra3 9.12 114 7 1)5
l{r 41 l lq
l lq .12
t.19
Client Ash Grove Cement Company
Facllity: Leamington Cement Plant
Test Location: Main Kiln Stack
Date= 6120123
Project #: M232512
Time
6:21
6:22
6:23
6:24
6:25
6:26
6:27
6:28
6:29
6:30
6:31
6:32
6:33
6:34
6:35
7:00
7:01
7:02
7:03
7:04
7:05
7:06
7:07
7:08
7:09
7:10
7:11
7:12
7:13
7:14
MostardiPlatt
Project No. M2325124
Main Kiln Stack
Linearity Gal/Pre I Cal
O2olo ldrvl THC ppmvw
30.32
30.11
22.38
1.66
-0.08
-0.09
8.79
21.11
20.98
20.25
19.13
3.58
9.41
9.89
10.11
22.20
22.10
9.60
0.00
19.20
1 1.10
11.10
11.10
0.00
0.00
0.00
11.20
1 1.30
1 1.30
11.30
ih
az
lm
v5.0
135 of 166
RATA FTIR 111122
OMostardi Plaft
Glient: Ash Grove Cement Company
Facility: Leamington Cement Plant
Project #: M232512
Test Location: Main Kiln Stack
Date: 612o123
Post l/Pre 2
02% ldwl
0.000.00 z
1.30
10.9011.00 m
20.60
20.60
20.70
20.70
Post 2/Pre 3
Time
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
Time
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
Time
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
THC ppmvw
8.44
-0.29
0.35
2.01
0.09
12.08
19.37
20.19
20.09
O2o/o (drvl
0.00
0.00
1.30
10.90
11.00
20.60
20.60
20.70
20.70
THG ppmvw
8.44
-0.29
0.35
2.01
0.09
12.08
19.37
20.19
20.09
Post 3/Pre 4
O2o/o (drvl
0.000.00 z
1.30
10.9011.00 m
20.60
20.60
20.70
20.70
Post 4/Pre 5
THC ppmvw
8.44
-0.29
0.35
2.01
0.09
12.08
19.37
20.19
20.09
02% (dwl
0.00
0.00
0.00
11.10
11.10
20.20
20.80
20.90
20.90
21.00
THG ppmvw
2.31z 0.39
-0.01
-0.01m -0.01
0.00
4.65
10.97
19.88
19.98
Time
11:25
11:26
11:27
11:28
11:29
11:30
11:31
11:32
11:33
11:34
Mostardi Platt
Project No. M232512A
Main Kiln Stack
v5.0
136 of 166
RATA FTIR 111122
@Mostardi Platt
Glient: Ash Grove Cement Company
Facility: Leamington Cement Plant
Project #: M232512
Test Location: Main Kiln Stack
Date:6120123
Post S/Pre 6
02%(dll THC ppmvw
0.00 2.31
0.00 z 0.39
0.00 -0.01
11.10 -0.01
1 1.10 m -0.01
20.20 0.00
20.80 4.6s
20.90 10.97
20.90 19.88
21.00 19.98
Post 6/Pre 7
Time
11:25
11:26
11:27
11:28
11:29
11:30
11:31
11:32
1 1:33
11:34
Tlme
13:27
13:28
13:29
13:30
13:31
13:32
13:33
13:34
13:35
13:36
Time
11:25
11:26
11:27
1'l:28
11:29
11:30
11:31
11:32
11:33
11:34
Time
13:27
13:28
13:29
13:30
13:31
13:32
13:33
13:34
13:35
13:36
02%@rvl
0.00
0.00
0.00
10.90
11.00
11.00
11.30
20.60
20.60
20.70
O2o/o (dryl
0.00
0.00
0.00
11.10
1'1.10
20.20
20.80
20.90
20.90
21.00
THC ppmvw
2.31
0.39
-0.01
-0.01
-0.01
0.00
4.65
10.97
19.88
19.98
Post 7/Pre 8
O2o/, (drvl
0.000.00 z
0.00
10.9011.00 m
1 1.00
11.30
20.60
20.60
20.70
Post 8/Pre 9
THC ppmvw
0.21
0.01
0.01
0.77
0.08
0.11
0.21
2.54
19.99
20.08
THC opmvw
0.21
0.01
0.01
0.77
0.08
0.11
0.21
2.54
19.99
20.08
MostardiPlatt
Project No. M2325124
Main Kiln Stack
v5.0
137 of 166
RATA FTIR 111122
@Mostardi Platt
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Project #: M232512
Test Location: Main Kiln Stack
Date:6120123
Time
13:27
13:28
13:29
13:30
13:31
13:32
13:33
13:34
13:35
13:36
Time
14:16
14:17
14:18
14:19
14:20
14:21
14:22
14:23
14:24
14:25
Post 9/Pre 10
O2o/o (dwl
0.000.00 z
0.00
10.9011.00 m
11.00
11.30
20.60
20.60
20.70
THC opmvw
0.21
0.01
0.01
0.77
0.08
0.11
0.21
2.54
19.99
20.08
Post 10
02 % (drvl
0.000.00 z
0.00
10.9011.00 m
11.10
20.50
20.50
20.40
20.40
THC ppmvw
0.31
0.05
-0.01
-o.02
-0.01
0.00
3.11
12.98
19.98
20.02
MostardiPlaft
Project No. M232512A
Main Kiln Stack
v5.0
138 of 166
RATA FTIR 111122
OMostardi Plaft
i
c.E!s6
tI
Y
(E
oo
o
(o(o
9oo)(")
c
3
6
T
ii!E
TBIgglt!! 5E
!
l-
3gE5
;6: Ed:ET :,!!i 5isis Io.i3i g-'i IEIi1
(\l
roN(.)v
N7i
=Eou)7Ct9Or0"6Ed>
Et
:
El36
E(L
E
(E
oo
@
(0
@
9oost
ao
n
s
3
iBBi
SSaE5il{
! IEi
a
n&
iE
59
r!ii
t:E!ot95
I
6
N
loN(o-c.t6>g
du)7C
6EOa
96Fd=
T
e
:
s(Eto-
E(E
oo
o
(o(o
go
$
-rl
I
,:lil
r:lrat
tt
.rl
EI
;$:t:lEI
_ltsH
-ll!l
&t
8il
u
5il
Irl
!
t
z
I
N
loN(r)-
N?i>5
oa7C
E9Oa
0"6Ed>
E*
=
?d
E
iE!E
El.I 5t'lEI 5E
i
sti3
3?
a Fi
:lti
!:E!6l *5
a
MOSTARDI PLATT
Procedures for Method 5 and Flow Calibration
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.
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.Ihe pitot tubes comply with the alignment speciflcations in Method 2, Section
10.1; and the pitot tube assemblies are in compliance with specifications in the same section.
CN&F-002 Cal Procedures M5 & flow Rev.2.2 1t1t2021
Project No. M2325124
Main Kiln Stack
142 of 166 @Mostardi Platt
Dry Gas Meter/Control Module Calibration Diagram
ATD-090 Dry Gas Meter Calibration
Project No. M2325124
Main Kiln Stack
Rev. 1.2 1t112021
143 of 166 @Mostardi Platt
(!
d
E
(E
oo
o
(o
@
o
$s
N
lr)
Nc/, vN7i
=E6@7C
6=Oa0'6d=
zo
F
e.
@
J
a
g.
u.tF
IJJ
=
d
Y
G
oo
o
(o(o
o
lr)$
N
lo
N(f)v
N7i>E
6u)7C
6=()a
0'6d>
3
ooqo
@o,
o?o
Noqo6
ooo)olr)
oo,qo()
o6qoo
oo
@c!
6
@
oNd
@
ooq
<fN
(o
N
co
o?*
NN:l
!
@F.\NN
q
F-N
C
C
oq
N
oq
N
G
c
G
o
r
g
E
ots
EgEEE}5f
Eo E
G
e
E6o
o
o
=
o(
G
so6
o
=o
t
E!dlE,!
FL
o
o
o
ti6l6,1
F!
E
((
o;
-oi=
o
=
9-5*
a=l
E
o
E
OE
E!!
OE
E
eo
o
OE
E.-6E
o
E
o
o-
ooF
o
=
a26E(,.o '
ooEo,ro o
o
o
=ooo
o
o>*E
EAe6
o
o2CE(,,o
o
E
i:
/
!ooo!
uJ
.E
E
o
o
!
oo
o
E3
oo
r)\
9(5
\
a
6l
co
E
c6)
aoo
Y
E
E
@
No
@oN
oL
o
Eo-
o
o
Eo
6l0
N
n
hooq
2
=
o
o6r
Go-I
zo
F-
d.
@
J
ot
lrJ
UJ
=
Stack Temperature Sensor Calibration
Temperature lD :526 Name:Rods
Ambient Temperature, '82.5 Date:May 25,2023
National lnstitute of Standards and Technology (NIST
ference Source Temoerature (o
Test Thermometer
Temperature (o F)Difference 96
0 0 0.0
250 250 0.0
600 600 0.0
1200 1204 0.2
(Ref. Temp.. "F + 460) - (.Test Therm. Temp.. "Ell60) * 100 <: 1.5 %
Ref. Temp., "F + 460
Project No. M2325124
Main Kiln Stack
146 of 166 @Mostardi Platt
S TYPE PITOT TUBE INSPECTION WORKSHEET
Pitot Tube No: 4036 Dale: 5/2412023 lnspectoB Nam€Rods
ryp€orProbe:(circtaon") f-;I-;T;;l ProbeLeneth: 8 ft.I-t-T--l
NOTEI
F.os q<rr <r.s DL "^ '""
il
ffi[
i
'11
1l
v-----------t)t,' I#tl lr0\ii I
\__1-_._l_
i
i
-'xMi9l$l ' * Z--...--
dJ__=Jp:::::_
cy'
Pitot lub€ assmbly level?
Pitot tub€ openings damaged?
X y6s _no
-Yes
(sxPlain b€bw)
6r=
br=
O "(<10") s.= g o(<10)
2 '(s5') br= 1 o (<so)
3 . 0= _L A= 0.94s (in.)
Xno
0.049 (in.): (s0.125 in.)
0.01649 (in.); (10.03125 in.)
0.473 (n.), PB = 0.473 (n')' D' = 0.375 (in.)
Rev. 1.0
147 ot 166
--I-no
z=Asiny=
w=Asin0=
CalibEtion required?
PIS-001 S Typ€ Pilot Tuh bsdid Fm
Project No. M232512A
Main Kiln Stack
a1712020
@Mostardi Platt
Appendix H - Calibration Gas Gylinder Data
Project No. M232512A
Main Kiln Stack
'148 of 1 66 @Mostardi Platl
CERTIFICATE OF AI\IALYSIS
Grade of Product:
E03N!78E15A0225
cc41il70
124 - Los Angetes (SAp) - CA
832022
CO2,02,BALN
AiIUAS.
an Alrllquiclo cmDely
Alrgac Specldty Gascs
Airgas USALLC
rtTu S, Alameda Strea
Loe Angeles, C,A9ooS9
Airyas.com
Part Number:
Cylinder Numben
Laboratory:
PGVP Number:
Gas Code:
Trlad Data Avaltable Upon Requ$t
EPA PROTOCOL STAhIDARI)
Reference Number: 4g-4O2ST4T1g_1CylinderVotume: iS2.0CF
Cyllnder Pressure: 20lS pSlG
Valve Ouflet:
Cedification Date:
590
M.28,2022
CARBON DIOXDE
OXYGEN
NITROGEN
11.00 %
11.00 %
Balanca
11.,t7 %
11.w%+l-0.7% NIST TraceaHe
CALIBRATION SI]ANDARILS
Concentrallon
NTRM
NTRM
13068t32
98051002
cc!.13737
SG915O866BAL
+/- 0.6%
+l-0.7%
NDIR
PARAMAGNETIC
M.17,2A2
@13,2022
149 of 166 ottrostap$falt,,
Aitgas.
anAhuqidccoqqny
AfryreSpcdrlryCeces
AirgasUSAHX
rrTu S. Alrncda Street
laAngde+CA9oo59
AlrS!..q
Part Number
Cylinder Numben
Laboratory:
PGVP Number:
Gas Code:
EPA PROTOCOL STAhIDARI)
Reference Number:,18-40?49596&l
CylinderVolunn: 162.0CF
Cylinder Pressurs: 201S pSlG
Valve Ouflet S90
CertmcatbnDate: JulZ5.,2tZ,
Dats:
Co'tflcen prtumrd h md.cr $h..SeU.q.+q.tyffiffiffiffi,g3o r_;""m"a.@{itr6rr*r""uorr,q/Hulrc.dak*ve.d&duer*riiruo,ceta,uac#.it"rl-e,!;-dirffir,iffi;i;il;ffij#ffi;;Hffi#HffiHffii,ffi"
molr/hdc br.b unl$r ofi!iltsr,pbd.
CERTIFICATE OF AhIALYSIS
Grade of Product:
E03N!56E15A1055
cc21763
124 - Los Angetes (SAp) - CA
8,32022
CO2,02,BALN
Rcqucctcd
Goncanffion
A}*A#rflC'ALRESI LT]S '- =.-"*
zL@*
22.@*
Babnco
+/-0.6%NISTTrffi
+/-0.3tt NlSTTrMle
LotlD Cyllnd.rilo Conc.ntrrton Unc.]t toty
NTRM
NTRII
12061540
1XfrMN
cc,3si{m
cf3,d]tffit
+r- 0.696
+l-02cfi
ANALYIIANL EQTIIPME}IT
SIEMENS 6E CO2
SIEMENS OXY}IAT6
Trlad D& Avr[aHc Upon R.$Et
150 of 166 @uostarfiHtfl of t
CERTIFICATE OF AI\ALYSIS
Grade of Product: EPA PROTOCOL STANDARD
MOSTARDI PLATT,
E02At99El 5 4'.1734
cc140776
124 - Pasadena (SG06) - TX
A32022
PPN,BALA
Airgas.
an Air Uquide company
Airgas Specialty Gases
Airgas USA LLC
98ro BAYAREABLVD
Pasadena, TX 75o7
Airgas.com
Customer:
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
163-402353480-1
146.2 CF
2015 PSIG
590
Feb 22,2022
Expiration Date: Feb 22,2030
Certmcation performed in accordance with 'EPA Traceabilily Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)' document EPA
6OO/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated balow 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 othenrvise noted.
Do Not Use This below 100 osio. i.e.0.7
Triad Data Available Upon Request
Sionature on file
Project No. trl&Prged for Release
Main Kiln Stack
ANALYTICAL RESULTS
Actua! Protoco!Concentration Method
PROPANE 1O.OO PPM 9.902 PPM
AIR Balance
G1 +l- 1.4o/o NIST Traceable 0212U2022
CALIBRATION STANDARDS
No Concentration
NTRM 17061006 ND61234 49.13 PPM PROPANE/AIR +l-0.40/o Jul 24,2023
AIYALYTICAL EQUIPMENT
Analytical Principle
C3H8-XL-N ICOLET iSsO AUP2O1O248 FTIR Feb20,2022
15'l of 166 @Mostardi PFSge I of 1
CERflFICATE OF AIVALYSIS
Grade of Product:
MOSTARDI PLATT,
EO2AI99E15AO1H9
cc733760
124 -Paeadena (SG06) - TX
13,2023
PPN,BAI-A
1ffigas.
an Alr Liquidc company
Custornen
Part Numbel:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Alrrlr speddtyGeccc
AirgasUSALI,C
98To BAYAREABLT/D
Pasadena, TXZSoz
Airlu.com
EPA PROTOCOL STAI{DARI)
Referene Numben 16U0267776*1
CyllnderVdume: 146.0CF
Cylinder Pmssure: 2015 PSIG
Valve Outet 590
CertificationData: Mar24,2023
Date:
Clmcetbn perbmreO ln mdanccwlh'EPATrmrbilty fficdforAgyud Cgdlcdon dcrour Cahrlton Stendadr 0iery2012)'do<ltmort EPA
6qlR-lzlxrt. u*E fio arqay pooodurlr lbbd. Analyd0d lu€&odology docE not ro$dr! aonlcfron b andidcal mcrb'lncc. Thh qllndcr har a bbl analytlcrl
unc..ffiy E ttdrd b.low wlur . conlucnc. lcvol d 9li%. Thoo er! no rtr{llcfl hrp.Jdhr llddr dt d th. u!. of ttdt calbraUon mlxurc. AI cono.rlr.llorE ar! o.r I
moHooabd.-rrltrr-0&lf'i&a lpbd-Il}3 rqq&l Ghta gdy h.Jh. lqm bqhd" IDo
t{ot t,!b Thh c!,{ndd bdox, l0o
Tdad DdArallable Upon Request
Project No. M2325124
Main Kiln Stack
AIYALYTICAL REST'LIS
Actual Pr6cdGoncentrrtlon tothod
PROPAI{E 2O.OO PPM I9.9{i PPM
AIR Balance
Gt +l-1.o% NlsTTraceable 03n4mn
CALIBRATION STAITDARDS
LotlD OrllnderNd Concenffion,
NTRII ,8068-12 61620701 29.99 PPM PROPN,IEAIR +14.1'lc Jtn 14,2025
ANALYMC.AL EQUIPMENT
c3lt8fi.t tcotET ts50 AUP20 r 0248 FTIR Mat?il,zoz3
Approved for Release 152 of 166 @Mostardi Pl$rgo t of t
Airgas.
an Air Liquide company
Airgas Specialty Gases
Airgas USA" LLC
rrTrr S. Alameda Street
los Angeles, CA 9oo59
Airgas.com
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
CERTIFICATE OF A]\IALYSIS
Grade of Product: EPA Protocol
E02Ar99E15A0705
E80086790
124 - Los Angeles (SAP) - CA
832021
PPN,BALA
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Mar 22.2029
48-402058889-1
146.2 CF
2015 PS|G
590
Mar 22,2021
Certification performed in accordance with 'EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)' document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confldence level of 95%. There are no signilicant impurities which affect the use of this calibration mixture. All concentrations are on a
Triad Data Available Upon Request
Sionature on file
Project Nord,PPtOfgSd for Release
Main Kiln Stack
mole/mole basis unless otherwise noted.
Do Not Use This
Component Requested
Concentration
ANALYTICAL RESULTS
Actual ProtocolConcentration Method
Total Relative
Uncertainty
Assay
Dates
PROPANE 3O.OO PPM 30.06 PPM G1 +l- 0.60/o NIST Traceable 0312212021
AIR Balance
CALIBRATION STANDARDS
Type Lot lD Cylinder No Concentration Uncertainty Expiration Date
NTRM '16061117 E80081910 50.06 PPM PROPANE/AIR +l-0.50/o Jul 26,2022
InstrumenUMake/Model
AIVALYTICAL EQI IIPMBNT
Analytical Principle Last Multipoint Calibration
MKS FTIR C3H8 01833582,1 FTIR Mar 09,2021
153 of 166 Pa$}10daa88m058889-1
lituas.
en Aruqlld! oofiiprry
Part Number:
Cylinder Number:
Laboratory:
Analysis Date:
Lot Number:
.tUrCrr Spedal$ carer
Airgas USAtrc
uru S. Alam€da S.treet
LosAqeles, C,rt9oo59
Arrta,com
CERTTFICATE OF AI\IALYSIS
GrAdC Of PrOdUCh CERIIEIED STAAIDARD-SPECx02Nt99crsAl268XCOeSS_gii-.,-*_ Refercnce Number: 4g{[)*fitzi3l1
ff:*;;weres(sAp)-cA .S,filriig:ffi, i*;'r$;''-$,ioiii;X,.l vrlve ouiler 3s0
Explnrton Date: Aug Ol, ZOSO
Produd compo$tbn rcr,fied Or r,rO
F______ Gas Mi:rrfire,€ftrence materhls.
Component Req Gone
ATYATM
Analytical
Uncertainty
Actual Concenhrfion
([oh t6)
ET}IYLENE 100.0 PPM
BahnceNIIROGEN 100.2 PPM +t-2%
OMostardi Platt
P.gplotl
Proiect No. 1 54 of 166
Main Kitn Stack Approved for Reteass
[i]ga$.
m AlrLhuldc cqnpany
efrgs Spedrttycacc,
AiryasUS&IIC
6Ur Eastoo Boad
Bldg2
Plumsteadvile PA18949
Airyas.com
CERTIFICAIE OF AI$ALYSE
Grade of Product: CERTIFIED STANDARD-SPEC
Part Number:
Cylinder Number:
Laboratory:
Analysis Date:
Lot Number
x03Nt99C15\4,0045
cc510322
124-Plumsteadvilh-PA
Nov 10,2021
Rebrence Numben
Cylinder Volume:
Cylinder Pressure:
Valve Ouflet:
16040,?272370.1
129.6 Cubic Feet
1800 PSIG
330
16040?272370-1
Expiraffon Date: Nov {0,2023
Product compositlon veriffed by direct omparison to calibraton standards traeaHe to N.I.S.T. weights and/or N.I.S.T.
C'as Mirfure reference materlals.
Component
AI{ALI.ITCAL RESIILTS
Req Conc ActualConcentration
(I{ole %)
Analytical
Uncertainty
SULFUR HDGFLUORIDE
HYDROGEN CHLORIDE
NITROGEN
5.0@PPM
50.00 PPM
Balance
5.000 PPM
47.92PPM
+r-5%
+l-2Yt
P.go I ot l60402ZI?it7O-1
@Mostardi PlattProject No.
Main Kiln Stack
for Release
155 of 166
*"*"--...-.
Appendix l- Mercury Analyses and QA Data
Project No. M232512A
Main Kiln Stack
156 of 166 @Mostardi Platt
Ash Grove Cement Company
Leamington Cement Plant
Main Kiln Stack
6/20/2023
Description Area Maximum Time
Std_100n9 HP 19000
Std_50n9 HP 9690
Std_25ng HP 5130
Std_250ng HP 48400
Std_10n9 HP 1990
Std_SOng RICCA ICV 9100
AGC Leamington Kiln Run 1a Section 1 2890
Run 1a Section 2 79
Run 1b Section 7 2870
Run 1b Section 2 160
Run 2a Section I 28tO
Run 2a Section 2 82
Run 2b Section 7 2700
Run 2b Section 2 48
Std_25ng CCV 4620
Run 3a Section 1 2800
Run 3a Section 2 l0
Run 3b Section 7 2620
Run 3b Section 2 ll0
Run 4a Section 1 3990
Run 4a Section 2 7L
Run 4b Section 1 8250
Run 4b Section 2 28
Std_25n9 HP 4690
Run 5a Section 1 5730
Run 5a Section 2 89
Run 5b Section 1 10600
Run 5b Section 2 tLB
Run 6a Section 1 6190
Run 6a Section 2 66
Run 6b Section 1 10300
Run 6b Section 2 IOL
Std_25n9 HP 4530
Run 7a Section L 5740
Run 7a Section 2 25
Run 7b Section 1 5930
Run 7b Section 2 87
Run 8a Section L 4730
Run 8a Section 2 12
Run 8b Section 1 4800
Run 8b Section 2 4
Std_25 ng HP 4580
Run 9a Section L 3720
Run 9a Section 2 36
Run 9b Section 1 3980
Run 9b Section 2 25
Blank -2
Run 10a Section 1 3850
Run 10a Section 2 87
Run 1Ob Section 1 4000
Run 10b Section 2 67
Std_25ng HP 4810
1800
78L
425
4770
160
715
253
3
99
t4
143
4
L28
3
449
246
1
247
5
335
2
584
19
328
68s
6
594
6
662
4
961
6
453
651
4
605
5
555
2
381
3
4t9
424
2
381
3
0
447
727
406
3
765
9:37:44 AM
9:40:13 AM
9:42:30 AM
9:44:43 AM
9:47:36 AM
10:15:38 AM
10:18:43 AM
10:20:49 AM
10:23:17 AM
10:25:25 AM
10:54:18 AM
10:55:12 AM
10:58:27 AM
11:00:22 AM
11:04:16 AM
11:51:42 AM
11:53:40 AM
11:58:14 AM
12:00:17 PM
!2:22:!8PM
t2:24:2LPM
12:28:50 PM
12:31:03 PM
L2:36:22PM
12:55:25 PM
12:58:32 PM
1:02:34 PM
1:04:32 PM
1:31:54 PM
1:33:49 PM
1:37:21 PM
1:39:13 PM
1:41;39 PM
2:22:35 PM
2:24:40PM
2:28:55 PM
2:30:52 PM
2:58:22PM
3:00:26 PM
3:06:01 PM
3:08:05 PM
3:10:51 PM
3:34:56 PM
3:35:53 PM
3:41:40 PM
3:43:36 PM
4:19:11 PM
4:21:38 PM
4:23:38 PM
4:27:32PM
4:30:01 PM
4:32:43 PM
Project No. M2325124
Main Kiln Stack
'157 of '166 @Mostardi Platt
Project#: M232512
Client: Ash Grove Cement Company
Facility: Leamington Cement Plant
Analyzer lD: 1423
METHOD 3OB CALIBRATION SUMMARY
Location:
Condition:
Data Taken By:
Main Kiln Stack
Mill On
SMcG
Calibration lD:CAL{1
Standard Mass
(ns)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (7o)
100 19000 98.33 'l.670/o
50 9690 50.15 0.30%
25 5130 26.55 6.20%
250 48400 250.47 0.19%
10 1990 10.30 3.00%
Slope 0.005175 0.00500
RSquared:0.999860
Enter Lowest Calibration Point
Standard Mass
(ns)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (%)
10 't990 9.95 0.5oo/o
lndependent Galibration Verifi cation
Standard Mass
(ns)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (ohl
50 9100 47.09 5.82o/o
Continuing Galibration Verifi cation
Standard Mass
(ns)
Ohio Lumex
Response
(Area)
Calculated
Mass (ng)
Percent
Error (ohl
25 4620 23.91 4.360/o
25 4690 24.27 2.92o/o
25 4530 23.44 6.24o/o
25 4580 23.7 5.20o/o
25 4810 24.89 0.44%
FT-008 Hg Template
Project No. M232512A
Main Kiln Stack
v5.0
158 of 166
't0t31t17
@Mostardi Platt
Project#: ?0232512
Cllent: Agh Grove Cement Company
Facility: Leamington Cement Plant
Analfzer lD: 1423
METHOD 3OB TEST RESULTS
v5.0
159 of 166
Location: Main Kiln Stack
Condltlon: Mill On
Data Taken By: SMcG
FT-008 Hg Template
Project No. M2325124
Main Kiln Stack
10131117
@Mostardi Platt
Cal Curve Run lD Trap lD Section
)hio Lumex
Response
(Area)
Hg Mass
(ns)Cal Curvo Run lD Trap lO Section
)hio Lumax
Response
(Area)
Hg Mass
(ns)
cAL-o1 1A o1607094 l-SamDlo 2890 15.0 cAL-01 7A oLCl 82607
1-Semble 5740 29.7
2-Breakthrouoh 79 0.4 2-Breakthrouoh 25 0.'l
cAL-o1 'lB oLc'182028 1-Samole zato 't4.9
cAL-01 7B oLc122435 l€amole 5930 30.7
2-Breaklhrouoh 't60 0.8 2-Breakthrcuoh a7 0.5
cAL-01 2A oLc181888 1-Samola 2810 14.5 CAL-01 8A o1607130 1-Samole 4730 24.5
rouoh a2 o.4 .Breakthrouoh 12 o.1
cAL-01 28 o1647104 l-Samole 2700 14.0 cAL-o1 8B 01607191
'l -Samole 4800 24.E
2-Breakthrouqh 48 o.2 2€reaKhrouqh 4 oo
cAL-o1 3A 01607210 l-Samole 2800 '14.5
cAL-o1 9A o1607249 I -SamDle 3720 19.3
Z-Breakthrouoh 10 01 2-Br6akthrouqh 36 o2
cAL-o1 3B o1649725 l-SamDle 2620 13.6 cAL-o1 9B o1607096 I -Samole 3980 20.6
Z-Breakthrouoh 110 0.6 Z-Breakthrouqh 25
cAL-01 4A oLM7147 t-Samole 3990 20.6 cAL-o1 10A 01647045 I -Samole 38s0 '19.9
2-Breakthrouoh 1 o.4 2-Breakthrouqh 87 0.5
cAL-o1 48 oLc't56189 l-Sample 4250 42.7 cAL-o'l 10B oL607247 l-Sample 4000 20.7
2-Breakthrouoh 2A 0.1 2-Breakthrouoh 67 0.3
cAL-o1 5A 01607152 1€amole 5730 297
2-Breallhrouoh 89 0.5
cAL-o1 5B o1c156360 1-Sample 10600 549
2-Breaklhrouoh 114 0.6
cAL-o1 6A 01607149 1-Samole 61 90 32.0
2-Breakthrouoh 66 0.3
cAL-01 6B o1c175835
'l €amolo 10300 s3.3
2-Breakthrouqh 'to'l 05
FT-008 Hg Template
Project No. M232512A
Main Kiln Stack
Method 30B Spike Recovery Summary
Leamington Cement Plant
Main Kiln Stack
v5.0
160 of 166
10t31t17
@Mostardi Platl
Test Run Date Start Time End Time
AGIUat
ConcGnlration. no
Expecleo uprxe
Concentration. no Recovew o/o
4A 6t20t2023 9:35 10:05 21.0 N/A 25.059 86.914842.8 25 25.147
5A 6120t2023 10:12 '10:42 30.2 N/A 25.022 101.03
5B 55.5 25 25.056
5A 6120t2023 10:48 '1't:18 32.3 N/A 24.935 8s.91
6B 53.8 25 24.953
Spike RecoveryAverage, % 91.28
Ohio Lum6x - Analytical Bias Test
Analtzer No. 1423
IUinimum Mass Sample Determination
Test Run Test Time Fraction
ACrUat
Concentration, nq
EIPesrsq aPric
Concentration, nq Recovery ol
,|8:38 Hq'10 10 't00.00
2 8:44 Hg"10 10 100.00
3 8:49 Ho'10 10 100.00
1 8:41 HgClz 10 10 100.00
2 8:47 HgCl2 10 10 100.00
3 8:5'1 HgCl2 10 10 100.00
0.000
0.000
o
LOD = 3-o
Maximum Mass Samole Determination
Test Run Test Time Fraction
Actual
Concentration. no
Expected Spike
Concentration. no Recovery o/o
1 9:32 H(1 960 2000 98.00
2 9'.41 Hr 1 930 2000 96.50
3 9:51 H(2010 2000 100.50
1 9:38 HgClz 1980 2000 99.00
2 9:47 HgCl2 1940 2000 97.00
3 9:55 HgCl2 1 950 2000 97.50
Prcject No. M2325124
Main Kiln Stack
161 of 156 OMostardi Platt
tphHH
7221 lnvestment Drive . North Charleston, SC 29418
[e-mail]
Product Description:
Product Number:
Lot Number:
Matrix:
Density:
Certilied Value:
BWWH
ACCiEDI'EO
_---I-
mgmE6
ISO '17034:2016 (RMP)
Accreditation
Certifi€te Number
AR-'1436
Ag7
Al <0.4
As na
Au <0.02
B<l
Ba <0.02
Be <0.02
Bi <0.02
Ca <l
cd <0.2
Ce <0.02
Co <0.05
Cr <0.05
Cs na
Shipped Date:
Expiration Date:
Certificate Issue Date:
Cu <0.02
Dy <0.02
Er <0.02
Eu <0.02
Fe <1
Ga <0.02
Gd <0.02
Ge <0.02
Hf <0.02
HgM
Ho <0.02
In <0.02
Ir <0.02
K<l
Element
Hg
ltg/mL
1000 + 6
<0.02
<0.02
<0.02
<0.5
<0.05
<0.02
<3
<0.02
<0.02
<0.02
<0.02
<5
<0.02
<0.02
SRM ID
3133
-1
<0.02
<0.02
<0.02
<0.02
<0.02
<0.02
<0. I
<5
<0.02
<0.5
<0.02
<0.02
<0.02
La
Li
Lu
Mg
Mn
Mo
Na
Nb
Nd
Ni
0s
Pb
Pd
Pr
Pt
Rb
Re
Rh
Ru
Sb
Sc
Se
si
Sm
Sn
Sr
Ta
Tb
Te <0.02
Th <0.02
Ti <0.02
Tl <0.02
Tm <0.02
u <0.05
v <0.05
w <0.02
Y <0.02
Yb <0.02
Zn <0.02
Zr <0.02
Packaging and Storage Conditions:
The standard is packaged in a pre-cleaned polyethylene bottle. To maintain the integrity ofthis product, the solution should be kept tightly
capped and stored under normal laboratory conditions.
Expiration Information:
The expiry date is guaranteed to be valid for eighteen months from the shipping date provided and is guaranteed through the month of
expiration. For this reason, standards from the same lot may have different exptation dates.
October 2022
April30,2024
J.uly 21,2022
m-t" Tf\ufufuww
Moven Mututuvari, Ph. D, VP Manufacturing
ReviriilUsQardi Ptatr
Page I of2
@efiittcste of flnil[yrir
Certified Reference
Material
Mercury
100033-l-100
22tE940-100
2% HNO3
1.012 gtnJ- + 0.002 elllaL @ 21.6oC t 0.3oC
The Certified value is based on gravimetric and volumetric preparation, and verified against NIST SRM 3100 series when available via
inductively coupled plasma optical emission spectrometry (ICP-OES) and/or inductively coupled plasma mass spectrometry (CP-MS) using an
internal laboratory-developed method. The uncertainty in the certified value is calculated for a95Yo confidence interval and coverage factor k is
about 2.
* Refer to Traceability lnformation, Section 4
Uncertified Values:
Trace Metal Impurity Scan: The data reported are based upon a scan of this specific lot via ICP-OES/ICP-MS analysis. The values are reported in pgll-.
L$l8HBh${b?11921&.l*
lf,milflmffinl[ilr
162 of 166
Preparation Information:
This Certified Reference Material is prepared using 99.99930/o pure Mercury Metal which was purchased from a
qualified vendor per ISO 9001 guidelines and assayed by analytical methods for conformity prior to use. This standard
was manufactured under appropriate laboratory conditions using the methods developed at NIST for SRM Spectrometric
Standard Solutions. Sub-boiling distilled high-purity acid has been used to place the materials in solution and stabilize
the standard. The matrix is as noted above in l8 megaohm deionized water. Stability of this product is based upon
rigorous short-term and long-term testing of the solution for the certified value. This testing includes, but is not limited
to, the effect of temperature and packaging on the product. If, during the period of validity, a recall is instituted due to
substantial changes in the stability of this product, the purchaser will be notified.
Ifomogeneity:
This product is determined to be homogeneous following in-house procedures developed in accordance with the
requirements of ISO 17034 and ISO Guide 35.
Intended Use:
This product is intended for use as a calibration standard, quality control standard, and/or for the validation of analytical
methods. The standard is confirmed homogeneous; therefore, the minimum sample size should be consistent with the end
user's measurement capabilities.
Traceability Information:
The traceability of this standard is maintained through an unbroken chain of comparisons to appropriate standards with
suitable procedure and measurement uncertainties. The maintenance of the base and derived units of lntemational
System of Units (SI) with traceability of measurement results (contemporary metrology) to SI ensures their
comparability over time as follows.
1. Standard Weight and Analytical Balance
The standard weights (NBS weights Inventory No 20231A) are calibrated every two years by South Carolina
Metrology Laboratory that is a participant in TIIST Weights and Measures Measurement Assurance Program'
with a certificate of measurement traceability to NIST primary standards. The balances are calibrated yearly by
the ISO 17025 acuedited metrology service, and are verified weekly by an in-house method using standard
weights.
2. Volumetric Device
The calibrations of volumetric vessels are verified using the ASTM method E542.
3. Thermometer
The standard thermometers are calibrated every year by the ISO 17025 accredited metrology service. The
thermometers used in-house are verified against the standard thermometers yearly.
4. CalibrationStandards
The Calibration Standard is traceable to SRM 3100 Series Spectrometric Standard Solutions. If an SRM is not
available, a second source standard or independent lot is used.
Refer to Safety Datasheet (SDS) for hazardous information.
NOTICE: HPS products ile intended for laboratory use only. All products should be handled md Ned by trained professional persomel. The responsibility for the safe hmdling
md use of these products rests solely with thc buyer md/or user. The data and infomation 6 stated was fumished by the manufactuer of the product. The infomation provided
in this certificate pertains only to the lot number specified. None ofthe infomation provided in this certificate may be used, reproduced or trmsmitted in my fom or by any
mems without uitten approval ftom High-Purity Stardtrds.
Rev{iiffibQardi Ptatt
Page 2 of 2
163 of 166
m
RrccA cHEMTcAL coMPANY'
-Certificate of Analysis
1490 Lammers Pike
Batesville, IN 47006
http :7***.riccachemical. com
1-888-GO-RICCA
customerservice@riccachemical. com
Mercury ICP Standard, 1000 ppm Hg in 8% HNO,
Int Numberz 42OgD27 h,oduct Nunber: PHGlKN Manufacture Date: SEP L4, 2022
&pirationDatd MAR 2024
The certified value for this product is confirmed in independent testing by a second qualilied chemist. The uncertainty associated with the certifiec
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 Beference Material 3133. All trace Ievel
elements were determined by ICP or ICP-MS.
Water
Nit"i" a.ia
Mercury
7732-18-5
7697-37-2
7439-97-6
Appearance
Assay (vs. Potassium Thiocyanate/Volhard's
cqlqrlqry liqqi.4 .
995-1005 ppm Hg
Beqqs4... "
1000 ppm Hg 999
Indicator)
Trace Elements by ICP or ICP'MS
All values reported in mgll, (ppm)
Iron (Fe)< 0.001 ppm
Lanthanum(Ld 0.0001ppm
I=Spectral Interference N=NotTested
Aluminum (Al)
Antimony (Sb)
Arsenic (As)
Barium (Ba)
Beryllium (Be)
Bismuth (Bi)
Boron (B)
Cadmium (CO
Calcium (Ca)
Cerium (Ce)
Cesium (Cs)
Chromium (Cr)
Cobalt (Co)
Copper (Cu)
Dysprosium Oy)
Erbium (Er)
Europium (Eu)
Gadolinium (Gd)
Gallium (Ga)
Germanium (Ge)
Gold (Au)
Hafnium (H0
Holmium (Ho)
Indium (In)
Iridium 0r)
< 0.0009 ppm
0.0666 ppm
0.0022 ppm
< 0.0001 ppm
0.0017 ppm
0.0082 ppm
I
0.0373 ppm
N
< 0.00003 ppn
0.0061ppm
< 0.00006 ppn
< 0.00002 ppn
< 0.00005 ppn
< 0.0001 ppm
N
0.0001ppm
< 0.0002 ppm
0.0022 ppm
0.0096 ppm
< 0.0005 ppm
0.0044 ppm
< 0.0001 ppm
< 0.00003 ppn
< 0.00007 ppn
Lead (Pb)
Lithium (Lil
< 0.00003 ppn
< 0.03 ppm
Silver (Ag)
Sodium (Na)
Strontium (Sr)
Sulfur (S)
Tantalum (Ta)
Tellurium (Te)
Terbium (Tb)
Thallium (Tl)
Thorium (Th)
Thulium (Tm)
Tin (Sn)
Titanium (Til
Tungsten (W)
Uranium (U)
Vanadium (V)
Ytterbium (Yb)
Yttrium (Y)
Zinc (Zn)
Zirconium (Zr)
0.1710 ppm
< 0.02 ppm
< 0.00006 ppn
I
0.0140 ppm
0.1464 ppm
N
0.0802 ppm
0.0035 ppm
0.0001ppm
0.0014 ppm
< 0.001 ppm
0.0541 ppm
0.0004 ppm
< 0.00004 ppn
< 0.001 ppm
< 0.00009 ppn
< 0.0003 ppm
0.0653 ppm
Lutetium (Ld < 0.0003 ppm
Magnesium (Mg) < 0.0007 ppm
Manganese (Md o.oo25 ppm
Molybdenum (Mo) 0.0203 ppm
Neodymium (N0 < 0.0002 ppm
Nickel (Nil < 0.0001 ppm
Niobium (Nb) 0.0011ppm
Osmium (Os) < 0.003 ppm
Palladium (PO 0.0503 ppm
Phosphorus (P) < 0.02 ppm
Platinum (Pt) 0.01?1 ppm
Potassium (K) N
Praseodymium (Pr) N
Bhenium (Re) < 0.00003 ppn
Rhodium (Rh) < 0.00003 ppn
Rubidium (Rb) < 0.00004 ppn
Ruthenium (Rd 0.0013 ppm
Samarium (Sm) < 0.002 ppm
Scandium (Sc) 0.0048 ppm
Selenium (Se) 0.0981 ppm
Silicon (Sil < 0.007 ppm
Version: 1.5 LtNumbo:4209D27 h,oductNumbc: PHG1KN
164 of 166
Page L of 2
@Mostardi PlaftProject No. M232512A
Main Kiln Stack
Mercury ICP Standard, 1 mL = 1 mB Hg (1,000 ppm Hg) Hg in 3%
HNOs
tni, "i".ra"tJ i" go"r"rri""a io be stable and
".".rrut"
p"o.riaed the o."a"" ir t"o, tightiv cappetl and sto.ed under normal laboratory conditions.
Balances are calibrated using MST traceable weights whose veri.fication of maintenance and recalibration is documented per in-house Standard
Operating Procedures. Class A glassware is aleo calibrated and routinely rechecked per in-house Standard Operating Procedures. Tlace metal
analyzed acids and Trace Metals Analyzed Water are used in the manufacture ofthis product. Triple cleaned containers are used in the manufacture of
this product.
EPA (200.7)
PHGfKN l9q
Recommmded Storage: 15oC ' 30oC
100 mL natural LDPE 18 months
(59"F - 86.F)
,QeA^"t'--
Paul Brando n @g t tU zozz)
Production Manager
This Certificate of Analysis is designed to comply with ISO Guide 31 "Reference
Materials -- Contents of Certificates and Labels."
This test report shall not be reproduced, except in full, without the written approval ofRicca Chemical Company.
IatNnnbc:42O9D27Version: 1.5
Project No. M2325124
Main Kiln Stack
hroductNunbe: PHG1KN
165 of 166
Page2 of 2
@Mostardi Platt
END OF THE REPORT
.. TAH DEPARTMENT OFENVIRONMENTAL QUALITY
Ai,r; ,ri :r.j
DIVIS,ON OF AIR QUALITY
Project No. M2325124
Main Kiln Stack
@Mostardi Platt