DAQ-2024-011245

1

DAQC-1088-24
Site ID 100547 (B4)

MEMORANDUM

TO: STACK TEST FILE – XCL ASSETCO, LLC – Against the Wind 2-2B-32

THROUGH: Rik Ombach, Minor Source Oil and Gas Compliance Section Manager

FROM: Paul Bushman, Environmental Scientist

DATE: October 23, 2024

SUBJECT: Source: One (1) Waukesha F18GSI engine
Contact: Lauren Brown: [phone]
Location: Duchesne County, UT
Test Contractor: Oasis Emission Consultants, Inc.
Permit/AO#: Permit by Rule
Action Code: TR
Subject: Review of stack test report dated August 26, 2024

On October 22, 2024, Utah Division of Air Quality (DAQ) received a test report for one (1) Waukesha
F18GSI engine at Against the Wind 2-2B-32, Duchesne County, Utah. Testing was performed August 21,
2024, to demonstrate compliance with the emission limits found in Utah Administrative Code R307-510
and 40 CFR Part 60, Subpart JJJJ. The calculated test results are:

Source Test Date Pollutant Method Tester Results DAQ Results Limits
Waukesha
F18GSI
SN: WPI-819
August 21,
2024
NOx 320 0.02 g/bhp-hr 0.019 g/bhp-hr 1.0 g/bhp-hr
CO 320 0.01 g/bhp-hr 0.011 g/bhp-hr 2.0 g/bhp-hr
VOC 320 0.04 g/bhp-hr 0.037 g/bhp-hr 0.7 g/bhp-hr

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The emissions from the Waukesha F18GSI engine should be
considered to have been in compliance with the emission limits
of UAC R307-510 and 40 CFR Part 60, Subpart JJJJ during
testing.

ATTACHMENTS: DAQ stack test review excel spreadsheets, XCL AssetCo, LLC
stack test report.
Emissions
XCL Resources
Against the Wind 2-2B-32
Duchesne County
Waukesha F18GSI; SN:WPI-819
Test Date: 8/21/2024
Run #1 2 3 Average
Start Time 8:05 9:07 10:08
Stop Time 9:05 10:07 11:08
Sample Duration (minutes)60 60 60
BHP Engine Load - Actual (bhp) 201 201 201 201
DS Stack Diameter (inches)8.5 8.5 8.5 8.5PAVG Average (Delta P)½ (" H2O)½0.4380 0.4370 0.4880 0.4543
CP Pitot Tube Constant (unitless)0.84 0.84 0.84 0.84
TS Stack Temperature (°F)1011 1012 1013 1012
Pbar Barometric Pressure (" Hg)24.90 24.90 24.90 24.90
Ps Stack Pressure ('' H2O)0.08 0.08 0.09 0.08
O2%vd O2 (%vd)0.0 0.0 0.0 0.0
CO2%vd CO2 (%vd)12.6 12.6 12.6 12.6
N2%vd N2 (%vd)87.4 87.4 87.4 87.4
dry NOX (ppmvd)5.2 4.0 4.0 4.4
dry CO (ppmvd) 6.2 3.0 3.2 4.1
wet NMEOC (ppmvw as C3H8)7.5 6.9 6.9 7.1
Run #1 2 3 Average
Bws Measured Moisture Content (%/100)0.190 0.194 0.193 0.192
Bws Saturated Moisture Content (%/100)1011.531 1015.156 1018.759 1015.148
Bws Actual Moisture Content (%/100)0.190 0.194 0.193 0.192
MD Molecular Weight Dry (lb/lb-mole)30.02 30.02 30.02 30.02
MA Molecular Weight Wet (lb/lb-mole)27.74 27.69 27.70 27.71
VS Gas Velocity (ft/sec)45.9 45.9 51.2 47.7
FACFM Gas Flow (acfm)1085 1084 1211 1127
FDSCFM Gas Flow (dscfm)262 261 291 272
FWSCFM Gas Flow (wscfm)324 324 361 336
FKWSCFH Gas Flow (kwscfh)19 19 22 20
FKWSCFM Gas Flow (kwscfm)0.324 0.324 0.361 0.336
lb/hr Gas Flow (lb/hr) 1400 1395 1558 1451
Fo Fo (unitless)1.659 1.659 1.659 1.659
wet O2 (%vw)0.0 0.0 0.0 0.0
wet CO2 (%vw)10.2 10.2 10.2 10.2
wet NOX (ppmvw)4.173 3.184 3.237 3.531
15 NOX (ppmvd @ 15% O2)1.454 1.115 1.132 1.234 82.0
lb/hr NOX (lb/hr)0.010 0.007 0.008 0.008
g/bhp-hr NOX (g/bhp-hr)0.022 0.017 0.019 0.019 1.0
wet CO (ppmvw) 5.048 2.435 2.559 3.347
15 CO (ppmvd @ 15% O2)1.759 0.853 0.895 1.169 270.0
lb/hr CO (lb/hr) 0.007 0.003 0.004 0.005
g/bhp-hr CO (g/bhp-hr) 0.016 0.008 0.009 0.011 2.0
dry NMEOC (ppmvd as C3H8)9.280 8.520 8.500 8.767
dry NMEOC (ppmvd as C3H8)9.280 8.520 8.500 8.767
15 NMEOC (ppmvd as C3H8 @ 15% O2)2.620 2.405 2.400 2.475 60.0
lb/hr NMEOC (lb/hr as C3H8)0.017 0.015 0.017 0.016
g/bhp-hr NMEOC (g/bhp-hr as C3H8)0.038 0.034 0.038 0.037 0.7
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1

Source Test Report
For
XCL Resources
Against the Wind #2-2B-32
Duchesne County, Utah

Test Date: August 21, 2024
Report Date: August 26, 2024

Federal Regulation: EPA 40 CFR 60, Subpart JJJJ
Engine: Waukesha F18GSI
SN: WPI-819
Unit ID: 810064 (100547)

Prepared By:

Oasis Emission Consultants, Inc.
2730 Commercial Way
Rock Springs, WY 82901

August 26, 2024

Mr. Ryan Sokolowski
XCL Resources

Dear Mr. Sokolowski:

Re: Engine Emission Testing For XCL Resources, Against the Wind #2-2B-32, Unit
810064 (100547), EPA 40 CFR 60, Subpart JJJJ.

An air emissions test program was conducted on a Waukesha F18GSI engine, operated by
XCL Resources and designated as Unit 810064 (100547), located at the Against the Wind #2-
2B-32 in Duchesne County, Utah. The purpose of the testing was to demonstrate compliance
with the emissions limits contained in EPA 40 CFR 60, Subpart JJJJ, for oxides of nitrogen
(NOx), carbon monoxide (CO) and volatile organic compounds (VOC).

Oasis Emission Consultants, Inc. conducted the testing on August 21, 2024.

EPA 40 CFR 60, Subpart JJJJ Emission Levels

The average recorded levels were found to comply with emission levels stipulated in the
permit, as shown in the attached report and summarized below.

Emission
Unit
Avg
NOx
Permit
NOx
Avg
CO
Permit
CO
Avg
NMNEHC*
Permit
VOC
g/bhp-hr 0.02 1.0 0.01 2.0 0.04 0.7
*VOC levels reported as non-methane, non-ethane hydrocarbon on a propane basis (NMNEHC C3).

Catalyst Parameters (Averaged Over 3 Test Runs)

Inlet Temp (deg F) DP (in H2O)
963 0.04

Engine Load (Averaged Over 3 Test Runs)

Rated BHP Operating BHP % Load
400 201.0 50.3

Testing Protocol

The attached report was generated using an extractive FTIR system using methodologies as
required by and in accordance with EPA 40 CFR 60(A) Methods 1-3 and EPA 40 CFR 63(A),
Method 320 as outlined in the submitted Source Test Protocol.

Quality Assurance

Oasis has performed a full review of the raw data and calculated results in this report. Any
errors we have encountered have been listed in the body of this report. After performing the
review, we are confident that this engine has met all requirements.

If you have any questions or require further information, please contact the undersigned at
[phone].

Yours truly,
Oasis Emission Consultants, Inc.

_________________________ _______________________
Charles A. Chapman Cember Crawley
Manager of Technical Services Environmental Scientist

_________________________

Christopher N. Knott, P.Eng.
Director, Engineering and Operations

SOURCE EMISSION TEST REPORT

FEDERAL REGULATION EPA 40 CFR 60, Subpart JJJJ

Test Performed By: Oasis Emission Consultants, Inc.

Test Company Contact: Chris Knott
2730 Commercial Way
Rock Springs, WY 82901
307.382.3297

Owner/Operator: XCL Resources

Owner/Operator Contact: Ryan Sokolowski

Facility Name: Against the Wind #2-2B-32
Duchesne County, Utah

Emission Source: Waukesha F18GSI
Unit 810064 (100547)

Date of Test: August 21, 2024

Date of Report: August 26, 2024

TABLE OF CONTENTS

1.1 Introduction .......................................................................................................................... 1
2.1 Stack Sampling Location ..................................................................................................... 2
3.1 Discussion of NOx, CO and VOC Test Results ................................................................... 4
3.1.1 Source Test 1 ............................................................................................................................................ 4
3.1.2 Source Test 2 ............................................................................................................................................ 4
3.1.3 Source Test 3 ............................................................................................................................................ 4
4.1 Stack Sampling Methods and Procedures ............................................................................ 5
4.2 Equipment Utilization .......................................................................................................... 6
4.3 Measurement of VOC (NMNEHC C3) ............................................................................... 7
4.4 Process Parameters ............................................................................................................... 7
5.1 Quality Assurance ................................................................................................................ 8

List of Tables and Figures

Figure 1 - Sample Port Location ............................................................................................................................. 2
Figure 2 - Sampling Train Schematic-Method 320 ................................................................................................. 6

Table 1 - Insertion Depths of Traverse Points for Stratification Test ..................................................................... 3
Table 2 - Location of Traverse Points in Circular Stacks ....................................................................................... 3
Table 3 - Test Matrix .............................................................................................................................................. 5
Table 4 - Concentrations and Interference .............................................................................................................. 6

APPENDIX A: NOx, CO and VOC Test Data

APPENDIX B: Quality Assurance/Calibration Data

APPENDIX C: Load Approximation

APPENDIX D: Example Calculations and Summary

APPENDIX E: Field Notes

1

1.1 Introduction

An air emissions test program was conducted on a Waukesha F18GSI engine, operated by
XCL Resources and designated as Unit 810064 (100547), located at the Against the Wind #2-
2B-32 in Duchesne County, Utah. The purpose of the testing was to demonstrate compliance
with the emissions limits contained in EPA 40 CFR 60, Subpart JJJJ, for oxides of nitrogen
(NOx), carbon monoxide (CO) and volatile organic compounds (VOC) defined as non-
methane, non-ethane hydrocarbons, reported as propane (NMNEHC C3).

The facility is currently located in Duchesne County, Utah.

Three one hour test runs were performed on August 21, 2024 to analyze NOx, CO and VOC
emission levels. Test runs were performed according to methodologies outlined by EPA 40
CFR 60(A) Methods 1-3 and EPA 40 CFR 63(A), Method 320 as outlined in the submitted
Source Test Protocol. Each one hour test run consisted of 60 readings taken at one minute
intervals.

Process parameters were recorded during each test run in order to determine the load.
Parameters include the engine RPM, intake manifold temperature and pressure, and the site
elevation.

The following key personnel were present during testing:

David Martinez, OEC
Bowdy

2

2.1 Stack Sampling Location

The facility is currently located in Duchesne County, Utah.

Testing was conducted on the Waukesha F18GSI engine. The sampling port for moisture,
NOx, CO and VOC measurements was approximately 2.8 pipe diameters (24”) downstream
from the nearest flow disturbance (Distance B) and 1.4 pipe diameters (11.5”) upstream from
the nearest disturbance (Distance A), as seen in Figure 1. The stack sampling location was
placed at approximately 50% insertion depth based on an O2 stratification check which
demonstrated a non-stratified flow regime. The stratification was conducted according to
EPA 40 CFR 75(A), §6.5.6.1 using 3 traverse points determined according to Table 1 below.
In accordance with EPA 40 CFR 60(A), Method 1, a total of 16 traverse insertion depths (8
traverse points through each of the 2 ports) were determined according to Table 2 below in
order to conduct Method 2.

Figure 1 - Sample Port Location

8.5"
A
B

Oxidation
Catalyst
3

Table 1 - Insertion Depths of Traverse Points for Stratification Test

Traverse Point Insertion Depth (Percent of Stack Diameter)
1 16.6
2 50.0
3 83.3

Table 2 - Location of Traverse Points in Circular Stacks

4

3.1 Discussion of NOx, CO and VOC Test Results

Three, one hour test runs were performed on August 21, 2024 to analyze exhaust NOx, CO
and VOC (NMNEHC C3) emission levels to demonstrate compliance with the emissions
limits contained in EPA 40 CFR 60, Subpart JJJJ. Testing for NOx, CO and VOC were run
concurrently with one another. Each test was performed at the maximum achievable load.
Measured emissions were below permitted limits. Please refer to the Appendices for a listing
of all raw data, calibration error response and calculations performed per EPA 40 CFR 60(A)
requirements.

3.1.1 Source Test 1: Waukesha F18GSI, NOx, CO and VOC

The first test was performed from 8:05 to 9:05 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
201.0 bhp, and the average NOx and CO levels were found to be 0.02 g/bhp-hr and
0.02 g/bhp-hr respectively, below limitations. The VOC level tested at 0.04 g/bhp-
hr, which tested in compliance.

3.1.2 Source Test 2: Waukesha F18GSI, NOx, CO and VOC

The second test was performed from 9:07 to 10:06 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
201.0 bhp, and the average NOx and CO levels were found to be 0.02 g/bhp-hr and
0.01 g/bhp-hr respectively, below limitations. The VOC level tested at 0.03 g/bhp-
hr, which tested in compliance.

3.1.3 Source Test 3: Waukesha F18GSI, NOx, CO and VOC

The third test was performed from 10:08 to 11:07 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
201.0 bhp, and the average NOx and CO levels were found to be 0.02 g/bhp-hr and
0.01 g/bhp-hr respectively, below limitations. The VOC level tested at 0.04 g/bhp-
hr, which tested in compliance.

Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
1 5.15 0.02 6.23 0.02 9.28 0.04 0.0
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
2 3.95 0.02 3.02 0.01 8.52 0.03 0.0
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
3 4.01 0.02 3.17 0.01 8.50 0.04 0.0
5

4.1 Stack Sampling Methods and Procedures

Testing followed EPA 40 CFR 60(A) Methods 1-3 and EPA 40 CFR 63(A), Method 320,
with no exceptions.

Table 3 - Test Matrix

Method Title Parameter Reference
EPA 40 CFR 60
Appendix A, Method
1
Sample and Velocity
Traverses for
Stationary Sources
Sampling Point
Determination
https://www.epa.gov/
sites/production/files/
2017-
08/documents/metho
d_1_3.pdf
EPA 40 CFR 60
Appendix A, Method
2
Determination of
Stack Gas Velocity
and Volumetric
Flow Rate
Exhaust Effluent
Flow
https://www.epa.gov/
sites/production/files/
2017-
08/documents/metho
d_2.pdf
EPA 40 CFR 60
Appendix A, Method
3
Gas Analysis for
the Determination
of Dry Molecular
Weight
O2, CO2, Dry
Volumetric Flow
Rate
https://www.epa.gov/
sites/production/files/
2017-
08/documents/metho
d_3.pdf
EPA 40 CFR 63
Appendix A, EPA
Method 320
Vapor Phase Organic
and Inorganic
Emissions by
Extractive FTIR
Nitrogen Oxides,
Carbon
Monoxide, Non-
Methane Non-
Ethane
Hydrocarbons on
a Propane Basis
https://www.epa.gov/
emc/method-320-
vapor-phase-organic-
and-inorganic-
emissions-extractive-
ftir
United States. U.S. Environmental Protection Agency. “EMC Promulgated Test Methods.” Air
Emission Measurement Center (EMC). 31 August 2023. Web. 26 August 2024.
<https://www.epa.gov/emc/emc-promulgated-test-methods>.

6

4.2 Equipment Utilization

The following equipment was used during the tests performed at this facility in conjunction
with procedures outlined by EPA 40 CFR 60(A) Methods 1-3 and EPA 40 CFR 63(A),
Method 320.

• (1) MKS MultiGas 2030 FTIR Continuous Gas Analyzer (0.210 L/min sample flow, 0.014
atmosphere sample pressure, 1 atmosphere cell pressure, 191°C cell temperature)
• (1) Laptop Computer for the FTIR Analyzer using MKS MG2000 Software
• (1) 75ft or 100ft Heated Teflon Line w/ Heated Sample Probe and Spike Bypass Line
• S-Type Pitot Tube c/w 20 ft. Heated Sample Line (coefficient 0.84)
• (1) Fyrite O2/CO2 Analyzer
• (5) EPA Protocol G1 Calibration Gas (NOx, CO, C3H8, C2H4 and NO2)

The MKS Multigas 2030 FTIR Analyzer operated with a spectral resolution of 0.5 cm-1 and a
scan time of 30 seconds. The FTIR spectrometer utilizes a multi-pass gas cell with a 5.11
meter effective pathlength.

Figure 2 - Sampling Train Schematic-Method 320

Table 4 - Concentrations and Interference

7

The MKS 2030 software provides a Natural Gas Method that is designed to minimize all
expected interferences by removing the regions in the quant region where they are most
absorbed (i.e. picket fence approach). So, for example, all the water peaks that are greater
than about 0.1 abs are removed from the quant region. Since the spectral noise measured
(sample spectrum) is in the range of 0.001 absorbance, it is desirable to have any error within
this range. The MKS software will match the water calibration spectrum to the sample
spectrum at any 1 point in the spectrum to about 1% precision. So, 1% of 0.1 absorbance is
0.001 abs. This is why any peaks greater than this for interfering compounds are usually
excluded so they do not interfere. To summarize, the MKS software and the method are
designed to minimize any interferences by removing their largest interfering absorptions.

4.3 Measurement of VOC (NMNEHC C3)

The algorithm currently used for NMNEHC C3 and developed for natural gas fired
applications by Dr. Spartz and MKS instruments in accordance with EPA standards, is the
following:

(2.4*c8/(1+exp((2-c8)/0.2))+1.9*c11/(1+exp((2-c11)/0.2))+6*c12/(1+exp((0.5-c12)
/0.2))+2.85*c13/(1+exp((2-c13)/0.2))+3*c14/(1+exp((1-c14)/0.2)))/3

c8= acetylene
c11= ethylene
c12= hexane
c13= propylene
c14= propane

Note: The constants in front of each of the compounds listed represents the FID response
factor when calibrated with Propane.

As with any CEMS analyzer, the FTIR may demonstrate a negative zero bias. The “exp”
functions listed in the algorithm above are intended to mathematically filter out any negative
biases and set them to approach zero.

4.4 Process Parameters

Process parameters were recorded during each test run in order to determine the load.
Parameters include the engine RPM, intake manifold temperature and pressure, and the site
elevation. Results are provided in Appendix C.

8

5.1 Quality Assurance

The MKS Multigas 2030 FTIR Analyzer was used to measure NOx, CO and VOC on a dry
basis. A pre Direct and System calibration measurement was made on compounds of NOx,
CO, C3H8 and C2H4. In addition, post System calibrations were made on compounds of NOx,
CO, C3H8 and C2H4. Compounds of CO2 and C3H8 were measured for the quality assurance
spiking requirements. Levels for calibrations and zeroes must be within +/- 5% of the
certified calibration gas or response to zero gas, respectively.

CTS procedures were followed according to EPA requirements for both pre and post testing.
Similarly, QA spiking procedures were followed. Analysis of the CO2 exhaust effluent was
used to determine the dilution factor. Steady levels of the CO2 were observed and a sufficient
duration of time was allowed to elapse for a representative average.

The calibration gas was spiked into the effluent stream using a bypass line at approximately
10% of the sampling rate. The dilution factor was obtained from observation of the stack CO2
behavior using the following equation:

CO2AVG – CO2SPIKE
DF = ------------------------
CO2 AVG

Where: CO2AVG = The average undiluted CO2 stack gas concentration of spike measurements
CO2SPIKE = The average diluted CO2 stack gas concentration when spiked

The sample recovery was then obtained from the following equation:

% REC = (Spike MEAS – Stack MEAS)* (1 – DF)
---------------------------------------------------------
CS * DF

Where: Spike MEAS = The average diluted stack gas concentration when spiked
Stack MEAS = The average undiluted stack gas concentration
DF = Dilution factor
CS = Certified concentration of calibration standards

The Sample Recovery average level for C3H8 was found to be 74.6%, which was within the
allowable tolerance of Method 320 (70% to 130%). A summary of all spiking
procedures/results can be found in Appendix B.

APPENDIX A

NO Dry
(ppm)
NO2 Dry
(ppm)
NOx Dry
(ppm)
CO Dry
(ppm)
NMNEHC C3 Dry
(ppm)
H2O% (High)
191C
Time
1 3.525775 0.715531 4.241306 6.411384 6.892641 14.086376 8:05:58 08/21/2024
2 3.594727 0.871658 4.466385 12.71556 10.071176 16.785564 8:06:58 08/21/2024
3 4.573251 0.994267 5.567518 6.07933 9.316185 17.58429 8:07:59 08/21/2024
4 4.164628 1.052862 5.21749 6.904348 10.243132 18.662367 8:08:59 08/21/2024
5 2.578834 1.288324 3.867158 4.498568 7.973937 18.838637 8:09:59 08/21/2024
6 7.260761 1.209776 8.470537 10.484949 7.748986 18.555572 8:10:59 08/21/2024
7 2.062303 1.308298 3.370601 4.569294 7.810711 22.907825 8:11:59 08/21/2024
8 5.523824 1.341079 6.864903 11.37056 10.810306 19.350773 8:12:59 08/21/2024
9 4.429941 1.179714 5.609655 9.433413 10.225954 18.319356 8:14:00 08/21/2024
10 8.642695 1.302082 9.944777 11.567826 9.367898 19.434635 8:15:00 08/21/2024
11 7.231876 1.157319 8.389195 14.577082 11.910693 18.644724 8:16:00 08/21/2024
12 2.4543 0.860845 3.315145 5.132962 9.049403 16.574002 8:17:00 08/21/2024
13 4.302725 0.97027 5.272995 5.468932 8.236609 17.386284 8:18:00 08/21/2024
14 1.486718 1.4311 2.917818 2.552664 6.604133 19.627815 8:19:00 08/21/2024
15 3.205472 1.212444 4.417916 5.982816 10.069503 18.749574 8:20:00 08/21/2024
16 10.913537 1.098968 12.012505 14.65372 12.355452 20.79837 8:21:01 08/21/2024
17 3.263664 1.157797 4.421461 6.668975 10.059935 18.048234 8:22:01 08/21/2024
18 3.1593 1.458917 4.618217 2.939806 7.736043 20.09516 8:23:01 08/21/2024
19 2.579451 0.939435 3.518886 5.308014 8.680766 17.275318 8:24:01 08/21/2024
20 2.304358 0.865577 3.169935 4.523998 8.877632 18.019278 8:25:01 08/21/2024
21 1.718992 1.213459 2.932451 10.07206 6.144645 18.565559 8:26:01 08/21/2024
22 4.491119 1.182247 5.673366 7.736109 10.254458 18.830204 8:27:02 08/21/2024
23 3.719186 1.153928 4.873114 11.74614 12.195878 18.238838 8:28:02 08/21/2024
24 12.009845 1.3776 13.387445 8.189193 10.739504 20.949708 8:29:02 08/21/2024
25 1.711803 1.296467 3.00827 3.8522 9.298183 18.784577 8:30:02 08/21/2024
26 2.420867 1.359945 3.780812 2.915037 8.407365 19.96165 8:31:02 08/21/2024
27 4.508515 1.533751 6.042266 6.016366 10.921515 20.963633 8:32:02 08/21/2024
28 1.521049 1.26623 2.787279 1.376698 5.211919 19.205349 8:33:02 08/21/2024
29 2.633887 1.192221 3.826108 8.608765 10.567271 18.179824 8:34:03 08/21/2024
30 4.898752 1.16994 6.068692 9.566532 8.650626 18.514552 8:35:03 08/21/2024
31 2.590571 1.198999 3.78957 4.039062 9.198856 18.83946 8:36:03 08/21/2024
32 1.937957 1.259806 3.197763 3.911384 9.210098 18.658356 8:37:03 08/21/2024
33 3.426902 0.959278 4.38618 10.75647 11.832330 20.471771 8:38:03 08/21/2024
34 6.417637 1.472582 7.890219 6.454807 8.808754 22.07298 8:39:03 08/21/2024
35 3.589152 1.42986 5.019012 5.050744 9.547205 20.698659 8:40:04 08/21/2024
36 5.667691 1.175782 6.843473 8.654905 12.077881 17.675245 8:41:04 08/21/2024
37 6.589615 1.187396 7.777011 9.058164 11.985002 17.722906 8:42:04 08/21/2024
38 2.826382 1.135476 3.961858 2.753785 7.392767 17.657871 8:43:04 08/21/2024
39 1.661229 1.329536 2.990765 2.383315 5.994562 20.833656 8:44:04 08/21/2024
40 1.733689 1.070937 2.804626 3.678249 8.257100 17.647135 8:45:04 08/21/2024
41 1.333661 1.084643 2.418304 1.844093 6.732865 17.39229 8:46:04 08/21/2024
42 1.46935 1.180046 2.649396 2.083115 7.886353 18.931674 8:47:05 08/21/2024
43 2.031589 1.208142 3.239731 4.672945 10.627980 18.403103 8:48:05 08/21/2024
44 3.291229 1.155872 4.447101 2.439426 7.514135 20.305469 8:49:05 08/21/2024
45 1.887548 1.515143 3.402691 2.286661 7.980766 20.096468 8:50:05 08/21/2024
46 1.701411 1.352 3.053411 2.359823 8.270103 19.648784 8:51:05 08/21/2024
47 2.031089 1.309683 3.340772 2.520195 7.409977 19.506801 8:52:05 08/21/2024
48 2.385032 1.25273 3.637762 3.8401 8.677868 17.983028 8:53:05 08/21/2024
49 5.304321 1.256884 6.561205 9.283065 12.287288 19.067197 8:54:06 08/21/2024
50 6.63064 1.047962 7.678602 6.828019 11.898420 18.204817 8:55:06 08/21/2024
51 2.413428 1.26538 3.678808 2.888399 8.008264 18.739081 8:56:06 08/21/2024
52 2.016738 1.433913 3.450651 2.476493 7.001355 21.272152 8:57:06 08/21/2024
53 2.50811 1.405951 3.914061 3.421556 9.110397 19.726738 8:58:06 08/21/2024
54 10.007606 1.222366 11.229972 15.85246 13.578250 18.886077 8:59:06 08/21/2024
55 6.949077 1.347032 8.296109 5.102321 7.718975 19.246122 9:00:07 08/21/2024
56 4.135535 1.533817 5.669352 7.372055 10.708572 20.642937 9:01:07 08/21/2024
57 3.890881 1.413207 5.304088 4.069148 9.758490 19.724744 9:02:07 08/21/2024
58 2.021893 1.290814 3.312707 4.325459 8.018980 18.746872 9:03:07 08/21/2024
59 4.90329 1.136576 6.039866 8.943226 13.519945 17.193435 9:04:07 08/21/2024
60 5.383444 1.314299 6.697743 2.813471 9.530738 20.869188 9:05:07 08/21/2024
AVG 3.93 1.22 5.15 6.23 9.28 18.98
ppm@15% O2 1.45 1.76 2.62
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.02 0.01 0.02 0.01 0.04 0.02
810064 (100547)
FTIR Measurements
Calculated Emission Levels
XCL Resources
Against the Wind #2-2B-32
Run 1
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 8.5 Inches Kp=85.49 ft/sec Cp=0.84
Traverse Points 16 Port Point Insertion Depth dP Ts Stat P sqrt dP
Ports 2 (inches)(in h2O)(deg R)(in H2O)
EPA REFERENCE METHOD 3 A 1 0.50 0.15 1471 0.08 0.387
Average O2 0.0 (% dry)A 2 0.89 0.16 0.400
Average CO2 12.6 (% dry)A 3 1.65 0.19 0.436
Average N2 + CO 87.4 (% dry)A 4 2.75 0.21 0.458
Dry Molecular Weight 30.02 lb/lbmol A 5 5.75 0.20 0.447
Wet Molecular Weight 27.74 lb/lbmol A 6 6.85 0.18 0.424
EPA REFERENCE METHOD 320 A 7 7.61 0.17 0.412
Barometric Pressure 24.90 in Hg A 8 8.00 0.16 0.400
Moisture Content 18.98 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 5.15 ppm A 11
Calculated NOx Mass Output 0.01 lbs/hr A 12
Calculated NOx Output 0.02 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 6.23 ppm A 15
Calculated CO Mass Output 0.01 lbs/hr A 16
Calculated CO Output 0.02 g/bhp-hr B 1 0.50 0.16 1471 0.08 0.400
EPA REFERENCE METHOD 320 B 2 0.89 0.18 0.424
Average Analyzer NMNEHC Level 9.28 ppm B 3 1.65 0.20 0.447
Calculated NMNEHC Mass Output 0.02 lbs/hr B 4 2.75 0.22 0.469
Calculated NMNEHC Output 0.04 g/bhp-hr B 5 5.75 0.26 0.510
LOAD APPROXIMATION B 6 6.85 0.23 0.480
Estimated Engine Load 201.0 BHP B 7 7.61 0.21 0.458
B 8 8.00 0.20 0.447
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.2 1471 0.1 0.438
Average Stack Gas Velocity 45.85 ft/sec
Average Dry Flowrate 262.44 dscfm
TEST RUN # 1
NO Dry
(ppm)
NO2 Dry
(ppm)
NOx Dry
(ppm)
CO Dry
(ppm)
NMNEHC C3 Dry
(ppm)
H2O% (High)
191C
Time
1 2.52074 1.241839 3.762579 4.118055 7.699517 18.295608 9:07:08 08/21/2024
2 3.278522 1.211901 4.490423 2.63723 8.948966 20.321893 9:08:08 08/21/2024
3 2.241316 1.902406 4.143722 0.999166 5.928166 22.18724 9:09:08 08/21/2024
4 3.615443 1.564617 5.18006 9.971843 11.038616 19.705147 9:10:08 08/21/2024
5 6.731746 1.234251 7.965997 6.528557 11.994042 18.107599 9:11:08 08/21/2024
6 2.521166 2.011812 4.532978 4.359283 10.578603 22.096636 9:12:08 08/21/2024
7 4.963313 1.514473 6.477786 4.205344 10.728612 20.579359 9:13:08 08/21/2024
8 2.537929 1.448827 3.986756 1.968958 7.553398 19.088869 9:14:09 08/21/2024
9 2.64773 1.447085 4.094815 4.015887 9.928145 20.055098 9:15:09 08/21/2024
10 3.145657 1.216192 4.361849 4.783473 11.102982 17.557886 9:16:09 08/21/2024
11 6.207145 1.586878 7.794023 6.117189 11.693298 20.019295 9:17:09 08/21/2024
12 3.246863 1.511459 4.758322 2.889212 8.863616 19.795537 9:18:09 08/21/2024
13 1.800351 1.170608 2.970959 2.521059 9.334254 17.520449 9:19:09 08/21/2024
14 1.829431 1.515935 3.345366 1.219484 5.760376 20.990714 9:20:10 08/21/2024
15 2.405551 1.513715 3.919266 5.083773 9.565460 19.303211 9:21:10 08/21/2024
16 2.537944 1.360971 3.898915 4.003264 7.079213 19.968822 9:22:10 08/21/2024
17 2.397748 1.428589 3.826337 4.109428 8.934995 19.027821 9:23:10 08/21/2024
18 3.674566 1.198261 4.872827 5.083423 12.791284 18.219123 9:24:10 08/21/2024
19 2.656941 1.424967 4.081908 1.484889 6.565467 19.29546 9:25:10 08/21/2024
20 1.484979 1.232483 2.717462 2.25841 8.544731 17.905994 9:26:10 08/21/2024
21 4.470271 1.459636 5.929907 5.55499 10.717868 20.247533 9:27:11 08/21/2024
22 2.1072 1.38971 3.49691 2.91454 7.766631 18.597254 9:28:11 08/21/2024
23 2.045646 1.321471 3.367117 2.619887 8.228906 18.601746 9:29:11 08/21/2024
24 1.79035 1.427106 3.217456 1.716769 6.615683 19.488226 9:30:11 08/21/2024
25 1.685961 1.25633 2.942291 2.163056 6.513399 18.533726 9:31:11 08/21/2024
26 2.549628 1.500203 4.049831 3.785947 8.870327 19.972255 9:32:11 08/21/2024
27 1.561028 1.514374 3.075402 1.837334 7.918306 20.255765 9:33:12 08/21/2024
28 2.299461 1.576555 3.876016 1.474057 8.197578 20.749933 9:34:12 08/21/2024
29 1.514214 1.426375 2.940589 0.835623 5.940336 19.822077 9:35:12 08/21/2024
30 2.252842 1.449717 3.702559 4.625181 6.769396 19.855496 9:36:12 08/21/2024
31 1.806301 1.445329 3.25163 1.799814 7.379007 19.076102 9:37:12 08/21/2024
32 1.493601 1.436712 2.930313 1.230574 6.294664 19.663919 9:38:12 08/21/2024
33 2.258174 1.370641 3.628815 2.61578 9.312456 18.627677 9:39:12 08/21/2024
34 1.584287 1.328377 2.912664 1.41699 6.542034 19.567204 9:40:13 08/21/2024
35 2.878619 1.153754 4.032373 4.968981 11.610225 17.547868 9:41:13 08/21/2024
36 3.339534 1.105877 4.445411 6.078397 10.658130 18.148215 9:42:13 08/21/2024
37 7.676645 1.332629 9.009274 7.750563 11.756062 19.294955 9:43:13 08/21/2024
38 2.332905 1.530796 3.863701 1.792176 8.174988 20.576251 9:44:13 08/21/2024
39 1.515672 1.442292 2.957964 1.031026 6.134968 19.177489 9:45:13 08/21/2024
40 1.508186 1.300396 2.808582 1.266921 5.706666 19.048909 9:46:14 08/21/2024
41 1.694908 1.336263 3.031171 1.823477 6.986917 18.69914 9:47:14 08/21/2024
42 1.292452 1.026066 2.318518 1.64858 6.946220 17.234967 9:48:14 08/21/2024
43 1.788416 1.18082 2.969236 1.931191 9.587604 18.49719 9:49:14 08/21/2024
44 1.581554 1.57056 3.152114 0.844881 5.697668 20.345908 9:50:14 08/21/2024
45 1.630629 1.389779 3.020408 1.10058 7.653210 19.739098 9:51:14 08/21/2024
46 1.971594 1.293709 3.265303 2.216425 8.186901 19.118453 9:52:15 08/21/2024
47 1.534196 1.226277 2.760473 2.044122 7.111313 18.297188 9:53:15 08/21/2024
48 1.711739 1.542618 3.254357 0.676142 6.129180 21.176789 9:54:15 08/21/2024
49 1.556003 1.512963 3.068966 1.967357 7.556140 19.515066 9:55:15 08/21/2024
50 2.06423 1.510494 3.574724 1.708311 9.675828 20.250335 9:56:15 08/21/2024
51 1.878862 1.250352 3.129214 3.548607 10.266811 17.947162 9:57:15 08/21/2024
52 3.566894 1.33595 4.902844 3.759285 11.293313 20.136589 9:58:15 08/21/2024
53 3.05883 1.813858 4.872688 2.431046 9.453820 21.369084 9:59:16 08/21/2024
54 2.839719 1.5976 4.437319 3.556402 11.048273 20.921646 10:00:16 08/21/2024
55 4.261023 1.316112 5.577135 3.491227 9.357646 18.407242 10:01:16 08/21/2024
56 1.991387 1.100656 3.092043 4.605797 9.068757 16.715106 10:02:16 08/21/2024
57 2.303518 1.002773 3.306291 3.267651 6.477088 17.047441 10:03:16 08/21/2024
58 1.461364 1.164638 2.626002 1.458494 6.278157 18.808584 10:04:16 08/21/2024
59 2.214659 1.788701 4.00336 2.132383 10.164361 21.615455 10:05:16 08/21/2024
60 1.557792 1.511021 3.068813 1.022531 6.758316 20.102368 10:06:17 08/21/2024
AVG 2.55 1.40 3.95 3.02 8.52 19.38
ppm@15% O2 1.12 0.85 2.41
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.02 0.01 0.01 0.00 0.03 0.02
Calculated Emission Levels
Record Date
XCL Resources
Against the Wind #2-2B-32
Run 2
810064 (100547)
FTIR Measurements
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 8.5 Inches Kp=85.49 ft/sec Cp=0.84
Traverse Points 16 Port Point Insertion Depth dP Ts Stat P sqrt dP
Ports 2 (inches)(in h2O)(deg R)(in H2O)
EPA REFERENCE METHOD 3 A 1 0.50 0.14 1472 0.08 0.374
Average O2 0.0 (% dry)A 2 0.89 0.16 0.400
Average CO2 12.6 (% dry)A 3 1.65 0.18 0.424
Average N2 + CO 87.4 (% dry)A 4 2.75 0.22 0.469
Dry Molecular Weight 30.02 lb/lbmol A 5 5.75 0.25 0.500
Wet Molecular Weight 27.69 lb/lbmol A 6 6.85 0.23 0.480
EPA REFERENCE METHOD 320 A 7 7.61 0.20 0.447
Barometric Pressure 24.9 in Hg A 8 8.00 0.18 0.424
Moisture Content 19.38 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 3.95 ppm A 11
Calculated NOx Mass Output 0.01 lbs/hr A 12
Calculated NOx Output 0.02 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 3.02 ppm A 15
Calculated CO Mass Output 0.00 lbs/hr A 16
Calculated CO Output 0.01 g/bhp-hr B 1 0.50 0.15 1472 0.08 0.387
EPA REFERENCE METHOD 320 B 2 0.89 0.16 0.400
Average Analyzer NMNEHC Level 8.52 ppm B 3 1.65 0.18 0.424
Calculated NMNEHC Mass Output 0.02 lbs/hr B 4 2.75 0.20 0.447
Calculated NMNEHC Output 0.03 g/bhp-hr B 5 5.75 0.24 0.490
LOAD APPROXIMATION B 6 6.85 0.22 0.469
Estimated Engine Load 201.0 BHP B 7 7.61 0.19 0.436
B 8 8.00 0.17 0.412
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.2 1472 0.1 0.437
Average Stack Gas Velocity 45.80 ft/sec
Average Dry Flowrate 260.67 dscfm
TEST RUN # 2
NO Dry
(ppm)
NO2 Dry
(ppm)
NOx Dry
(ppm)
CO Dry
(ppm)
NMNEHC C3 Dry
(ppm)
H2O% (High)
191C
Time
1 2.414987 1.409846 3.824833 2.388672 6.804840 19.477836 10:08:17 08/21/2024
2 7.031778 1.580104 8.611882 9.905746 12.926763 20.701146 10:09:17 08/21/2024
3 4.0411 1.339485 5.380585 3.590309 7.720365 19.084378 10:10:17 08/21/2024
4 1.995928 1.543875 3.539803 1.459725 7.702323 21.101968 10:11:17 08/21/2024
5 1.497467 1.384165 2.881632 1.170065 7.354185 19.089533 10:12:17 08/21/2024
6 1.65911 1.257417 2.916527 1.101354 5.862414 18.674627 10:13:18 08/21/2024
7 2.195804 1.253251 3.449055 4.692477 6.090752 18.448415 10:14:18 08/21/2024
8 1.881812 1.594062 3.475874 1.880982 9.657223 20.283888 10:15:18 08/21/2024
9 1.945731 1.161452 3.107183 1.537231 8.790710 18.65866 10:16:18 08/21/2024
10 4.523307 0.936689 5.459996 7.558955 11.831702 17.050384 10:17:18 08/21/2024
11 2.323553 1.391395 3.714948 2.070324 7.809102 19.497264 10:18:18 08/21/2024
12 3.673812 1.42548 5.099292 4.759259 10.861226 19.29343 10:19:19 08/21/2024
13 2.578653 1.230653 3.809306 5.256618 9.454640 18.09846 10:20:19 08/21/2024
14 3.405593 1.212417 4.61801 4.07884 7.695331 17.902055 10:21:19 08/21/2024
15 3.832528 1.374974 5.207502 9.897266 11.979460 21.430401 10:22:19 08/21/2024
16 2.796068 1.44388 4.239948 1.769957 6.223953 19.745781 10:23:19 08/21/2024
17 2.178625 1.500419 3.679044 2.305419 7.336102 19.994916 10:24:19 08/21/2024
18 7.819186 1.261227 9.080413 13.813318 13.963038 18.261285 10:25:19 08/21/2024
19 2.570617 1.293702 3.864319 1.658007 6.420900 19.29587 10:26:20 08/21/2024
20 1.904519 1.586709 3.491228 3.099038 6.896916 20.251463 10:27:20 08/21/2024
21 6.264472 1.371529 7.636001 7.961715 13.223227 19.530108 10:28:20 08/21/2024
22 3.435486 1.409296 4.844782 2.452482 7.569934 19.659625 10:29:20 08/21/2024
23 2.855685 1.496739 4.352424 3.424482 9.448229 19.923813 10:30:20 08/21/2024
24 1.688638 1.376998 3.065636 1.469782 7.302804 20.343258 10:31:20 08/21/2024
25 1.487976 1.368636 2.856612 0.990127 5.851272 18.961147 10:32:21 08/21/2024
26 1.581207 1.409818 2.991025 1.289696 6.463267 18.665208 10:33:21 08/21/2024
27 1.342952 1.167686 2.510638 1.737185 7.173444 17.326687 10:34:21 08/21/2024
28 1.633195 1.45337 3.086565 0.833105 6.576284 20.188496 10:35:21 08/21/2024
29 1.642468 1.331926 2.974394 1.511717 8.469246 19.397456 10:36:21 08/21/2024
30 2.053148 1.66466 3.717808 1.377822 7.497414 20.918776 10:37:21 08/21/2024
31 2.616739 1.411143 4.027882 3.156568 9.564745 19.102777 10:38:21 08/21/2024
32 1.555264 1.480732 3.035996 1.207917 6.333119 19.911055 10:39:22 08/21/2024
33 1.427991 1.432938 2.860929 1.053924 7.580356 19.247835 10:40:22 08/21/2024
34 2.05582 1.309357 3.365177 2.590948 9.019042 18.279134 10:41:22 08/21/2024
35 1.443285 1.142967 2.586252 2.021887 8.143751 17.908622 10:42:22 08/21/2024
36 2.448256 1.818469 4.266725 1.723406 9.702228 22.27538 10:43:22 08/21/2024
37 1.932147 1.325224 3.257371 2.195983 7.823503 18.687186 10:44:22 08/21/2024
38 1.452071 1.239777 2.691848 1.456768 6.070119 18.548992 10:45:22 08/21/2024
39 1.478575 1.410961 2.889536 1.102013 6.848063 19.29699 10:46:23 08/21/2024
40 1.702061 1.417103 3.119164 1.498063 7.608928 19.333888 10:47:23 08/21/2024
41 2.334563 1.318156 3.652719 5.362043 12.314387 19.632109 10:48:23 08/21/2024
42 7.356729 1.785633 9.142362 6.470628 12.279871 21.311719 10:49:23 08/21/2024
43 3.180261 1.316543 4.496804 4.349262 10.631304 18.256652 10:50:23 08/21/2024
44 2.370509 1.693156 4.063665 1.652678 8.439297 21.058099 10:51:23 08/21/2024
45 1.628356 1.344764 2.97312 1.253068 6.913002 18.811752 10:52:24 08/21/2024
46 1.542477 1.182023 2.7245 2.276173 6.821232 17.637445 10:53:24 08/21/2024
47 1.761534 1.139813 2.901347 1.234611 5.770442 18.792005 10:54:24 08/21/2024
48 1.987662 1.513486 3.501148 2.114232 9.487756 19.813169 10:55:24 08/21/2024
49 1.847112 1.278111 3.125223 2.269652 4.760590 19.337309 10:56:24 08/21/2024
50 3.294614 1.478688 4.773302 5.330766 11.320108 19.811282 10:57:24 08/21/2024
51 4.459517 1.421568 5.881085 4.294829 9.976070 19.275786 10:58:24 08/21/2024
52 2.309792 1.365159 3.674951 1.877831 6.511994 18.998374 10:59:25 08/21/2024
53 3.847464 1.172141 5.019605 5.265961 10.962428 17.563893 11:00:25 08/21/2024
54 1.560554 1.145201 2.705755 2.713123 6.927217 17.141594 11:01:25 08/21/2024
55 2.219599 1.295408 3.515007 2.875465 9.996861 18.511414 11:02:25 08/21/2024
56 1.815292 1.236046 3.051338 2.22014 7.255970 18.951018 11:03:25 08/21/2024
57 4.074401 1.019701 5.094102 5.348923 9.859745 17.04393 11:04:25 08/21/2024
58 2.963043 1.258349 4.221392 3.355672 11.132170 23.116395 11:05:26 08/21/2024
59 2.246452 1.371814 3.618266 2.227553 7.822290 19.182417 11:06:26 08/21/2024
60 1.908542 1.226674 3.135216 2.672373 9.441159 17.936927 11:07:26 08/21/2024
AVG 2.65 1.36 4.01 3.17 8.50 19.27
ppm@15% O2 1.13 0.89 2.40
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.02 0.01 0.01 0.00 0.04 0.02
FTIR Measurements
810064 (100547)
Calculated Emission Levels
XCL Resources
Against the Wind #2-2B-32
Run 3
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 8.5 Inches Kp=85.49 ft/sec Cp=0.84
Traverse Points 16 Port Point Insertion Depth dP Ts Stat P sqrt dP
Ports 2 (inches)(in h2O)(deg R)(in H2O)
EPA REFERENCE METHOD 3 A 1 0.50 0.19 1473 0.09 0.436
Average O2 0.0 (% dry)A 2 0.89 0.21 0.458
Average CO2 12.6 (% dry)A 3 1.65 0.23 0.480
Average N2 + CO 87.4 (% dry)A 4 2.75 0.25 0.500
Dry Molecular Weight 30.02 lb/lbmol A 5 5.75 0.29 0.539
Wet Molecular Weight 27.70 lb/lbmol A 6 6.85 0.26 0.510
EPA REFERENCE METHOD 320 A 7 7.61 0.23 0.480
Barometric Pressure 24.9 in Hg A 8 8.00 0.21 0.458
Moisture Content 19.27 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 4.01 ppm A 11
Calculated NOx Mass Output 0.01 lbs/hr A 12
Calculated NOx Output 0.02 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 3.17 ppm A 15
Calculated CO Mass Output 0.00 lbs/hr A 16
Calculated CO Output 0.01 g/bhp-hr B 1 0.50 0.20 1473 0.09 0.447
EPA REFERENCE METHOD 320 B 2 0.89 0.21 0.458
Average Analyzer NMNEHC Level 8.50 ppm B 3 1.65 0.24 0.490
Calculated NMNEHC Mass Output 0.02 lbs/hr B 4 2.75 0.26 0.510
Calculated NMNEHC Output 0.04 g/bhp-hr B 5 5.75 0.30 0.548
LOAD APPROXIMATION B 6 6.85 0.27 0.520
Estimated Engine Load 201.0 BHP B 7 7.61 0.25 0.500
B 8 8.00 0.22 0.469
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.2 1473 0.1 0.488
Average Stack Gas Velocity 51.16 ft/sec
Average Dry Flowrate 291.41 dscfm
TEST RUN # 3

APPENDIX B

Date Time NO 191C span NO2 191C span H2O% (high) 191C Formaldehyde 191C Ethylene 191C TE span Propane 191C span Acetaldehyde 191C span CO ppm 191C (1of2) spanCO ppm Dry CO2% 191C NOx Wet NOx Dry NM NE HC C3 Temp ( C )Pressure (atm)8/21/2024 7:47:24 0.102758 -0.017069 -0.058481 -0.013567 -0.17863 0.201709 -0.303097 -0.075336 -0.075292 0.005751 0.085689 0.085639 0.009604 190.984467 1.0473598/21/2024 7:47:32 0.063411 0.015723 -0.061048 0.043138 -0.372734 0.272839 -0.001044 -0.040633 -0.040608 0.012201 0.079134 0.079086 0.00604 190.984467 1.0463938/21/2024 7:47:39 0.105745 0.050482 -0.064123 0.056791 -0.345163 -0.099718 0.251072 -0.162586 -0.162482 0.009833 0.156226 0.156126 -0.003784 190.984467 1.017925
8/21/2024 7:47:47 -0.004085 0.002025 -0.064046 -0.01694 -0.17121 -0.038686 -0.214312 -0.091346 -0.091287 0.014363 -0.00206 -0.002058 -0.001466 190.984467 1.026338/21/2024 7:48:26 0 0 0 0 0 0 0 0 0 0 0 0 0 190.984467 1.028164
8/21/2024 7:48:39 -0.017427 -0.054589 0.000568 0.000877 -0.321705 0.282849 0.02176 0.11482 0.114821 0.008777 -0.072016 -0.072016 0.007062 190.986572 1.0244898/21/2024 7:48:47 0.039172 0.007133 -0.000856 0.074677 -0.090603 0.063332 0.160081 0.079137 0.079136 -0.001058 0.046305 0.046304 0.008092 191.008987 1.0215828/21/2024 7:48:54 -0.0359 0.005503 -0.001678 -0.004053 0.069226 0.166878 0.016257 0.115358 0.115356 0.005074 -0.030396 -0.030396 0.021569 191.028061 1.0204478/21/2024 7:49:02 -0.049842 -0.017759 -0.002897 0.046823 -0.246075 0.345322 0.054166 -0.066739 -0.066737 -0.000196 -0.067601 -0.067599 0.02973 191.06076 1.0263188/21/2024 7:49:09 -0.140404 0.018714 -0.00247 -0.034696 -0.058698 -0.03162 -0.260629 0.057687 0.057685 -0.004051 -0.12169 -0.121687 0.019145 191.06076 1.0189218/21/2024 7:49:17 -0.059307 0.038155 -0.002526 -0.011925 -0.136834 0.069623 0.074807 0.089805 0.089803 0.000706 -0.021152 -0.021151 0.004244 191.06076 1.0130678/21/2024 7:49:24 -0.034931 -0.009275 -0.003082 0.015914 -0.209939 0.056487 0.090924 -0.095702 -0.095699 0.002667 -0.044207 -0.044205 0.007035 191.06076 1.025693
8/21/2024 7:49:32 -0.082255 -0.006808 -0.004258 -0.009417 0.379318 0.130658 0.146791 0.057116 0.057114 0.010026 -0.089063 -0.089059 0.016673 191.06076 1.0158698/21/2024 7:49:39 -0.019675 0.025315 -0.000266 -0.005731 0.114485 0.258924 0.080677 -0.009582 -0.009581 0.000947 0.00564 0.00564 0.015048 191.06076 1.023028
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Temp ( C )Pressure (atm)Date Time Ethylene 191C TE Temp ( C )Pressure (atm)8/21/2024 7:50:15 507.47685 518.419452 507.255109 191.06076 1.020812 8/21/2024 7:53:34 98.060733 190.984467 1.0307078/21/2024 7:50:23 511.970912 522.742739 511.02334 191.058945 1.017432 8/21/2024 7:53:42 98.026547 190.984467 1.03348
8/21/2024 7:50:30 503.236113 514.185065 501.463227 191.020798 1.033279 8/21/2024 7:53:49 98.837276 190.984467 1.0240898/21/2024 7:50:38 503.323435 514.929832 504.564131 190.984467 1.029912 8/21/2024 7:53:57 99.320891 190.984467 1.0239868/21/2024 7:50:45 507.601964 519.382523 508.879326 190.984467 1.019844 8/21/2024 7:54:05 99.600683 190.984467 1.0195148/21/2024 7:50:53 510.593655 521.559749 509.997703 190.984467 1.017765 8/21/2024 7:54:12 99.154533 190.984467 1.0283548/21/2024 7:51:00 508.537258 519.54595 508.510837 190.984467 1.018132 8/21/2024 7:54:20 99.164259 190.984467 1.0266488/21/2024 7:51:08 506.921284 518.487812 507.452592 190.984467 1.02361 8/21/2024 7:54:27 99.16489 190.984467 1.0209378/21/2024 7:51:15 506.075728 517.288948 505.594539 190.984467 1.021208 8/21/2024 7:54:35 99.579398 190.984467 1.020277
8/21/2024 7:51:23 505.290614 516.475249 505.540528 190.984467 1.022689 8/21/2024 7:54:42 99.966309 190.984467 1.020102
Date Time NO2 191C span Temp ( C )Pressure (atm)8/21/2024 7:51:58 129.06765 190.984467 1.0114758/21/2024 7:52:05 138.10733 190.984467 1.0284698/21/2024 7:52:13 140.995821 190.984467 1.022764
8/21/2024 7:52:20 143.193167 190.984467 1.0149628/21/2024 7:52:28 142.007173 190.984467 1.0285198/21/2024 7:52:35 143.803866 190.984467 1.0185088/21/2024 7:52:43 144.626318 190.984467 1.0157488/21/2024 7:52:50 142.915711 190.984467 1.024988/21/2024 7:52:58 144.61145 190.984467 1.0189248/21/2024 7:53:05 144.746449 190.984467 1.017062
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Temp ( C )Pressure (atm)Date Time Ethylene 191C TE Temp ( C )Pressure (atm)8/21/2024 7:55:14 185.337383 212.464433 160.96492 190.984467 0.989584 8/21/2024 7:56:55 51.563727 191.06076 1.0019528/21/2024 7:55:22 477.601424 492.447497 477.103404 190.984467 1.000108 8/21/2024 7:57:02 98.175466 190.969925 0.9982098/21/2024 7:55:29 477.806262 492.510902 474.821534 190.984467 1.025908 8/21/2024 7:57:10 99.207406 190.963577 0.9988778/21/2024 7:55:37 506.258901 518.185849 505.259572 190.984467 1.017191 8/21/2024 7:57:17 98.124753 190.95903 1.022834
8/21/2024 7:55:44 504.845952 516.875387 506.45082 191.00592 1.019875 8/21/2024 7:57:25 98.651778 190.95903 1.0304578/21/2024 7:55:52 508.930262 519.967996 507.842414 191.04895 1.016867 8/21/2024 7:57:32 98.350257 190.95903 1.029287
8/21/2024 7:55:59 504.720243 516.020311 504.787916 191.06076 1.019893 8/21/2024 7:57:40 99.419871 190.95903 1.0207048/21/2024 7:56:07 508.137166 519.279548 507.564362 191.06076 1.017788 8/21/2024 7:57:47 98.584177 190.95903 1.0244918/21/2024 7:56:14 504.592298 515.82624 502.946288 191.06076 1.024388 8/21/2024 7:57:55 98.582204 190.95903 1.0271558/21/2024 7:56:22 507.079344 518.712068 507.668543 191.06076 1.018445 8/21/2024 7:58:02 98.954105 190.95903 1.025929
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)8/21/2024 7:58:25 0.135047 0.190359 0.468639 0.218019 190.965393 1.010198/21/2024 7:58:32 0.079531 0.0866 0.188525 0.107723 190.965393 1.0123498/21/2024 7:58:40 0.019436 0.089776 0.101227 -0.136095 190.965393 1.0170498/21/2024 7:58:47 0.063341 0.027138 0.218516 0.129238 190.965393 1.0053488/21/2024 7:58:55 -0.038225 0.091626 0.259957 -0.228085 190.965393 1.010026
8/21/2024 7:59:02 -0.009022 0.070013 0.462836 -0.204705 190.965393 1.0117648/21/2024 7:59:10 0.069174 -0.026623 0.3372 -0.144866 190.965393 1.016629
8/21/2024 7:59:17 0.099228 -0.069135 0.20502 -0.068095 190.965393 1.01588
Raw Calibration Data
BACKGROUND / PRE DIRECT ZERO
PRE DIRECT CAL
NO2 CAL
PRE SYSTEM CAL
PRE SYSTEM ZERO
Date Time CO2% 191C Propane 191C span Temp ( C )Pressure (atm)
8/21/2024 8:01:14 11.662958 9.583714 190.971741 1.0026738/21/2024 8:01:21 11.67351 9.058419 190.971741 0.9974818/21/2024 8:01:29 11.745184 10.31992 190.971741 0.991758/21/2024 8:01:36 11.541614 12.981764 190.971741 0.9907138/21/2024 8:01:44 11.283304 10.816585 190.971741 0.9867368/21/2024 8:02:21 11.142943 6.497215 190.971741 0.989858/21/2024 8:02:29 8.012837 26.283727 190.971741 1.001116
8/21/2024 8:02:36 5.132084 237.413584 190.971741 0.9936668/21/2024 8:02:44 7.311828 151.812318 190.971741 0.9829138/21/2024 8:02:51 10.566077 43.516992 190.971741 0.9875258/21/2024 8:02:59 10.401962 48.704585 190.971741 0.9919488/21/2024 8:03:06 10.027102 57.17296 190.971741 0.9964228/21/2024 8:03:14 9.855149 66.760637 190.971741 0.9981758/21/2024 8:03:21 9.818445 66.530003 190.971741 0.997151
8/21/2024 8:03:29 10.07177 56.614393 190.971741 0.9923548/21/2024 8:03:36 10.19691 48.422846 190.971741 0.994724
8/21/2024 8:04:14 10.190454 43.049295 191.020432 0.989936
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Temp ( C )Pressure (atm)Date Time Ethylene 191C TE Temp ( C )Pressure (atm)8/21/2024 11:19:51 499.155093 511.302457 499.36703 191.037979 1.009217 8/21/2024 11:18:13 98.662401 190.954407 1.017141
8/21/2024 11:19:58 503.067234 516.224506 504.164269 191.009888 1.009272 8/21/2024 11:18:20 98.767588 190.981277 1.017088/21/2024 11:20:06 503.247035 516.756805 504.581146 190.967209 1.009318 8/21/2024 11:18:28 98.856052 190.988998 1.0169798/21/2024 11:20:13 502.961524 516.120224 506.46826 190.965393 1.009206 8/21/2024 11:18:35 99.065823 190.998993 1.0171148/21/2024 11:20:21 502.615073 515.967422 504.121504 190.965393 1.009134 8/21/2024 11:18:43 98.887903 191.05043 1.0114688/21/2024 11:20:28 502.486208 516.603364 505.166736 190.965393 1.009123 8/21/2024 11:18:50 99.199595 191.090729 1.012188/21/2024 11:20:36 502.442739 515.581806 506.488799 190.965393 1.009077 8/21/2024 11:18:58 98.824482 191.075287 1.0123048/21/2024 11:20:43 502.947932 516.616769 504.628673 190.965393 1.009209 8/21/2024 11:19:06 98.760037 191.044067 1.012296
8/21/2024 11:20:51 503.084133 516.621783 504.735473 190.965393 1.009066 8/21/2024 11:19:13 98.839859 191.041687 1.0123528/21/2024 11:20:58 502.57245 516.390973 505.466602 190.965393 1.009149 8/21/2024 11:19:21 98.686947 191.041687 1.012479
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Temp ( C )Pressure (atm)Date Time Ethylene 191C TE Temp ( C )Pressure (atm)8/21/2024 11:18:28 -0.014707 0.078952 -0.048634 190.988998 1.016979 8/21/2024 11:21:46 -0.623908 190.965393 1.0107818/21/2024 11:18:35 -0.150716 0.234918 0.021279 190.998993 1.017114 8/21/2024 11:21:53 -0.563691 190.965393 1.010926
8/21/2024 11:18:43 0.046273 0.115229 -0.470621 191.05043 1.011468 8/21/2024 11:22:01 -0.401166 190.969925 1.0108268/21/2024 11:18:50 0.038797 0.02037 -0.027342 191.090729 1.01218 8/21/2024 11:22:08 -0.368049 191.002625 1.0110598/21/2024 11:18:58 -0.102065 0.10803 0.127639 191.075287 1.012304 8/21/2024 11:22:16 -0.890227 191.027145 1.0109448/21/2024 11:19:06 -0.132004 0.136964 -0.009949 191.044067 1.012296 8/21/2024 11:22:23 -0.505498 191.041687 1.0110168/21/2024 11:19:13 -0.072245 0.069554 0.268396 191.041687 1.012352 8/21/2024 11:22:31 -0.492155 191.041687 1.0108468/21/2024 11:19:21 -0.220171 0.008997 -0.164106 191.041687 1.012479 8/21/2024 11:22:38 -0.386719 191.041687 1.010763
POST SYSTEM ZERO
SAMPLE SPIKE RECOVERY
POST SYSTEM CAL
PRE TEST 1 497.5 11.5 9.9 10.5 46.1 0.089 74.6%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 516.5 514.5 0.0 0.38 -0.01
CO 505.3 501.8 0.0 0.70 0.01
Propane 505.5 497.5 0.1 1.62 0.03
Ethylene 100.0 99.76 -0.1 0.21 -0.08
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 518.7 514.5 0.1 0.82 0.01
CO 507.1 501.8 0.0 1.05 0.01
Propane 507.7 497.5 0.3 2.04 0.06
Ethylene*99.0 99.76 0.0 -0.81 -0.04
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 516.4 514.5 0.1 0.37 0.02 0.45 0.01
CO 502.6 501.8 -0.1 0.15 -0.01 0.90 0.02
Propane 505.5 497.5 0.0 1.60 0.00 0.44 0.06
Ethylene*98.7 99.76 -0.6 -1.08 -0.57 0.27 0.53
*CTS Scans are conducted with Ethylene through the sample line.
Stack Propane
Concentration
Stack + Spike CO2
Concentration
Stack + Propane
Concentration
DF
Calculated
POST SYSTEM CAL
PRE SYSTEM CAL
% Recovery
Propane
PRE DIRECT CAL
FTIR QA/QC SUMMARY
SAMPLE RECOVERY CALCULATIONS
Period Spike #Concentration of
Propane Cylinder
Stack CO2
Concentration
XCL - Against the Wind #2-2B-32
8-21-24
XCL - Against the Wind #2-2B-32
8-21-24
XCL - Against the Wind #2-2B-32
8-21-24

Spectral Fit
Run 1

Spectral Fit
Run 2
Spectral Fit
Run 3

Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000143.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000068.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000069.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000070.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000071.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000072.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000073.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000074.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 1.45 2.3 3.95 0.24 0.32 3.14 3.14 4.43 4.43 0.48 1.32 0-2795 1.03 Close to DL
NO2 191C 1.18 0.71 0.23 0.03 0.03 0.74 0.74 0.29 0.65 0.05 0.08 0-488 1.01 Close to DL
N2O 191C 11.25 0.56 -0.03 0.03 0.64 0.64 -0.3 --0-200 -Good
NH3 TE 191C 0.54 37.38 2.58 4.14 7.06 63.8 63.8 2.98 33.45 0.4 0.86 0-2995 -Close to DL
H2O% (HIGH) 191C21.19 0.45 -0.02 0.03 0.7 0.7 -0.42 --0-40 -Good
FORMALDEHYDE 191C-0.07 0.52 0.11 0.24 0.27 0.59 0.59 0.11 0.28 0 0.04 0-69 -Close to DL
FORMIC ACID 191C TE-0.11 5.34 0.78 1.56 1.83 6.25 6.25 1.07 3.84 0.3 0.26 0-466 -Close to DL
CH4 2900 CM-1 191C350.42 8.71 -1.64 2.38 17.54 17.54 -7.01 --0-3143 0.97 Good
PROPANE 191C 5.44 0.76 -0.22 0.27 0.91 0.91 -0.4 --0-4976 0.95 Good
PROPYLENE 191C TE-1.82 6.32 2.45 1.57 1.86 7.48 7.48 2.71 4.72 0.25 0.82 0-194 -Close to DL
ETHANE 191C 20.68 1.54 -0.55 0.85 2.4 2.4 -0.57 --0-1004 -Good
ETHYLENE 191C TE1.61 17.79 2.17 2.07 2.55 21.95 21.95 2.35 15.74 0.17 0.72 0-900 -Close to DL
CO PPM 191C (1OF2)2.28 1.35 8.28 0.25 0.55 2.91 2.91 9.3 9.3 1.02 2.76 0-5010 1.01 Close to DL
CO2% 191C 9.97 0.25 -0.01 0.02 0.34 0.34 -0.2 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C-0.31 1.44 0.71 0.63 0.81 1.85 1.85 0.8 0.81 0.09 0.24 0-186 1 Close to DL
ACETYLENE 191C0.17 3.72 0.29 0.79 1.05 4.91 4.91 0.33 2.96 0.04 0.1 0-1016 -Close to DL
SO2 191C 7.17 6.89 1.47 0.26 0.32 8.4 8.4 1.58 6.46 0.1 0.49 0-964 1.02 Close to DL
HEXANE 191C 0 0.51 0.35 0.13 0.18 0.69 0.69 0.45 0.45 0.11 0.12 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000204.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000068.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000069.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000070.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000071.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000072.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000073.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000074.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 2.63 2.82 3.95 0.24 0.32 3.85 3.85 4.43 4.43 0.48 1.32 0-2795 1.03 Close to DL
NO2 191C 1.07 0.79 0.23 0.03 0.03 0.83 0.83 0.29 0.74 0.05 0.08 0-488 1.01 Close to DL
N2O 191C 12.1 0.53 -0.03 0.03 0.6 0.6 -0.28 --0-200 -Good
NH3 TE 191C -3.97 31.89 2.58 4.14 7.06 54.44 54.44 2.98 27.86 0.4 0.86 0-2995 -Close to DL
H2O% (HIGH) 191C20.14 0.45 -0.02 0.03 0.7 0.7 -0.4 --0-40 -Good
FORMALDEHYDE 191C-0.05 0.51 0.11 0.24 0.27 0.58 0.58 0.11 0.27 0 0.04 0-69 -Close to DL
FORMIC ACID 191C TE-0.12 5.79 0.78 1.56 1.83 6.77 6.77 1.07 4.28 0.3 0.26 0-466 -Close to DL
CH4 2900 CM-1 191C393.8 9.02 -1.64 2.38 18.16 18.16 -7.88 --0-3143 0.97 Good
PROPANE 191C 8.23 0.77 -0.22 0.27 0.93 0.93 -0.35 --0-4976 0.95 Good
PROPYLENE 191C TE-1.11 6.72 2.45 1.57 1.86 7.94 7.94 2.71 5.14 0.25 0.82 0-194 -Close to DL
ETHANE 191C 28.17 1.53 -0.55 0.85 2.38 2.38 -0.58 --0-1004 -Good
ETHYLENE 191C TE2.06 18.37 2.17 2.07 2.55 22.66 22.66 2.35 16.3 0.17 0.72 0-900 -Close to DL
CO PPM 191C (1OF2)3.06 1.24 8.28 0.25 0.55 2.67 2.67 9.3 9.3 1.02 2.76 0-5010 1.01 Close to DL
CO2% 191C 10.09 0.25 -0.01 0.02 0.34 0.34 -0.2 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C-0.4 1.42 0.71 0.63 0.81 1.83 1.83 0.8 0.8 0.09 0.24 0-186 1 Close to DL
ACETYLENE 191C0.32 3.33 0.29 0.79 1.05 4.4 4.4 0.33 2.57 0.04 0.1 0-1016 -Close to DL
SO2 191C 6.56 6.3 1.47 0.26 0.32 7.68 7.68 1.58 5.89 0.1 0.49 0-964 1.02 Close to DL
HEXANE 191C 0.11 0.53 0.35 0.13 0.18 0.72 0.72 0.45 0.45 0.11 0.12 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000265.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000068.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000069.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000070.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000071.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000072.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000073.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000074.LAB
C:\OLT\Data\XCL Resources\ATW WPI819 8-21-24\XCL ATW WPI819 8-21-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 1.73 2.78 3.95 0.24 0.32 3.79 3.79 4.43 4.43 0.48 1.32 0-2795 1.03 Close to DL
NO2 191C 1.11 0.72 0.23 0.03 0.03 0.76 0.76 0.29 0.68 0.05 0.08 0-488 1.01 Close to DL
N2O 191C 14.05 0.68 -0.03 0.03 0.78 0.78 -0.37 --0-200 -Good
NH3 TE 191C -2.62 33.97 2.58 4.14 7.06 57.99 57.99 2.98 29.98 0.4 0.86 0-2995 -Close to DL
H2O% (HIGH) 191C19 0.45 -0.02 0.03 0.7 0.7 -0.38 --0-40 -Good
FORMALDEHYDE 191C-0.1 0.5 0.11 0.24 0.27 0.57 0.57 0.11 0.26 0 0.04 0-69 -Close to DL
FORMIC ACID 191C TE-0.25 5.13 0.78 1.56 1.83 6.01 6.01 1.07 3.62 0.3 0.26 0-466 -Close to DL
CH4 2900 CM-1 191C356.67 8.9 -1.64 2.38 17.92 17.92 -7.13 --0-3143 0.97 Good
PROPANE 191C 5.25 0.73 -0.22 0.27 0.88 0.88 -0.37 --0-4976 0.95 Good
PROPYLENE 191C TE-1.44 6.08 2.45 1.57 1.86 7.19 7.19 2.71 4.49 0.25 0.82 0-194 -Close to DL
ETHANE 191C 20.19 1.45 -0.55 0.85 2.26 2.26 -0.52 --0-1004 -Good
ETHYLENE 191C TE1.37 17.6 2.17 2.07 2.55 21.71 21.71 2.35 15.55 0.17 0.72 0-900 -Close to DL
CO PPM 191C (1OF2)1.57 1.22 8.28 0.25 0.55 2.63 2.63 9.3 9.3 1.02 2.76 0-5010 1.01 Close to DL
CO2% 191C 10.23 0.26 -0.01 0.02 0.36 0.36 -0.2 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C-0.03 1.39 0.71 0.63 0.81 1.79 1.79 0.8 0.8 0.09 0.24 0-186 1 Close to DL
ACETYLENE 191C0.15 3.47 0.29 0.79 1.05 4.58 4.58 0.33 2.71 0.04 0.1 0-1016 -Close to DL
SO2 191C 6.95 6.02 1.47 0.26 0.32 7.34 7.34 1.58 5.6 0.1 0.49 0-964 1.02 Close to DL
HEXANE 191C -0.07 0.49 0.35 0.13 0.18 0.67 0.67 0.45 0.45 0.11 0.12 0-1000 -Close to DL

APPENDIX C

Customer:XCLProject:Against the Wind #2-2B-32
Engine Information:Waukesha F18GSI
Calculated By:Charles Chapman
Date Performed:21-Aug-24
Additional Notes:
Calculate:1
Select Engine Model:
Engine/Site
5 Required Inputs:F18GSID Values Multiplier Resultant
Intake Manifold Pressure (inHG gauge)3.983
Engine Speed (RPM)1520 0.1344 204.288
IMP x RPM 0.004793
Intake Manifold Temperature (°F)149 -0.5179 -77.1671
Ignition Timing (°BTDC)24 1.507 36.168
Exhaust Oxygen (dry volume %)-10.58
Altitude (ft)5831 -0.003983 -23.224873
Intercept 1 61 61
Calculated Bhp 201
Calculated kWb 150
Calculated BMEP (psi)
Calculated BMEP (bar)
Based on the following data ranges: (Reference Service Bulletin 14-2749D or latest revision)
Dry Commercial Quality Natural (64 – 90 WKI™)
75 –185 psi BMEP
0 – 16 in Hg (gauge) Intake Manifold Pressure
130 – 175° F Intercooler Water Inlet Temperature
1000 – 1800 RPM Engine Speed
16 – 28° BTDC Ignition Timing
15:5 – 18:1 Mass Air/Fuel Ratio
8.7:1 Compression Ratio
** Accuracy is ±3% on power, and ±1.0 inHG for intake manifold pressure
** The above calculation is intended as a guide for estimating average horsepower or intake
manifold pressure for a VGF-GSID engine
Avg Run
Waukesha Engine
BHP / IMP Prediction
VGF GSID MenuClear
VGF Instructions
BHP IMP
Waukesha Engine, Dresser, Inc.Bhp-Pred v1.6

APPENDIX D

Test
Run
Flowrate
dscfm
Approx.
BHP
Avg O2
%
NOx
ppmvd
NOx
g/bhp-hr
NOx
lbs/hr
CO
ppmvd
CO
g/bhp-hr
CO
lbs/hr
NMNEHC
ppmvd
NMNEHC
g/bhp-hr
NMNEHC
lbs/hr
Moisture
Content %
1 262.44 201.0 0.0 5.15 0.02 0.01 6.23 0.02 0.01 9.28 0.04 0.02 18.98
2 260.67 201.0 0.0 3.95 0.02 0.01 3.02 0.01 0.00 8.52 0.03 0.02 19.38
3 291.41 201.0 0.0 4.01 0.02 0.01 3.17 0.01 0.00 8.50 0.04 0.02 19.27
201.0 0.0 4.37 0.02 0.01 4.14 0.01 0.00 8.77 0.04 0.02 19.21
Summary
Average Levels
Example Calculations: XCL Resources, Against the Wind #2-2B-32, 810064 (100547)

The following is a step-by-step calculation for the first test run conducted on the Against the
Wind #2-2B-32 810064 (100547).

Test Parameters  Stack Diameter = 8.5 inches  Traverse Points = 16  Ports = 2  Barometric Pressure = 24.90 in Hg  Average O2 = 0.0%  Average CO2 = 12.6%  Load Approximation = 201.0 bhp  Moisture Content = 18.98%

EPA 40 CFR 60(A) Methods 1-3: Determination of Stack Gas Velocity and Flow Rate
Dry Molecular Weight (lb/lbmol) = (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO))
Where: %CO2 – Carbon Dioxide Content Of The Gas = 12.6% %O2 – Oxygen Content Of The Gas = 0.0%
%N2 – Nitrogen Content Of The Gas %CO – Carbon Monoxide Content Of The Gas
(%N2 +%CO) = (100 - %O2 - %CO2) = (100 – 0.0 – 12.6)
= 87.4% Dry
= (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO)) = (0.44 * 12.6) + (0.32 * 0.0) + (0.28 * 87.4)
= 30.02 lb/lbmol
Wet Molecular Weight (lb/lbmol) = MD * (1-BWS) + (18) * BWS
Where: MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 30.02 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 18.98% = MD * (1-BWS) + (18) * BWS
= 30.02 * (1 – (18.98/ 100)) + (18 * (18.98/ 100))
= 27.74 lb/lbmol

Average Stack Gas Velocity (ft/sec)
= Cp * (85.49) * ∆PAVG * (TS / (((PS / 13.6) + PB) * MA))
Where:
CP – Pitot tube constant (unitless) = 0.84 ∆PAVG – Average square root of the stack gas pitot DP (inches water) = 0.438 in H2O
TS – Average stack temperature (R) = 1471 R PB – Barometric pressure (in Hg) = 24.90 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.1 in H2O
MA – Molecular weight of the wet gas (lb/lbmol) = 27.74 lb/lbmol
= Cp * (85.49) * ∆PAVG * (TS / (((PS / 13.6) + PB) * MA))

= 0.84 * (85.49) * 0.438 * ( 1471 / (((0.1/ 13.6) + 24.90) * 27.74))
= 45.85 ft/sec

Average Dry Flowrate (dscfm)
= 60 * (1-BWS) * VS *  * (((DS / 2) / 12))2)* TSTD / TS * (PB + (PS / 13.6)) / 29.92
Where:
DS – Diameter of the stack (inches) = 8.5 inches
BWS – Moisture content of the gas (%) = 18.98%
TSTD – Standard temperature (528R)
TS – Average stack temperature (R) = 1471 R PB – Barometric pressure (in Hg) = 24.90 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.1 in H2O VS– Average Stack gas velocity (ft/sec) = 45.85 ft/sec

= 60 * (1-BWS) * VS *  * (((DS / 2) / 12))2)* TSTD / TS * (PB + (PS / 13.6)) / 29.92

= 60 * (1 - (18.98/ 100)) * 45.85 *  * (((8.5 / 2) / 12))2) * 528 / 1471 * (24.90 + (0.1 /
13.6)) / 29.92

= 262.44 dscfm

Conversion of Dry Flowrate to m3/hr
= Q * 60 * 2.83168*10 -2
Where:
Q – Volumetric Flowrate = 262.44 dscfm
2.83168*10 -2 – Conversion factor for cubic feet to cubic meter 60 – Minutes in an hour

= Q * 60 * 2.83168*10 -2

= 262.44 *60 * 2.83168*10 -2
= 445.882 m3/hr

ASTM D 6348-03: Determination of NOx, CO and VOC Emissions From Stationary Sources
NOx Emission Rate (g/Bhp-hr)
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
Where:
Cd – Measured NOx concentration in ppm = 5.15 ppm
1.92*10 -3 - Conversion constant for ppm to g/m3 NOx
Q – Volumetric Flowrate = 445.882 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 201.0 Bhp
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
= (5.15 * 1.912*10 -3 * 445.882 * 1) / 201.0

= 0.02 g/Bhp-hr

NOx Emission Rate (lbs/hr) = g/Bhp-hr / 454 * Bhp

Where: g/Bhp-hr = 0.02 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 201.0 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.02 / 454 * 201.0

= 0.01 lbs/hr

CO Emission Rate (g/Bhp-hr) = (Cd * 1.164*10 -3 * Q * T) / HP-hr

Where: Cd – Measured CO concentration in ppm = 6.23 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 CO
Q – Volumetric Flowrate = 445.882 m3/hr T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 201.0 Bhp
= (Cd * 1.164*10 -3 * Q * T) / HP-hr

= (6.23 * 1.164*10 -3 * 445.882 * 1) / 201.0
= 0.02 g/Bhp-hr

CO Emission Rate (lbs/hr) = g/Bhp-hr / 454 * Bhp
Where:
g/Bhp-hr = 0.02 g/Bhp-hr 454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 201.0 Bhp
= g/Bhp-hr / 454 * Bhp

= 0.02 / 454 * 201.0
= 0.01 lbs/hr
VOC Emission Rate (g/Bhp-hr) = (Cd * 1.833*10 -3 * Q * T) / HP-hr
Where:
Cd – Measured VOC concentration in ppm = 9.28 ppm 1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – Volumetric Flowrate = 445.882 m3/hr
T – Time in Hours of Test Run = 1 hr HP-hr – Unit Brake Horsepower = 201.0 Bhp

= (Cd * 1.833*10 -3 * Q * T) / HP-hr
= (9.28 * 1.833*10 -3 * 445.882 * 1) / 201.0
= 0.04 g/Bhp-hr
VOC Emission Rate (lbs/hr)
= g/Bhp-hr / 454 * Bhp
Where: g/Bhp-hr = 0.04 g/Bhp-hr
454 – Conversion factor for g to lbs Bhp - Unit Brake Horsepower = 201.0 Bhp

= g/Bhp-hr / 454 * Bhp
= 0.04 / 454 * 201.0
= 0.02 lbs/hr

APPENDIX E

FTIR Engine Test Sheet
Company Name ill
Location / Unit I.D. A."'....:\1;s-t -rnt_ W\il~ *::l:"''d.~\.~)
3xHlr Nt:..,VTvoe of Test Completed
Field Technician (5) David Martinez
Client Rep and/or State Rep Bovtlv
g~"QlI' i\ t.IDate
1:~\~'65Non-Resettable Run Time Hours
WillA lo{e,..sl...:\
---,-~".",_..~.",~.,
Engine Make ~1~(;5"IEngine Model
Engine SIN ~r"'~~ II, S\' l~PPort Distance A a.$of"Port Distance B V.l \\Exhaust Diameter (inches)
ConcentrationCvlinder#Calibration Gas (
NO (ppm) 514.5
CO (ppm)
CC745222
501.8
Propane
CC450607
497.5
N02 (ppm)
ND46380ppm)
144
Ethvlene (ppm)
CC510760
99.97
Methane (ppm)
CC127876
494.5
Acetaldehvde (ppm)
CC471136
XC015587B 199.1
Stack Diagram
. ,."""".",
.;, ..~"",.;",,,
""«,
t t
t
'-­
','.­
T

t
A
1
B
Test 1 Test 2 Test 3
Time of Reading ~,'O5 ato~ to/Ot
Atm Pressure (in Hg) d';. b' TI~l "1 ~"",61
Atm Temp CF) 6~ ~ ]'l:j
Engine RPM \S k\ \~~17 I~ r'f..,,­"'­
*Manifold Pres. Vae(") orJ;~oost(psi»>r Boost (psia) f o O~
Manifold Temp CF) "-..~ 1'1­\\.1.f.\, 1'1~ 1 "0
Psuction (psi) Stage 1 '1Q ~q '~I:
Tsuction CF) Stage 1 ----Pdischarce (nsi) Staae 1 l.\, 1'l""1 QV
Psuction (psi) Stage 2 \ \ \
Tsuction OF) Stage 2 1 I
Pdischarae (osi) Staae 2 ~0"J.. \D '-I ~C(
Psuction (psi) Stage 3 , T
Tsuction CF) Stage 3 I ,
Pdischarae (psi) Staae 3 r &1 \a66 id, 6
Psuction psi) Stage 4
Tsuction CF) Stage 4
Pdischarge (psi) Stage 4
Gas Throughput (mmef/d\ or ( \
Pre Cat Temp CF) t.' (" If ~~ C(£':)
Post Cat Temp CF) IhH' rul (/11 ~
Cat Differential Pres. t" of H2O) n,OL( O/{) Cf o .o»
Humiditv% --, -
02% 0 C <::>
C02 % Drv \"d,b 1'). T Ill./:
LOAD % (Panel) or (Estimated) ---Ignition Timing CF) ~'-\ ";}.£.f a~
AFR Setting m\4l::efrsank) O\\\~ ~,h\'6 t'.~~
AFR Settina -R:uL£Riaht 6.ank) -_. -"--, " .._.­_..
Rev 8
• Some units show boost in inches of Hg. In this situation please indicate if it is
positive (+) or negative(-). Eg: (+12") or (- 5'')
9/17/2019
Worksheet: O2 Stratification
Client:XCL
Location:Against The Wind #2-2B-32
Date:8/21/2024
PD:8.5
DD:24 YES Method 1 Criteria Met
UD:11.5 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 1.41 0.00
A 2 4.25 0.00
A 3 7.08 0.00
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 0.00
Notes: To demonstrate non-stratified flow and utilize one sampling location
O2 may not deviate by more than +/- 0.3% of the average O2 concentration.
EPA REFERENCE METHOD 3A (Determination Of Stratification)
COMPANY NAME:XCL COMPANY LOCATION:Against The Wind #2-2B-32 DATE:8/21/24
STACK DIAMETER (inches):8.5 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:0 AVERAGE O2:0 AVERAGE O2:0
AVERAGE CO2:12.6 AVERAGE CO2:12.6 AVERAGE CO2:12.6
BARO PRESSURE:24.9 BARO PRESSURE:24.9 BARO PRESSURE:24.9
Point Insertion DepthDP (H2O)Ts (deg R)Stat P (H2O)Point Insertion DepthDP (H2O)Ts (deg R)Stat P (H2O)Point Insertion DepthDP (H2O)Ts (deg R)Stat P (H2O)
1 0.5 0.15 1011 0.08 1 0.5 0.14 1012 0.08 1 0.5 0.19 1013 0.09
2 0.8925 0.16 2 0.8925 0.16 2 0.8925 0.21
3 1.649 0.19 3 1.649 0.18 3 1.649 0.23
4 2.7455 0.21 4 2.7455 0.22 4 2.7455 0.25
5 5.7545 0.2 5 5.7545 0.25 5 5.7545 0.29
6 6.851 0.18 6 6.851 0.23 6 6.851 0.26
7 7.6075 0.17 7 7.6075 0.2 7 7.6075 0.23
8 8 0.16 8 8 0.18 8 8 0.21
9 9 9
10 10 10
11 11 11
12 12 12
13 13 13
14 14 14
15 15 15
16 16 16
1 0.5 0.16 1011 0.08 1 0.5 0.15 1012 0.08 1 0.5 0.2 1013 0.09
2 0.8925 0.18 2 0.8925 0.16 2 0.8925 0.21
3 1.649 0.2 3 1.649 0.18 3 1.649 0.24
4 2.7455 0.22 4 2.7455 0.2 4 2.7455 0.26
5 5.7545 0.26 5 5.7545 0.24 5 5.7545 0.3
6 6.851 0.23 6 6.851 0.22 6 6.851 0.27
7 7.6075 0.21 7 7.6075 0.19 7 7.6075 0.25
8 8 0.2 8 8 0.17 8 8 0.22
9 9 9
10 10 10
11 11 11
12 12 12
13 13 13
14 14 14
15 15 15
16 16 16