DAQ-2024-011529

1

DAQC-1140-24
Site ID 101072 (B4)

MEMORANDUM

TO: STACK TEST FILE – XCL ASSETCO, LLC – Taylor 31-3A-22 Pad

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

FROM: Paul Bushman, Environmental Scientist

DATE: November 12, 2024

SUBJECT: Source: One (1) Caterpillar G3516J 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 23, 2024

On October 22, 2024, Utah Division of Air Quality (DAQ) received a test report for one (1) Caterpillar
G3516J engine at Taylor 31-3A-22 Pad, Duchesne County, UT. Testing was performed August 19, 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
Caterpillar
G3516J
SN:
N6W/JEF01675
August 19,
2024
NOx 320 0.36 g/bhp-hr 0.365 g/bhp-hr 1.0 g/bhp-hr
CO 320 0.11 g/bhp-hr 0.108 g/bhp-hr 2.0 g/bhp-hr
VOC 320 0.23 g/bhp-hr 0.227 g/bhp-hr 0.7 g/bhp-hr

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The emissions from the Caterpillar G3516J 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
Taylor 31-3A-22
Duchesne County
Caterpillar G3516J; SN: N6W/JEF01675
Test Date: 8/19/2024
Run #1 2 3 Average
Start Time 14:00 15:01 16:02
Stop Time 15:00 16:01 17:02
Sample Duration (minutes)60 60 60
BHP Engine Load - Actual (bhp) 1242 1242 1242 1242
DS Stack Diameter (inches)14.0 14.0 14.0 14.0PAVG Average (Delta P)½ (" H2O)½0.7990 0.8070 0.7820 0.7960
CP Pitot Tube Constant (unitless)0.84 0.84 0.84 0.84
TS Stack Temperature (°F)823 826 821 824
Pbar Barometric Pressure (" Hg)24.77 24.77 24.77 24.77
Ps Stack Pressure ('' H2O)0.37 0.35 0.36 0.36
O2%vd O2 (%vd)8.9 8.9 8.9 8.9
CO2%vd CO2 (%vd)7.3 7.3 7.2 7.3
N2%vd N2 (%vd)83.8 83.8 83.9 83.8
dry NOX (ppmvd)93.1 95.1 94.6 94.3
dry CO (ppmvd) 45.9 46.0 46.1 46.0
wet NMEOC (ppmvw as C3H8)53.6 53.0 53.5 53.3
Run #1 2 3 Average
Bws Measured Moisture Content (%/100)0.127 0.129 0.129 0.128
Bws Saturated Moisture Content (%/100)466.507 473.266 461.335 467.036
Bws Actual Moisture Content (%/100)0.127 0.129 0.129 0.128
MD Molecular Weight Dry (lb/lb-mole)29.52 29.52 29.51 29.52
MA Molecular Weight Wet (lb/lb-mole)28.06 28.04 28.03 28.05
VS Gas Velocity (ft/sec)77.9 78.8 76.2 77.7
FACFM Gas Flow (acfm)4998 5056 4890 4981
FDSCFM Gas Flow (dscfm)1487 1497 1455 1480
FWSCFM Gas Flow (wscfm)1704 1720 1670 1698
FKWSCFH Gas Flow (kwscfh)102 103 100 102
FKWSCFM Gas Flow (kwscfm)1.704 1.720 1.670 1.698
lb/hr Gas Flow (lb/hr) 7447 7510 7291 7416
Fo Fo (unitless)1.644 1.644 1.667 1.651
wet O2 (%vw)7.8 7.8 7.8 7.8
wet CO2 (%vw)6.4 6.4 6.3 6.3
wet NOX (ppmvw)81.294 82.807 82.426 82.176
15 NOX (ppmvd @ 15% O2)45.779 46.738 46.502 46.340 82.0
lb/hr NOX (lb/hr)0.991 1.019 0.985 0.998
g/bhp-hr NOX (g/bhp-hr)0.362 0.372 0.360 0.365 1.0
wet CO (ppmvw) 40.067 40.036 40.167 40.090
15 CO (ppmvd @ 15% O2)22.563 22.597 22.661 22.607 270.0
lb/hr CO (lb/hr) 0.297 0.300 0.292 0.297
g/bhp-hr CO (g/bhp-hr) 0.109 0.110 0.107 0.108 2.0
dry NMEOC (ppmvd as C3H8)61.370 60.800 61.380 61.183
dry NMEOC (ppmvd as C3H8)61.370 60.800 61.380 61.183
15 NMEOC (ppmvd as C3H8 @ 15% O2)30.174 29.893 30.179 30.082 60.0
lb/hr NMEOC (lb/hr as C3H8)0.626 0.624 0.612 0.621
g/bhp-hr NMEOC (g/bhp-hr as C3H8)0.229 0.228 0.224 0.227 0.7
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1

Source Test Report
For
XCL Resources
Taylor 31-3A-22
Duchesne County, Utah

Test Date: August 19, 2024
Report Date: August 23, 2024

Federal Regulation: EPA 40 CFR 60, Subpart JJJJ
Engine: Caterpillar 3516J
SN: N6W/JEF01675
Unit ID: E130334 (101072)

Prepared By:

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

August 23, 2024

Mr. Ryan Sokolowski
XCL Resources

Dear Mr. Sokolowski:

Re: Engine Emission Testing For XCL Resources, Taylor 31-3A-22, Unit E130334
(101072), EPA 40 CFR 60, Subpart JJJJ.

An air emissions test program was conducted on a Caterpillar 3516J engine, operated by XCL
Resources and designated as Unit E130334 (101072), located at the Taylor 31-3A-22 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 19, 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 0.36 1.0 0.11 2.0 0.23 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)
801 0.8

Engine Load (Averaged Over 3 Test Runs)

Rated BHP Operating BHP % Load
1380 1242.0 90.0

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: Taylor 31-3A-22
Duchesne County, Utah

Emission Source: Caterpillar 3516J
Unit E130334 (101072)

Date of Test: August 19, 2024

Date of Report: August 23, 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 Caterpillar 3516J engine, operated by XCL
Resources and designated as Unit E130334 (101072), located at the Taylor 31-3A-22 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 19, 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 panel load percent reading.

The following key personnel were present during testing:

David Martinez, OEC
John, Archrock

2

2.1 Stack Sampling Location

The facility is currently located in Duchesne County, Utah.

Testing was conducted on the Caterpillar 3516J engine. The sampling port for moisture, NOx,
CO and VOC measurements was approximately 2.0 pipe diameters (28”) downstream from
the nearest flow disturbance (Distance B) and 1.1 pipe diameters (15”) 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

15"
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 19, 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: Caterpillar 3516J, NOx, CO and VOC

The first test was performed from 14:00 to 14:59 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1242.0 bhp, and the average NOx and CO levels were found to be 0.36 g/bhp-hr and
0.11 g/bhp-hr respectively, below limitations. The VOC level tested at 0.23 g/bhp-
hr, which tested in compliance.

3.1.2 Source Test 2: Caterpillar 3516J, NOx, CO and VOC

The second test was performed from 15:01 to 16:00 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1242.0 bhp, and the average NOx and CO levels were found to be 0.37 g/bhp-hr and
0.11 g/bhp-hr respectively, below limitations. The VOC level tested at 0.23 g/bhp-
hr, which tested in compliance.

3.1.3 Source Test 3: Caterpillar 3516J, NOx, CO and VOC

The third test was performed from 16:02 to 17:01 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1242.0 bhp, and the average NOx and CO levels were found to be 0.36 g/bhp-hr and
0.11 g/bhp-hr respectively, below limitations. The VOC level tested at 0.22 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 93.11 0.36 45.89 0.11 61.37 0.23 8.9
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
2 95.06 0.37 45.96 0.11 60.80 0.23 8.9
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
3 94.58 0.36 46.09 0.11 61.38 0.22 8.9
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. 18 March 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 panel load percent reading. 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 88.6%, 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 73.772732 19.5105 93.283232 46.260014 61.856016 12.842558 14:00:00 08/19/2024
2 74.882442 20.1661 95.048542 46.187295 61.483824 12.761993 14:01:00 08/19/2024
3 74.800345 20.234791 95.035136 46.279445 61.355368 12.860835 14:02:00 08/19/2024
4 73.410458 19.535095 92.945553 46.021146 62.026618 12.788679 14:03:00 08/19/2024
5 73.759997 19.630884 93.390881 46.248932 62.040413 12.794351 14:04:01 08/19/2024
6 76.94556 20.885375 97.830935 46.462347 61.455049 12.874514 14:05:01 08/19/2024
7 70.808045 18.515258 89.323303 45.72354 63.040390 12.951186 14:06:01 08/19/2024
8 76.295514 20.270751 96.566265 46.538153 61.663304 12.984682 14:07:01 08/19/2024
9 70.898364 18.450197 89.348561 45.807547 62.930107 12.898557 14:08:01 08/19/2024
10 75.902851 20.201079 96.10393 46.384326 61.461591 12.804429 14:09:01 08/19/2024
11 72.292767 18.981605 91.274372 45.783261 63.047345 12.595393 14:10:01 08/19/2024
12 70.678029 18.421855 89.099884 45.554757 62.348786 12.93424 14:11:02 08/19/2024
13 73.66835 19.314768 92.983118 45.957256 61.342106 13.06932 14:12:02 08/19/2024
14 74.264781 19.489332 93.754113 45.738698 60.232196 12.499978 14:13:02 08/19/2024
15 73.104479 19.300924 92.405403 45.818581 60.607911 12.512463 14:14:02 08/19/2024
16 76.079116 20.699241 96.778357 46.179475 59.688927 12.527818 14:15:02 08/19/2024
17 73.126073 19.94709 93.073163 45.630934 60.234795 13.055131 14:16:02 08/19/2024
18 74.410097 20.602253 95.01235 45.755304 60.002811 12.953804 14:17:03 08/19/2024
19 75.47876 20.84568 96.32444 46.198018 60.350324 12.677346 14:18:03 08/19/2024
20 72.133231 19.62587 91.759101 45.764343 61.384802 12.706092 14:19:03 08/19/2024
21 74.153992 20.295202 94.449194 45.958586 61.060030 12.600216 14:20:03 08/19/2024
22 70.270526 18.803376 89.073902 45.547001 61.671538 12.595126 14:21:03 08/19/2024
23 74.385761 20.244887 94.630648 46.041266 60.236270 12.601358 14:22:03 08/19/2024
24 73.849773 20.042413 93.892186 46.101577 60.798127 12.455948 14:23:03 08/19/2024
25 73.629775 19.983652 93.613427 46.108708 61.067358 12.459628 14:24:04 08/19/2024
26 74.252947 20.262909 94.515856 46.080359 60.919216 12.427003 14:25:04 08/19/2024
27 71.308959 19.402594 90.711553 45.842855 61.966752 12.457601 14:26:04 08/19/2024
28 73.107299 19.888415 92.995714 45.950899 61.315816 12.540226 14:27:04 08/19/2024
29 73.831645 20.305996 94.137641 45.974071 61.197277 12.589554 14:28:04 08/19/2024
30 71.947677 19.672027 91.619704 45.726315 61.525531 13.950094 14:29:04 08/19/2024
31 74.710901 20.584663 95.295564 46.054334 61.301421 13.23306 14:30:04 08/19/2024
32 71.541025 19.499161 91.040186 45.778446 62.377348 12.987831 14:31:05 08/19/2024
33 69.736246 18.904854 88.6411 45.515528 62.028415 13.002718 14:32:05 08/19/2024
34 72.662441 19.806471 92.468912 45.599404 62.149022 12.707772 14:33:05 08/19/2024
35 71.991495 19.159201 91.150696 45.592827 62.357517 12.624005 14:34:05 08/19/2024
36 73.938277 20.166355 94.104632 45.887495 60.958163 12.596121 14:35:05 08/19/2024
37 70.327681 19.075724 89.403405 45.666767 62.205881 12.556292 14:36:05 08/19/2024
38 71.635809 19.478504 91.114313 45.410339 61.546880 12.581129 14:37:06 08/19/2024
39 73.309112 20.005056 93.314168 45.712858 60.883847 12.694699 14:38:06 08/19/2024
40 72.761026 19.770453 92.531479 45.742882 61.413564 12.754199 14:39:06 08/19/2024
41 75.425252 20.99186 96.417112 46.241448 60.269517 12.84512 14:40:06 08/19/2024
42 76.893274 21.37541 98.268684 46.686876 60.104140 12.832834 14:41:06 08/19/2024
43 76.674491 21.22158 97.896071 46.510295 61.430305 12.793796 14:42:06 08/19/2024
44 64.908103 17.296508 82.204611 44.871383 64.837265 12.795597 14:43:06 08/19/2024
45 73.594772 20.067365 93.662137 46.135568 61.699753 12.626766 14:44:07 08/19/2024
46 72.037718 19.805264 91.842982 46.142702 61.548960 12.506772 14:45:07 08/19/2024
47 71.641672 19.944592 91.586264 46.017127 61.356554 12.458107 14:46:07 08/19/2024
48 72.128755 20.057011 92.185766 45.890313 60.666075 12.340062 14:47:07 08/19/2024
49 72.797478 20.051787 92.849265 45.908002 60.408326 12.411046 14:48:07 08/19/2024
50 75.169676 20.646832 95.816508 46.139615 59.505703 13.227565 14:49:07 08/19/2024
51 73.720177 20.471079 94.191256 45.861641 59.491172 13.3493 14:50:07 08/19/2024
52 71.454092 20.160599 91.614691 45.56229 60.220819 13.109093 14:51:08 08/19/2024
53 73.196225 21.156591 94.352816 45.870584 60.662162 12.86899 14:52:08 08/19/2024
54 77.393235 22.834844 100.228079 46.21136 59.824414 13.151933 14:53:08 08/19/2024
55 78.288014 23.269958 101.557972 45.851234 60.358080 12.839594 14:54:08 08/19/2024
56 70.101652 20.477156 90.578808 44.870954 62.943121 11.731741 14:55:08 08/19/2024
57 69.64746 20.350626 89.998086 45.059096 62.931177 11.46212 14:56:08 08/19/2024
58 68.553126 19.904688 88.457814 45.34658 63.086969 11.575144 14:57:09 08/19/2024
59 69.676713 20.087772 89.764485 45.793636 62.221654 11.920443 14:58:09 08/19/2024
60 72.390284 20.887504 93.277788 46.106827 61.322721 11.91432 14:59:09 08/19/2024
AVG 73.10 20.02 93.11 45.89 61.37 12.69
ppm@15% O2 45.78 22.56 30.18
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.36 0.99 0.11 0.30 0.23 0.63
E130334 (101072)
FTIR Measurements
Calculated Emission Levels
XCL Resources
Taylor 31-3A-22
Run 1
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 14 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 0.55 1283 0.37 0.742
Average O2 8.9 (% dry)A 2 1.47 0.59 0.768
Average CO2 7.3 (% dry)A 3 2.72 0.63 0.794
Average N2 + CO 83.8 (% dry)A 4 4.52 0.68 0.825
Dry Molecular Weight 29.52 lb/lbmol A 5 9.48 0.73 0.854
Wet Molecular Weight 28.06 lb/lbmol A 6 11.28 0.69 0.831
EPA REFERENCE METHOD 320 A 7 12.53 0.64 0.800
Barometric Pressure 24.77 in Hg A 8 13.50 0.61 0.781
Moisture Content 12.69 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 93.11 ppm A 11
Calculated NOx Mass Output 0.99 lbs/hr A 12
Calculated NOx Output 0.36 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 45.89 ppm A 15
Calculated CO Mass Output 0.30 lbs/hr A 16
Calculated CO Output 0.11 g/bhp-hr B 1 0.50 0.57 1283 0.37 0.755
EPA REFERENCE METHOD 320 B 2 1.47 0.60 0.775
Average Analyzer NMNEHC Level 61.37 ppm B 3 2.72 0.64 0.800
Calculated NMNEHC Mass Output 0.63 lbs/hr B 4 4.52 0.69 0.831
Calculated NMNEHC Output 0.23 g/bhp-hr B 5 9.48 0.72 0.849
LOAD APPROXIMATION B 6 11.28 0.67 0.819
Estimated Engine Load 1242.0 BHP B 7 12.53 0.63 0.794
B 8 13.50 0.59 0.768
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.6 1283 0.4 0.799
Average Stack Gas Velocity 77.91 ft/sec
Average Dry Flowrate 1488.09 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 74.265473 21.687074 95.952547 46.397762 60.806046 11.878912 15:01:09 08/19/2024
2 72.713429 20.880736 93.594165 45.982899 61.630731 12.382604 15:02:09 08/19/2024
3 74.196731 21.327633 95.524364 46.164837 60.771857 13.363186 15:03:09 08/19/2024
4 73.815965 21.014634 94.830599 46.447955 61.380448 12.999508 15:04:10 08/19/2024
5 74.816462 21.251054 96.067516 46.34474 61.167521 13.022365 15:05:10 08/19/2024
6 76.442958 21.801672 98.24463 46.60887 61.815693 12.961798 15:06:10 08/19/2024
7 70.292764 19.541803 89.834567 45.771139 62.555935 12.891558 15:07:10 08/19/2024
8 74.061129 20.82694 94.888069 46.162409 60.934804 12.802191 15:08:10 08/19/2024
9 73.387691 20.628196 94.015887 46.088872 60.395377 12.977078 15:09:10 08/19/2024
10 74.799248 20.908492 95.70774 46.293744 60.101423 13.192964 15:10:10 08/19/2024
11 76.557914 21.622449 98.180363 46.26046 59.756640 12.908112 15:11:11 08/19/2024
12 74.450426 21.093334 95.54376 46.103843 60.728820 13.198797 15:12:11 08/19/2024
13 74.548004 20.891363 95.439367 45.990572 60.688016 13.022951 15:13:11 08/19/2024
14 73.67027 20.611131 94.281401 45.991912 60.444448 12.782085 15:14:11 08/19/2024
15 75.052574 21.254898 96.307472 46.219341 60.415487 12.996563 15:15:11 08/19/2024
16 76.225851 21.641431 97.867282 46.413788 59.618724 12.929673 15:16:11 08/19/2024
17 72.974781 20.713475 93.688256 45.932696 60.146502 13.400892 15:17:11 08/19/2024
18 78.849436 22.644227 101.493663 46.632767 60.163179 13.334373 15:18:12 08/19/2024
19 70.474557 19.754885 90.229442 45.859734 61.960139 13.057856 15:19:12 08/19/2024
20 74.3629 21.512958 95.875858 46.128351 60.126568 12.869996 15:20:12 08/19/2024
21 72.311322 20.989317 93.300639 45.545211 60.356558 12.800574 15:21:12 08/19/2024
22 73.387276 21.296312 94.683588 45.708282 59.817566 12.811053 15:22:12 08/19/2024
23 74.960708 21.662891 96.623599 45.985699 58.830029 12.67018 15:23:12 08/19/2024
24 74.543896 21.341645 95.885541 45.884681 58.643560 13.197443 15:24:13 08/19/2024
25 77.607692 22.479822 100.087514 46.434904 59.103469 13.078628 15:25:13 08/19/2024
26 75.015159 21.924739 96.939898 46.01493 60.254409 12.681307 15:26:13 08/19/2024
27 74.024777 21.229386 95.254163 45.926755 60.920925 12.521687 15:27:13 08/19/2024
28 75.161366 21.691739 96.853105 46.259175 60.440493 12.49266 15:28:13 08/19/2024
29 74.048534 21.289082 95.337616 45.705902 60.909193 13.582493 15:29:13 08/19/2024
30 74.555982 21.334556 95.890538 45.814849 60.639337 13.660632 15:30:13 08/19/2024
31 74.301286 22.016398 96.317684 45.911385 61.921826 12.96255 15:31:14 08/19/2024
32 71.598202 21.136017 92.734219 45.726313 62.065775 12.418594 15:32:14 08/19/2024
33 74.795464 22.204422 96.999886 46.012212 61.081152 12.450004 15:33:14 08/19/2024
34 70.724588 20.878891 91.603479 45.531431 61.491402 12.741476 15:34:14 08/19/2024
35 71.550339 20.941182 92.491521 45.542772 60.976327 13.020937 15:35:14 08/19/2024
36 73.004269 21.645254 94.649523 45.855001 60.753023 13.009761 15:36:14 08/19/2024
37 73.708678 21.651916 95.360594 45.899815 60.011219 12.667988 15:37:14 08/19/2024
38 72.758603 21.255755 94.014358 45.881431 60.692878 12.559893 15:38:15 08/19/2024
39 73.623466 21.730659 95.354125 45.831037 60.101144 12.562888 15:39:15 08/19/2024
40 74.159174 21.841177 96.000351 46.217851 60.749740 12.829007 15:40:15 08/19/2024
41 74.341892 21.835535 96.177427 46.098323 61.607326 12.505588 15:41:15 08/19/2024
42 74.065218 21.980982 96.0462 46.097161 61.599143 12.56582 15:42:15 08/19/2024
43 73.530488 21.679554 95.210042 45.92736 62.220984 12.465894 15:43:15 08/19/2024
44 66.615359 19.142996 85.758355 44.855343 63.008549 12.425987 15:44:15 08/19/2024
45 72.614582 21.239919 93.854501 45.774338 60.490684 12.510335 15:45:16 08/19/2024
46 73.74235 21.66415 95.4065 45.820302 59.496035 13.209103 15:46:16 08/19/2024
47 72.505617 21.676003 94.18162 45.65472 60.445535 12.945046 15:47:16 08/19/2024
48 74.035164 21.635315 95.670479 45.739729 59.629339 12.545975 15:48:16 08/19/2024
49 73.612341 21.934571 95.546912 45.522509 60.414635 14.778059 15:49:16 08/19/2024
50 75.442774 22.737666 98.18044 46.237398 59.779770 14.464926 15:50:16 08/19/2024
51 70.884663 20.956361 91.841024 45.522296 61.267441 13.280317 15:51:17 08/19/2024
52 75.245166 22.397518 97.642684 46.131419 60.612901 12.722396 15:52:17 08/19/2024
53 75.90732 22.211141 98.118461 46.50392 61.235866 12.630348 15:53:17 08/19/2024
54 75.041218 21.861472 96.90269 46.404287 62.557736 12.957953 15:54:17 08/19/2024
55 72.38192 20.792993 93.174913 45.761039 62.841717 12.561514 15:55:17 08/19/2024
56 73.488778 20.92811 94.416888 45.944152 62.780717 12.602312 15:56:17 08/19/2024
57 66.769684 18.552345 85.322029 45.066399 63.058323 12.558387 15:57:17 08/19/2024
58 75.140115 21.700762 96.840877 45.77079 59.751519 12.646944 15:58:18 08/19/2024
59 72.112641 20.737066 92.849707 45.440562 60.381332 12.711576 15:59:18 08/19/2024
60 74.936378 21.665236 96.601614 45.833863 59.513929 12.642035 16:00:18 08/19/2024
AVG 73.74 21.32 95.06 45.96 60.80 12.89
ppm@15% O2 46.74 22.60 29.89
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.37 1.02 0.11 0.30 0.23 0.62
Calculated Emission Levels
Record Date
XCL Resources
Taylor 31-3A-22
Run 2
E130334 (101072)
FTIR Measurements
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 14 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 0.57 1286 0.35 0.755
Average O2 8.9 (% dry)A 2 1.47 0.59 0.768
Average CO2 7.3 (% dry)A 3 2.72 0.62 0.787
Average N2 + CO 83.8 (% dry)A 4 4.52 0.66 0.812
Dry Molecular Weight 29.52 lb/lbmol A 5 9.48 0.71 0.843
Wet Molecular Weight 28.04 lb/lbmol A 6 11.28 0.70 0.837
EPA REFERENCE METHOD 320 A 7 12.53 0.67 0.819
Barometric Pressure 24.77 in Hg A 8 13.50 0.64 0.800
Moisture Content 12.89 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 95.06 ppm A 11
Calculated NOx Mass Output 1.02 lbs/hr A 12
Calculated NOx Output 0.37 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 45.96 ppm A 15
Calculated CO Mass Output 0.30 lbs/hr A 16
Calculated CO Output 0.11 g/bhp-hr B 1 0.50 0.56 1286 0.35 0.748
EPA REFERENCE METHOD 320 B 2 1.47 0.60 0.775
Average Analyzer NMNEHC Level 60.80 ppm B 3 2.72 0.64 0.800
Calculated NMNEHC Mass Output 0.62 lbs/hr B 4 4.52 0.69 0.831
Calculated NMNEHC Output 0.23 g/bhp-hr B 5 9.48 0.74 0.860
LOAD APPROXIMATION B 6 11.28 0.70 0.837
Estimated Engine Load 1242.0 BHP B 7 12.53 0.68 0.825
B 8 9.50 0.66 0.812
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.7 1286 0.4 0.807
Average Stack Gas Velocity 78.79 ft/sec
Average Dry Flowrate 1497.97 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 75.552103 22.003436 97.555539 46.010395 59.420222 12.541471 16:02:18 08/19/2024
2 73.382661 21.343588 94.726249 45.685807 60.532478 12.505249 16:03:18 08/19/2024
3 75.126706 21.794985 96.921691 45.91094 60.432621 12.900226 16:04:18 08/19/2024
4 75.787825 22.186362 97.974187 46.03064 60.619405 12.564489 16:05:19 08/19/2024
5 75.089767 21.984412 97.074179 45.866939 60.874078 12.377975 16:06:19 08/19/2024
6 75.719815 22.019495 97.73931 46.054295 60.890497 12.345624 16:07:19 08/19/2024
7 74.634932 21.905336 96.540268 46.033836 62.268342 12.311065 16:08:19 08/19/2024
8 69.971908 20.562194 90.534102 45.639126 63.614891 14.36193 16:09:19 08/19/2024
9 70.343001 20.638055 90.981056 45.503804 61.571422 13.489579 16:10:19 08/19/2024
10 72.513452 21.675058 94.18851 45.783132 60.278504 12.952827 16:11:20 08/19/2024
11 71.317552 20.903359 92.220911 45.625708 60.832047 12.818135 16:12:20 08/19/2024
12 75.123962 22.717407 97.841369 45.869317 59.654027 12.967049 16:13:20 08/19/2024
13 74.227634 22.27966 96.507294 45.818939 60.042963 12.587022 16:14:20 08/19/2024
14 73.101227 21.997139 95.098366 45.80358 60.712379 12.504213 16:15:20 08/19/2024
15 73.080947 21.778146 94.859093 45.872489 60.717673 12.506401 16:16:20 08/19/2024
16 73.689927 22.055432 95.745359 45.927189 60.661062 12.502765 16:17:20 08/19/2024
17 75.655169 22.750568 98.405737 46.095521 60.120509 12.852054 16:18:21 08/19/2024
18 73.869376 22.038849 95.908225 46.098258 60.993020 12.772537 16:19:21 08/19/2024
19 75.785495 22.591376 98.376871 46.177478 60.978964 12.793416 16:20:21 08/19/2024
20 74.491163 21.714857 96.20602 46.310548 62.845412 12.716337 16:21:21 08/19/2024
21 70.198195 19.871177 90.069372 45.643848 63.754866 12.683366 16:22:21 08/19/2024
22 72.768835 20.798043 93.566878 46.01571 62.510207 12.709709 16:23:21 08/19/2024
23 70.805973 19.874947 90.68092 45.920295 62.760659 13.167382 16:24:21 08/19/2024
24 71.212733 20.485025 91.697758 46.118633 61.258236 13.449749 16:25:22 08/19/2024
25 72.977656 21.260564 94.23822 46.194402 60.994237 12.84676 16:26:22 08/19/2024
26 71.514382 20.709833 92.224215 45.865894 60.448224 14.058452 16:27:22 08/19/2024
27 75.300302 22.438297 97.738599 46.546631 59.602498 13.17509 16:28:22 08/19/2024
28 73.296737 22.036584 95.333321 46.319366 60.723869 12.697446 16:29:22 08/19/2024
29 76.069568 22.782997 98.852565 46.695674 60.419488 12.564896 16:30:22 08/19/2024
30 71.901681 21.204922 93.106603 46.115408 62.273464 12.691105 16:31:22 08/19/2024
31 74.138326 22.134906 96.273232 46.168494 60.747692 12.687491 16:32:23 08/19/2024
32 71.852607 21.198605 93.051212 46.067262 62.801486 13.160352 16:33:23 08/19/2024
33 70.743987 20.894013 91.638 45.881991 61.744910 13.141188 16:34:23 08/19/2024
34 74.80327 22.270729 97.073999 46.201558 61.352257 12.976476 16:35:23 08/19/2024
35 68.826869 19.941482 88.768351 45.44408 62.240322 13.392894 16:36:23 08/19/2024
36 73.402207 22.004479 95.406686 46.524746 60.231149 12.91117 16:37:23 08/19/2024
37 71.314377 21.112213 92.42659 46.152603 61.498191 12.640696 16:38:24 08/19/2024
38 72.466459 21.288701 93.75516 46.128638 60.635861 12.477929 16:39:24 08/19/2024
39 70.914818 20.769958 91.684776 45.902256 60.963388 12.508017 16:40:24 08/19/2024
40 74.318579 21.956312 96.274891 46.300018 60.038227 13.015905 16:41:24 08/19/2024
41 73.38056 21.469165 94.849725 45.766609 60.020811 13.231309 16:42:24 08/19/2024
42 73.922387 22.012201 95.934588 45.903697 59.621791 13.052279 16:43:24 08/19/2024
43 74.455604 22.62895 97.084554 45.980358 60.015905 12.885381 16:44:24 08/19/2024
44 76.196997 23.450698 99.647695 46.25582 60.520084 12.753397 16:45:25 08/19/2024
45 72.777308 21.835513 94.612821 45.961139 62.754173 12.657472 16:46:25 08/19/2024
46 73.469797 22.087117 95.556914 46.075545 62.544078 12.818895 16:47:25 08/19/2024
47 72.372149 21.750213 94.122362 46.011642 62.302459 12.655122 16:48:25 08/19/2024
48 72.643678 21.555104 94.198782 46.18607 63.584681 12.412963 16:49:25 08/19/2024
49 71.164237 21.241324 92.405561 46.131811 62.857713 12.25291 16:50:25 08/19/2024
50 72.496515 21.868561 94.365076 46.29785 61.430243 13.375147 16:51:25 08/19/2024
51 72.378505 21.868402 94.246907 46.651191 61.243101 13.215992 16:52:26 08/19/2024
52 72.708502 22.147444 94.855946 46.774551 62.054791 12.982579 16:53:26 08/19/2024
53 71.903946 21.760054 93.664 46.506952 62.309073 12.747009 16:54:26 08/19/2024
54 71.052967 21.507733 92.5607 46.421034 62.486242 12.652462 16:55:26 08/19/2024
55 71.648288 21.545885 93.194173 46.441187 62.506828 12.353888 16:56:26 08/19/2024
56 73.741199 22.148314 95.889513 46.51508 61.396000 13.463547 16:57:26 08/19/2024
57 72.675627 21.721002 94.396629 46.768956 63.982288 12.809364 16:58:26 08/19/2024
58 68.366454 19.989848 88.356302 45.831653 63.440860 13.044145 16:59:27 08/19/2024
59 71.407352 21.233451 92.640803 46.193744 61.201736 12.814162 17:00:27 08/19/2024
60 71.750862 21.392183 93.143045 46.104921 61.176250 12.751269 17:01:27 08/19/2024
AVG 72.96 21.62 94.58 46.09 61.38 12.85
ppm@15% O2 46.50 22.66 30.18
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.36 0.98 0.11 0.29 0.22 0.61
FTIR Measurements
E130334 (101072)
Calculated Emission Levels
XCL Resources
Taylor 31-3A-22
Run 3
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 14 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 0.54 1281 0.36 0.735
Average O2 8.9 (% dry)A 2 1.47 0.59 0.768
Average CO2 7.2 (% dry)A 3 2.72 0.63 0.794
Average N2 + CO 83.9 (% dry)A 4 4.52 0.68 0.825
Dry Molecular Weight 29.51 lb/lbmol A 5 9.48 0.73 0.854
Wet Molecular Weight 28.03 lb/lbmol A 6 11.28 0.71 0.843
EPA REFERENCE METHOD 320 A 7 12.53 0.70 0.837
Barometric Pressure 24.77 in Hg A 8 13.50 0.69 0.831
Moisture Content 12.85 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 94.58 ppm A 11
Calculated NOx Mass Output 0.98 lbs/hr A 12
Calculated NOx Output 0.36 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 46.09 ppm A 15
Calculated CO Mass Output 0.29 lbs/hr A 16
Calculated CO Output 0.11 g/bhp-hr B 1 0.50 0.58 1281 0.36 0.762
EPA REFERENCE METHOD 320 B 2 1.47 0.55 0.742
Average Analyzer NMNEHC Level 61.38 ppm B 3 2.72 0.62 0.787
Calculated NMNEHC Mass Output 0.61 lbs/hr B 4 4.52 0.67 0.819
Calculated NMNEHC Output 0.22 g/bhp-hr B 5 9.48 0.70 0.837
LOAD APPROXIMATION B 6 11.28 0.68 0.825
Estimated Engine Load 1242.0 BHP B 7 12.53 0.65 0.806
B 8 13.50 0.20 0.447
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.6 1281 0.4 0.782
Average Stack Gas Velocity 76.22 ft/sec
Average Dry Flowrate 1455.41 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)8/19/2024 13:36:16 -0.040306 0.047718 -0.008014 -0.037436 -0.202712 0.41909 0.103392 -0.083413 -0.083406 0.000549 0.007412 0.007411 0.013723 191.009888 0.9939348/19/2024 13:36:23 0.119637 -0.01763 -0.00662 0.004903 -0.02906 -0.145853 0.23029 -0.1075 -0.107493 0.003677 0.102007 0.102 -0.003289 191.009888 0.9954818/19/2024 13:36:31 0.03175 0.023103 -0.008618 -0.047292 -0.249882 -0.125194 0.327608 -0.142432 -0.142419 0.005057 0.054852 0.054848 -0.00961 191.009888 0.984456
8/19/2024 13:36:38 0.001393 0.029656 -0.00754 0.038924 -0.327545 -0.305965 0.055236 -0.17036 -0.170347 0.006682 0.031049 0.031046 -0.003413 191.009888 0.9941858/19/2024 13:37:15 0 0 0 0 0 0 0 0 0 0 0 0 0 191.007645 0.997069
8/19/2024 13:37:28 -0.008418 0.007384 -0.000916 -0.036631 0.348275 -0.154407 0.115468 0.08985 0.089849 0.000861 -0.001034 -0.001034 0.012369 190.927246 0.995768/19/2024 13:37:36 -0.114861 -0.019754 0.001936 -0.039277 0.532209 0.26009 -0.096406 0.020702 0.020703 0.006926 -0.134615 -0.134617 0.004244 190.927246 1.0013618/19/2024 13:37:43 0.086364 -0.00779 -0.001754 -0.068893 0.20685 -0.083482 0.487707 0.063439 0.063438 0.004152 0.078574 0.078573 -0.000675 190.927246 0.9991968/19/2024 13:37:51 -0.063812 -0.018359 0.000405 -0.058581 0.265067 0.293047 0.238003 0.004432 0.004432 -0.00024 -0.082171 -0.082171 0.017282 190.927246 0.9962848/19/2024 13:37:58 -0.028661 0.013344 -0.002092 -0.044546 0.338405 0.471839 0.549789 -0.017324 -0.017324 0.001869 -0.015317 -0.015317 0.036049 190.927246 0.9905888/19/2024 13:38:06 -0.020289 0.02637 -0.000033 0.003322 0.145434 -0.033572 0.314094 -0.033462 -0.033462 0.000496 0.006081 0.006081 0.002191 190.927246 0.9933398/19/2024 13:38:13 0.041629 -0.018025 -0.001165 -0.021537 0.243684 0.186216 -0.030803 0.139898 0.139896 -0.002962 0.023604 0.023604 0.00372 190.927246 0.9922
8/19/2024 13:38:21 0.065669 0.007855 -0.001977 -0.000345 0.413693 -0.003193 0.109794 -0.103144 -0.103142 0.002103 0.073524 0.073522 0.002505 190.932007 0.999658/19/2024 13:38:28 0.036485 -0.020875 -0.001086 -0.05153 0.127135 0.148721 0.137298 -0.003698 -0.003697 0.003137 0.01561 0.01561 0.007381 190.987183 0.997366
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)8/19/2024 13:39:03 497.233054 512.188016 501.411096 191.00354 0.989191 8/19/2024 13:42:12 99.364089 190.984467 0.9901738/19/2024 13:39:10 502.462473 516.657482 508.565027 191.00354 0.991627 8/19/2024 13:42:20 99.397186 190.984467 0.98947
8/19/2024 13:39:18 500.451045 514.947397 505.456408 191.00354 0.996055 8/19/2024 13:42:27 98.612555 190.984467 0.9968938/19/2024 13:39:25 499.802736 514.761447 505.444348 191.00354 0.991993 8/19/2024 13:42:35 99.441935 190.984467 0.9895638/19/2024 13:39:33 501.60859 515.305061 504.657092 191.00354 1.002377 8/19/2024 13:42:42 99.474174 190.984467 0.9958578/19/2024 13:39:41 501.111575 515.115161 505.729674 191.00354 1.003056 8/19/2024 13:42:50 99.02994 190.984467 0.9960898/19/2024 13:39:48 502.095723 516.152566 506.955456 191.00354 1.001634 8/19/2024 13:42:57 100.054265 190.984467 0.9904248/19/2024 13:39:56 500.334224 515.643115 506.702564 191.00354 0.996008 8/19/2024 13:43:05 100.127829 190.984467 0.992558/19/2024 13:40:03 497.63824 513.289202 505.713391 190.99173 0.989277 8/19/2024 13:43:12 99.096787 190.984467 0.995585
8/19/2024 13:40:11 498.440757 514.020768 506.164442 190.908173 0.99259 8/19/2024 13:43:20 99.413148 190.951874 0.997813
Date Time NO2 191C span Temp ( C )Pressure (atm)8/19/2024 13:40:38 143.921579 190.968033 0.9939748/19/2024 13:40:46 145.409227 190.984467 0.9980778/19/2024 13:40:53 145.873928 190.984467 1.001513
8/19/2024 13:41:01 145.621553 190.984467 0.9986188/19/2024 13:41:08 146.037712 190.984467 0.9991218/19/2024 13:41:16 146.873455 190.984467 0.9959528/19/2024 13:41:23 146.311685 190.984467 0.997768/19/2024 13:41:31 147.45225 190.984467 0.9844168/19/2024 13:41:38 147.467528 190.984467 0.9869178/19/2024 13:41:46 146.400608 190.984467 0.993717
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)8/19/2024 13:43:48 175.773787 201.871036 157.140406 190.968567 0.972337 8/19/2024 13:47:27 98.969753 190.95903 0.980388/19/2024 13:43:56 415.507425 434.962675 422.739926 190.971741 0.971119 8/19/2024 13:47:34 99.191416 190.95903 0.9791388/19/2024 13:44:03 417.533176 437.605948 426.599414 190.971741 0.970057 8/19/2024 13:47:42 99.326289 190.95903 0.9776458/19/2024 13:44:11 423.708919 443.210922 432.611705 190.971741 0.966032 8/19/2024 13:47:49 99.210124 190.95903 0.9837
8/19/2024 13:44:18 422.540866 442.182853 433.242333 190.971741 0.966443 8/19/2024 13:47:57 97.945158 190.95903 1.0066328/19/2024 13:44:26 433.348443 451.125029 434.670379 190.971741 0.982368 8/19/2024 13:48:04 99.447866 190.95903 1.006137
8/19/2024 13:44:33 499.572554 513.658214 502.571855 190.985367 0.996815 8/19/2024 13:48:12 99.762871 190.95903 1.0046838/19/2024 13:44:41 500.943804 515.990284 505.940484 191.039291 0.990226 8/19/2024 13:48:19 99.665487 190.95903 1.0063418/19/2024 13:44:48 502.325548 515.996974 506.856253 191.048035 0.998519 8/19/2024 13:48:27 98.6452 190.95903 1.0055588/19/2024 13:44:56 499.045459 513.648334 506.162371 191.048035 0.999296 8/19/2024 13:48:34 99.053639 190.95993 1.001052
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)8/19/2024 13:48:57 0.037557 0.24629 0.07983 0.589229 191.035324 0.9975358/19/2024 13:49:04 -0.04395 -0.017871 -0.116984 0.535723 191.035324 0.992098/19/2024 13:49:12 0.05874 0.061661 0.156149 0.550746 191.035324 0.9952328/19/2024 13:49:19 0.009595 -0.039011 0.026478 0.487125 191.035324 0.9860598/19/2024 13:49:27 0.081599 0.137811 0.295507 0.27126 191.035324 0.994931
8/19/2024 13:49:34 -0.001804 -0.101505 0.148336 0.265262 191.035324 0.9911678/19/2024 13:49:42 0.106748 0.050718 0.212808 -0.06075 191.035324 0.991434
8/19/2024 13:49:50 0.128809 0.080264 -0.228 0.190311 191.035324 0.987645
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)
8/19/2024 13:54:46 6.360071 40.2403 190.939423 0.9809148/19/2024 13:54:54 6.410017 39.514455 190.939957 0.9761018/19/2024 13:55:01 6.342835 40.430691 190.939957 0.9802318/19/2024 13:55:09 6.381799 40.034552 190.939957 0.9762388/19/2024 13:55:16 6.364214 40.900341 190.939957 0.983468/19/2024 13:55:54 6.390122 41.19406 190.939957 0.9790498/19/2024 13:56:01 5.193493 110.433195 190.939957 0.970251
8/19/2024 13:56:09 3.055116 263.208692 190.95108 0.9949898/19/2024 13:56:16 3.451986 233.652944 190.979919 0.9977768/19/2024 13:56:24 5.898604 75.64337 191.022614 0.9904058/19/2024 13:56:31 5.987356 66.373769 191.022614 0.9960338/19/2024 13:56:39 5.980278 67.474494 191.022614 0.9973518/19/2024 13:56:46 5.891982 79.0112 191.022614 0.9822168/19/2024 13:56:54 5.611064 97.029242 191.022614 0.984606
8/19/2024 13:57:01 5.647169 96.773603 191.022614 0.9808338/19/2024 13:57:09 5.61253 97.194511 191.022614 0.990485
8/19/2024 13:57:16 5.709146 94.839052 191.022614 0.990128/19/2024 13:57:24 5.841566 80.491905 191.022614 0.9947338/19/2024 13:57:31 5.832298 81.992941 191.022614 0.9940018/19/2024 13:57:39 5.779192 85.45554 191.022614 0.9900958/19/2024 13:58:09 5.806556 83.248581 191.022614 0.984469
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)8/19/2024 17:10:41 497.564938 507.726204 497.401679 190.997177 1.008847 8/19/2024 17:08:51 98.826337 191.016251 1.0095068/19/2024 17:10:49 501.000329 513.67513 503.593942 191.002625 1.013663 8/19/2024 17:08:59 98.983499 191.016251 1.0188158/19/2024 17:10:56 504.111698 515.835865 503.071165 191.07074 1.01736 8/19/2024 17:09:06 99.592332 191.016251 1.0116328/19/2024 17:11:04 503.765327 517.701596 507.700243 191.079834 1.007594 8/19/2024 17:09:14 99.442807 191.016251 1.014188
8/19/2024 17:11:12 506.116239 518.220114 508.363748 191.078247 1.009648 8/19/2024 17:09:21 99.429403 191.016251 1.0095428/19/2024 17:11:19 498.880311 512.423418 500.933002 191.018066 1.016712 8/19/2024 17:09:29 99.974153 191.016251 1.014426
8/19/2024 17:11:27 504.897771 517.593913 505.434591 190.984467 1.006751 8/19/2024 17:09:36 99.119368 191.016251 1.0157198/19/2024 17:11:34 504.591215 516.80182 502.009591 190.984467 1.011242 8/19/2024 17:09:44 99.423456 191.016251 1.0155568/19/2024 17:11:42 500.118819 512.706532 499.574224 190.984467 1.016302 8/19/2024 17:09:51 99.002191 191.014435 1.0194058/19/2024 17:11:49 507.825818 520.042467 505.273302 190.984467 1.007491 8/19/2024 17:09:59 99.258241 190.942673 1.01091
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)8/19/2024 17:09:06 -0.035795 -0.09206 -0.033513 191.016251 1.011632 8/19/2024 17:12:35 -0.101565 191.06076 1.0129268/19/2024 17:09:14 -0.120348 -0.093417 0.254976 191.016251 1.014188 8/19/2024 17:12:42 -0.162118 191.06076 1.0215098/19/2024 17:09:21 -0.015818 -0.124513 0.183653 191.016251 1.009542 8/19/2024 17:12:50 -0.11359 191.06076 1.0142778/19/2024 17:09:29 -0.171364 -0.061745 0.237602 191.016251 1.014426 8/19/2024 17:12:57 0.029173 191.06076 1.0200918/19/2024 17:09:36 -0.088968 -0.064275 0.09403 191.016251 1.015719 8/19/2024 17:13:05 -0.456507 191.06076 1.01784
8/19/2024 17:09:44 -0.154159 -0.053837 0.289426 191.016251 1.015556 8/19/2024 17:13:12 -0.595513 191.06076 1.0178518/19/2024 17:09:51 0.016145 -0.103742 0.145516 191.014435 1.019405 8/19/2024 17:13:20 0.039564 191.06076 1.0115
8/19/2024 17:09:59 -0.181368 -0.111814 0.456069 190.942673 1.01091 8/19/2024 17:13:27 -0.53454 191.052811 1.015604
POST SYSTEM ZERO
SAMPLE SPIKE RECOVERY
POST SYSTEM CAL
PRE TEST 1 497.5 6.4 40.4 5.7 88.6 0.098 88.6%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 514.0 514.5 0.0 -0.09 0.00
CO 498.4 501.8 0.0 -0.67 0.00
Propane 506.2 497.5 0.1 1.74 0.02
Ethylene 99.4 99.76 0.3 -0.35 0.31
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 513.6 514.5 0.0 -0.17 0.01
CO 499.0 501.8 0.0 -0.55 0.01
Propane 506.2 497.5 0.1 1.74 0.02
Ethylene*99.1 99.76 0.4 -0.71 0.38
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 520.0 514.5 -0.1 1.08 -0.02 1.24 0.03
CO 507.8 501.8 -0.1 1.20 -0.02 1.75 0.02
Propane 505.3 497.5 0.2 1.56 0.03 0.18 0.01
Ethylene*99.3 99.76 -0.2 -0.50 -0.16 0.21 0.54
*CTS Scans are conducted with Ethylene through the sample line.
% Recovery
Propane
PRE DIRECT CAL
FTIR QA/QC SUMMARY
SAMPLE RECOVERY CALCULATIONS
Period Spike #Concentration of
Propane Cylinder
Stack CO2
Concentration
Stack Propane
Concentration
Stack + Spike CO2
Concentration
Stack + Propane
Concentration
DF
Calculated
POST SYSTEM CAL
PRE SYSTEM CAL
XCL - Taylor 31-3A-22
8-19-24
XCL - Taylor 31-3A-22
8-19-24
XCL - Taylor 31-3A-22
8-19-24

Spectral Fit
Run 1

Spectral Fit
Run 2
Spectral Fit
Run 3

Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000147.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\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000068.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000069.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000070.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000071.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000072.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000073.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000074.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_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 61.48 2.17 -0.24 0.32 2.95 2.95 -1.24 --0-2795 1.03 Good
NO2 191C 17.52 0.47 -0.03 0.03 0.49 0.49 -0.35 --0-488 1.01 Good
N2O 191C 0.11 0.24 0.14 0.03 0.03 0.27 0.27 0.16 0.21 0.02 0.05 0-200 -Close to DL
NH3 TE 191C -8.45 34.32 8.53 4.14 7.06 58.59 58.59 9.91 30.16 1.39 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C13.11 0.31 -0.02 0.03 0.5 0.5 -0.26 --0-40 -Good
FORMALDEHYDE 191C7.36 0.77 7.62 0.24 0.27 0.87 0.87 8.47 8.47 0.85 2.54 0-69 -Close to DL
FORMIC ACID 191C TE1.76 12.88 1.97 1.56 1.83 15.08 15.08 2.12 11.33 0.15 0.66 0-466 -Close to DL
CH4 2900 CM-1 191C793.27 26.39 -1.64 2.38 48.81 48.81 -15.9 --0-3143 0.97 Good
PROPANE 191C 38.51 1.6 -0.22 0.27 1.92 1.92 -0.8 --0-4976 0.95 Good
PROPYLENE 191C TE0.73 12.71 1.07 1.57 1.86 15.03 15.03 1.35 11.14 0.29 0.36 0-194 -Close to DL
ETHANE 191C 88.63 3.33 -0.55 0.85 5.18 5.18 -1.78 --0-1004 -Good
ETHYLENE 191C TE8.99 22.33 9.49 2.07 2.55 27.54 27.54 10.92 20.05 1.44 3.16 0-900 -Close to DL
CO PPM 191C (1OF2)39.55 1.19 -0.25 0.55 2.46 2.46 -0.79 --0-5010 1.01 Good
CO2% 191C 6.34 0.14 -0.01 0.02 0.19 0.19 -0.13 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C0.72 1.93 0.76 0.63 0.81 2.47 2.47 1.02 1.29 0.26 0.25 0-186 1 Close to DL
ACETYLENE 191C0.32 3.03 0.45 0.79 1.05 4 4 0.61 2.27 0.16 0.15 0-1016 -Close to DL
SO2 191C 1.74 3.49 2.32 0.26 0.32 4.25 4.25 2.54 3.22 0.22 0.77 0-964 1.02 Close to DL
HEXANE 191C 4.06 1.02 4.35 0.13 0.18 1.38 1.38 4.84 4.85 0.49 1.45 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000208.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\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000068.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000069.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000070.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000071.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000072.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000073.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000074.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_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 65.12 2.21 -0.24 0.32 3.01 3.01 -1.3 --0-2795 1.03 Good
NO2 191C 19.55 0.48 -0.03 0.03 0.51 0.51 -0.39 --0-488 1.01 Good
N2O 191C 0.1 0.22 0.14 0.03 0.03 0.25 0.25 0.16 0.2 0.02 0.05 0-200 -Close to DL
NH3 TE 191C -6.11 29.37 8.53 4.14 7.06 50.13 50.13 9.91 25.27 1.39 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C12.72 0.29 -0.02 0.03 0.47 0.47 -0.25 --0-40 -Good
FORMALDEHYDE 191C7.76 0.73 7.62 0.24 0.27 0.84 0.84 8.47 8.47 0.85 2.54 0-69 -Close to DL
FORMIC ACID 191C TE2.26 12.16 1.97 1.56 1.83 14.24 14.24 2.12 10.59 0.15 0.66 0-466 -Close to DL
CH4 2900 CM-1 191C780.18 25.44 -1.64 2.38 47.06 47.06 -15.61 --0-3143 0.97 Good
PROPANE 191C 38.17 1.49 -0.22 0.27 1.78 1.78 -0.77 --0-4976 0.95 Good
PROPYLENE 191C TE0.94 12.06 1.07 1.57 1.86 14.26 14.26 1.35 10.48 0.29 0.36 0-194 -Close to DL
ETHANE 191C 87.76 3.14 -0.55 0.85 4.88 4.88 -1.76 --0-1004 -Good
ETHYLENE 191C TE10.42 21.19 9.49 2.07 2.55 26.14 26.14 10.92 18.88 1.44 3.16 0-900 -Close to DL
CO PPM 191C (1OF2)40.23 1.19 -0.25 0.55 2.47 2.47 -0.8 --0-5010 1.01 Good
CO2% 191C 6.39 0.13 -0.01 0.02 0.18 0.18 -0.13 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C1.23 1.77 0.76 0.63 0.81 2.27 2.27 1.02 1.12 0.26 0.25 0-186 1 Close to DL
ACETYLENE 191C0.36 2.82 0.45 0.79 1.05 3.73 3.73 0.61 2.06 0.16 0.15 0-1016 -Close to DL
SO2 191C 1.57 3.28 2.32 0.26 0.32 4 4 2.54 3.02 0.22 0.77 0-964 1.02 Close to DL
HEXANE 191C 4.06 0.96 4.35 0.13 0.18 1.3 1.3 4.84 4.85 0.49 1.45 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000269.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\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000068.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000069.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000070.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000071.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000072.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000073.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_000074.LAB
C:\OLT\Data\XCL Resources\Taylor 1675 8-19-24!\XCL TAYLOR 1675 8-19-24!_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 62.68 2.2 -0.24 0.32 2.99 2.99 -1.26 --0-2795 1.03 Good
NO2 191C 19.27 0.43 -0.03 0.03 0.45 0.45 -0.39 --0-488 1.01 Good
N2O 191C 0.11 0.22 0.14 0.03 0.03 0.25 0.25 0.16 0.19 0.02 0.05 0-200 -Close to DL
NH3 TE 191C -6.47 31.96 8.53 4.14 7.06 54.56 54.56 9.91 27.85 1.39 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C12.98 0.29 -0.02 0.03 0.47 0.47 -0.26 --0-40 -Good
FORMALDEHYDE 191C7.52 0.78 7.62 0.24 0.27 0.88 0.88 8.47 8.47 0.85 2.54 0-69 -Close to DL
FORMIC ACID 191C TE1.88 12.78 1.97 1.56 1.83 14.96 14.96 2.12 11.22 0.15 0.66 0-466 -Close to DL
CH4 2900 CM-1 191C771.73 25.81 -1.64 2.38 47.74 47.74 -15.47 --0-3143 0.97 Good
PROPANE 191C 39.24 1.6 -0.22 0.27 1.92 1.92 -0.81 --0-4976 0.95 Good
PROPYLENE 191C TE0.61 12.57 1.07 1.57 1.86 14.87 14.87 1.35 11 0.29 0.36 0-194 -Close to DL
ETHANE 191C 88 3.34 -0.55 0.85 5.2 5.2 -1.77 --0-1004 -Good
ETHYLENE 191C TE9.8 21.54 9.49 2.07 2.55 26.57 26.57 10.92 19.24 1.44 3.16 0-900 -Close to DL
CO PPM 191C (1OF2)40.67 1.21 -0.25 0.55 2.51 2.51 -0.81 --0-5010 1.01 Good
CO2% 191C 6.39 0.13 -0.01 0.02 0.18 0.18 -0.13 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C0.87 2 0.76 0.63 0.81 2.56 2.56 1.02 1.35 0.26 0.25 0-186 1 Close to DL
ACETYLENE 191C0.44 2.91 0.45 0.79 1.05 3.85 3.85 0.61 2.15 0.16 0.15 0-1016 -Close to DL
SO2 191C 1.53 3.29 2.32 0.26 0.32 4.01 4.01 2.54 3.03 0.22 0.77 0-964 1.02 Close to DL
HEXANE 191C 4.28 1.01 4.35 0.13 0.18 1.37 1.37 4.84 4.85 0.49 1.45 0-1000 -Close to DL

APPENDIX C

Test Run Load %Site Rated Load, bhp Load Approx., bhp
1 90 1380 1242.0
2 90 1380 1242.0
3 90 1380 1242.0
Engine Load Approximation based on Panel Levels

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 1488.09 1242.0 8.9 93.11 0.36 0.99 45.89 0.11 0.30 61.37 0.23 0.63 12.69
2 1497.97 1242.0 8.9 95.06 0.37 1.02 45.96 0.11 0.30 60.80 0.23 0.62 12.89
3 1455.41 1242.0 8.9 94.58 0.36 0.98 46.09 0.11 0.29 61.38 0.22 0.61 12.85
1242.0 8.9 94.25 0.36 1.00 45.98 0.11 0.30 61.18 0.23 0.62 12.81
Summary
Average Levels
Example Calculations: XCL Resources, Taylor 31-3A-22, E130334 (101072)

The following is a step-by-step calculation for the first test run conducted on the Taylor 31-3A-
22 E130334 (101072).

Test Parameters  Stack Diameter = 14 inches  Traverse Points = 16  Ports = 2  Barometric Pressure = 24.77 in Hg  Average O2 = 8.9%  Average CO2 = 7.3%  Load Approximation = 1242.0 bhp  Moisture Content = 12.69%

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 = 7.3% %O2 – Oxygen Content Of The Gas = 8.9%
%N2 – Nitrogen Content Of The Gas %CO – Carbon Monoxide Content Of The Gas
(%N2 +%CO) = (100 - %O2 - %CO2) = (100 – 8.9 – 7.3)
= 83.8% Dry
= (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO)) = (0.44 * 7.3) + (0.32 * 8.9) + (0.28 * 83.8)
= 29.52 lb/lbmol
Wet Molecular Weight (lb/lbmol) = MD * (1-BWS) + (18) * BWS
Where: MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 29.52 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 12.69% = MD * (1-BWS) + (18) * BWS
= 29.52 * (1 – (12.69/ 100)) + (18 * (12.69/ 100))
= 28.06 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) = 0.799 in H2O
TS – Average stack temperature (R) = 1283 R PB – Barometric pressure (in Hg) = 24.77 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.4 in H2O
MA – Molecular weight of the wet gas (lb/lbmol) = 28.06 lb/lbmol
= Cp * (85.49) * ∆PAVG * (TS / (((PS / 13.6) + PB) * MA))

= 0.84 * (85.49) * 0.799 * ( 1283 / (((0.4/ 13.6) + 24.77) * 28.06))
= 77.91 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) = 14 inches
BWS – Moisture content of the gas (%) = 12.69%
TSTD – Standard temperature (528R)
TS – Average stack temperature (R) = 1283 R PB – Barometric pressure (in Hg) = 24.77 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.4 in H2O VS– Average Stack gas velocity (ft/sec) = 77.91 ft/sec

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

= 60 * (1 - (12.69/ 100)) * 77.91 *  * (((14 / 2) / 12))2) * 528 / 1283 * (24.77 + (0.4 /
13.6)) / 29.92

= 1488.09 dscfm

Conversion of Dry Flowrate to m3/hr
= Q * 60 * 2.83168*10 -2
Where:
Q – Volumetric Flowrate = 1488.09 dscfm
2.83168*10 -2 – Conversion factor for cubic feet to cubic meter 60 – Minutes in an hour

= Q * 60 * 2.83168*10 -2

= 1488.09 *60 * 2.83168*10 -2
= 2528.28 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 = 93.11 ppm
1.92*10 -3 - Conversion constant for ppm to g/m3 NOx
Q – Volumetric Flowrate = 2528.28 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1242.0 Bhp
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
= (93.11 * 1.912*10 -3 * 2528.28 * 1) / 1242.0

= 0.36 g/Bhp-hr

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

Where: g/Bhp-hr = 0.36 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1242.0 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.36 / 454 * 1242.0

= 0.99 lbs/hr

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

Where: Cd – Measured CO concentration in ppm = 45.89 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 CO
Q – Volumetric Flowrate = 2528.28 m3/hr T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1242.0 Bhp
= (Cd * 1.164*10 -3 * Q * T) / HP-hr

= (45.89 * 1.164*10 -3 * 2528.28 * 1) / 1242.0
= 0.11 g/Bhp-hr

CO Emission Rate (lbs/hr) = g/Bhp-hr / 454 * Bhp
Where:
g/Bhp-hr = 0.11 g/Bhp-hr 454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1242.0 Bhp
= g/Bhp-hr / 454 * Bhp

= 0.11 / 454 * 1242.0
= 0.30 lbs/hr
VOC Emission Rate (g/Bhp-hr) = (Cd * 1.833*10 -3 * Q * T) / HP-hr
Where:
Cd – Measured VOC concentration in ppm = 61.37 ppm 1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – Volumetric Flowrate = 2528.28 m3/hr
T – Time in Hours of Test Run = 1 hr HP-hr – Unit Brake Horsepower = 1242.0 Bhp

= (Cd * 1.833*10 -3 * Q * T) / HP-hr
= (61.37 * 1.833*10 -3 * 2528.28 * 1) / 1242.0
= 0.23 g/Bhp-hr
VOC Emission Rate (lbs/hr)
= g/Bhp-hr / 454 * Bhp
Where: g/Bhp-hr = 0.23 g/Bhp-hr
454 – Conversion factor for g to lbs Bhp - Unit Brake Horsepower = 1242.0 Bhp

= g/Bhp-hr / 454 * Bhp
= 0.23 / 454 * 1242.0
= 0.63 lbs/hr

APPENDIX E

FTIR Engine Test Sheet
Company Name 7t.L
Location / Unit 1.0. r~.,... ~l ~sA ~~t\ \b/~
3x1hr /VLV
David Martinez
:\,J".... -Art-L
~-Iq~dq
Type of Test Completed
Field Technician (s)
Client Rep and/or State Rep
Date
Stack Diagram
Engine Make
\OS')\Non-Resettable Run Time Hours
CA'I
-,,,,,,,,., ,m,,,Enqlne Model t.3~1 c:\
-r"E-J: C7 I6/."Enqine SIN 'I',w,,....·,·.·,·,···.·.•··•··•····· .....,.."...."""."."
Port Distance A
Port Distance B '\,:Exhaust Diameter (inches)
Calibration Gas ·r"""eConcentrationCvlinder#
514.5
CO (ppm
CC745222NO (ppm
CC450607 501.8
Propane 497.5
N02 (ppm)
ND46380'ppm)
144CC51 0760 l!-ti t .CC127876 99.97
Methane (ppm
Ethylene ppm
CC471136 494.5 I~~~~J
199.1XC015587BAcetaldehvde 'opm)
««<<'<'<"<<<<­
'T

t
A
1
B
Test 1 Test 2 Test 3
Time of Readinq
Atm Pressure (in HQ) A'-/.I...,~ LI. 7)
Atm Temp CF)
Engine RPM .

*Manifold Pres. Vac(") or BOost(psi}!'or Boost (psia)

Manifold Temp ('F) ~
\).." ,f., 131
Psuction (psi) Stage 1 "75l
Tsuction OF Staoe 1

Pdischarae (psi) Staae 1
,~ n\d-.\
Psuction (psi) StaQe 2 l\ 1 TITsuction CF staae 2

Pdischar e (psi) Staqe 2

Psuction psi) Staae 3
\ I
I I

Pdischar e (psi) Staae 3

Psuction (psi) Stage 4

Tsuction OF) StaQe 4

Pdischarge (psi) StaQe 4

Tsuction 'F) Staae 3
i
Gas Throuohout (mmcf/d\ or l m F J:

Pre Cat Temp ('F)

Post Cat Temp CF)

Cat Differential Pres. (" of H20)

Humidity%

02%

C02%Dry ~
.7;3
LOAD %APanetl or (Estimated) Cfn
IQnitionnmii'ir.f CF
.A~nk)AFR Setting '""'

AFR Settin!:J v
---.,"
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:Taylor #31-3A-22A 1675
Date:8/19/2024
PD:14
DD:28 YES Method 1 Criteria Met
UD:15 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 2.32 8.90
A 2 7.00 8.90
A 3 11.66 8.90
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 8.90
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:Taylor #31-3A-22A 1675 DATE:8/19/24
STACK DIAMETER (inches):14 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:8.9 AVERAGE O2:8.9 AVERAGE O2:8.9
AVERAGE CO2:AVERAGE CO2:AVERAGE CO2:
BARO PRESSURE:BARO PRESSURE:BARO PRESSURE:
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 0.55 823 0.37 1 0.5 0.57 826 0.35 1 0.5 0.54 821 0.36
2 1.47 0.59 2 1.47 0.59 2 1.47 0.59
3 2.716 0.63 3 2.716 0.62 3 2.716 0.63
4 4.522 0.68 4 4.522 0.66 4 4.522 0.68
5 9.478 0.73 5 9.478 0.71 5 9.478 0.73
6 11.284 0.69 6 11.284 0.7 6 11.284 0.71
7 12.53 0.64 7 12.53 0.67 7 12.53 0.7
8 13.5 0.61 8 13.5 0.64 8 13.5 0.69
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 0.57 823 0.37 1 0.5 0.56 826 0.35 1 0.5 0.58 821 0.36
2 1.47 0.6 2 1.47 0.6 2 1.47 0.55
3 2.716 0.64 3 2.716 0.64 3 2.716 0.62
4 4.522 0.69 4 4.522 0.69 4 4.522 0.67
5 9.478 0.72 5 9.478 0.74 5 9.478 0.7
6 11.284 0.67 6 11.284 0.7 6 11.284 0.68
7 12.53 0.63 7 12.53 0.68 7 12.53 0.65
8 13.5 0.59 8 13.5 0.66 8 13.5 0.2
9 9 9
10 10 10
11 11 11
12 12 12
13 13 13
14 14 14
15 15 15
16 16 16