DAQ-2024-012026

1

DAQC-1221-24
CAERS ID 11679 (B4)

MEMORANDUM

TO: STACK TEST FILE – SCOUT ENERGY MANAGEMENT, LLC – Ashley
Compressor Station

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

FROM: Paul Bushman, Environmental Scientist

DATE: December 10, 2024

SUBJECT: Source: One (1) Caterpillar G3516J engine; Unit C-4
Contact: Chris Breitling: 469-485-3418
Location: Duchesne County, UT
Test Contractor: Great Plains Analytical Services, Inc.
Permit/AO#: Approval Order DAQE-116790009-15, dated February 9, 2015
Action Code: TR
Subject: Review of stack test report dated November 25, 2024

On December 9, 2024, DAQ received a test report for the above listed unit at Ashley Compressor Station
in Duchesne County, UT. Testing was performed November 13, 2024, to demonstrate compliance with
the emission limits found in condition II.B.4.c of Approval Order DAQE-AN116790009-15, and 40 CFR
Part 60, Subpart JJJJ. The calculated test results are:

Source Test Date Test
Method Pollutant Tester
Results DAQ Results Limits
Caterpillar
G3516J
Unit C-4
SN:
N6W/JEF03271
November
13, 2024 RM320
NOx
0.50 g/hp-hr 0.498 g/hp-hr 1.00 g/hp-hr
1.22 lb/hr 1.217 lb/hr 3.04 lb/hr
CO
0.02 g/hp-hr 0.024 g/hp-hr 2.00 g/hp-hr
0.06 lb/hr 0.059 lb/hr 0.85 lb/hr
VOC
0.26 g/hp-hr 0.264 g/hp-hr 0.7 g/hp-hr
0.65 lb/hr 0.646 lb/hr 2.13 lb/hr

2

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The emissions from the above unit should be considered to have
been in compliance with the emission limits of the AO and 40
CFR 60 subpart JJJJ during testing.

ATTACHMENTS: DAQ stack test review Excel Spreadsheets, Scout Energy
Management, LLC stack test report
Emissions
Scout Energy Management, LLC
Ashley Compressor Compressor Station
Duchesne County, Utah
Caterpillar G3516J SN: N6W/JEF03271 Unit C-4
Test Date: 11/13/2024
Run #1 2 3 Average
Start Time 9:45 10:46 11:46
Stop Time 10:45 11:46 12:46
Sample Duration (minutes)60 60 60
BHP Engine Load (hp) 1104 1118 1104 1109
DS Stack Diameter (inches)16.0 16.0 16.0 16.0PAVG Average (Delta P)½ (" H2O)½0.8680 0.9140 0.9340 0.9053
CP Pitot Tube Constant (unitless)0.84 0.84 0.84 0.84
TS Stack Temperature (°F)587 591 598 592
Pbar Barometric Pressure (mbar)845 845 844 845
Pbar Barometric Pressure (" Hg)24.22 24.22 24.23 24.22
Ps Stack Pressure ('' H2O)0.46 0.48 0.49 0.48
O2%vd O2 (%vd)8.2 8.3 8.3 8.3
CO2%vd CO2 (%vd)7.1 7.1 7.1 7.1
N2%vd N2 (%vd)84.7 84.6 84.6 84.6
dry NOX (ppmvd)72.4 68.3 69.1 69.9
dry CO (ppmvd) 5.5 5.6 5.5 5.5
wet TVOC (ppmvw as C3H8)34.0 34.6 34.3 34.3
Run #1 2 3 Average
Bws Measured Moisture Content (%/100)0.118 0.113 0.115 0.115
Bws Saturated Moisture Content (%/100)116.912 120.409 126.665 121.329
Bws Actual Moisture Content (%/100)0.118 0.113 0.115 0.115
MD Molecular Weight Dry (lb/lb-mole)29.46 29.47 29.47 29.47
MA Molecular Weight Wet (lb/lb-mole)28.12 28.17 28.15 28.15
VS Gas Velocity (ft/sec)77.2 81.4 83.5 80.7
FACFM Gas Flow (acfm)6471 6821 6994 6762
FDSCFM Gas Flow (dscfm)2332 2460 2503 2432
FWSCFM Gas Flow (wscfm)2645 2777 2830 2750
FKWSCFH Gas Flow (kwscfh)159 167 170 165
FKWSCFM Gas Flow (kwscfm)3 3 3 3
lb/hr Gas Flow (lb/hr) 11579 12181 12405 12055
Fo Fo (unitless)1.789 1.775 1.775 1.779
wet O2 (%vw)7.2 7.4 7.3 7.3
wet CO2 (%vw)6.3 6.3 6.3 6.3
wet NOX (ppmvw)63.834 60.590 61.173 61.866
15 NOX (ppmvd @ 15% O2)33.611 32.000 32.370 32.661
lb/hr NOX (lb/hr)1.208 1.204 1.239 1.217 4.18
g/bhp-hr NOX (g/bhp-hr)0.496 0.488 0.509 0.498 1.00
wet CO (ppmvw) 4.879 4.921 4.885 4.895
15 CO (ppmvd @ 15% O2)2.569 2.599 2.585 2.584
lb/hr CO (lb/hr) 0.056 0.060 0.060 0.059 0.37
g/bhp-hr CO (g/bhp-hr)0.023 0.024 0.025 0.024 2.00
dry TVOC (ppmvd as C3H8)38.500 38.970 38.710 38.727
15 TVOC (ppmvd as C3H8 @ 15% O2)42.138 42.991 42.704 42.611
lb/hr TVOC (lb/hr as C3H8)0.616 0.658 0.664 0.646 0.8
g/bhp-hr TVOC (g/bhp-hr as C3H8)0.253 0.267 0.273 0.264 0.7
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1
Source Test Report
For
Scout Energy Management, LLC
Ashley Compressor Station
Duchesne County, Utah
Test Date: November 13, 2024
Report Date: November 25, 2024
Federal Regulation: EPA 40 CFR 60, Subpart JJJJ
UDEQ Approval Order: #DAQE-AN116790009-15
Engine: Caterpillar G3516J
SN: N6W/JEF03271
Unit ID: C-4
Prepared By:
Oasis Emission Consultants, Inc.
2730 Commercial Way
Rock Springs, WY 82901
November 25, 2024
Mr. Chris Breitling
Scout Energy Management, LLC
13800 Montfort Drive
Dallas, TX 75240
Dear Mr. Breitling:
Re: Engine Emission Testing For Scout Energy Management, LLC, Ashley
Compressor Station, Unit C-4, Approval Order #DAQE-AN116790009-15.
An air emissions test program was conducted on a Caterpillar G3516J engine, operated by
Scout Energy Management, LLC and designated as Unit C-4, located at the Ashley
Compressor Station in Duchesne County, Utah. The purpose of the testing was to
demonstrate ongoing compliance with the emissions limits contained in UDEQ Approval
Order #DAQE-AN116790009-15 and 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 November 13, 2024.
UDEQ Approval Order #DAQE-AN116790009-15 Emission Levels
The average recorded levels were found to comply with emission levels stipulated in the
Approval Order, as shown in the attached report and summarized below.
Emission
Unit
Avg
NOx
Permit
NOx
Avg
CO
Permit
CO
Avg
NMNEHC*
Avg
VOC
g/bhp-hr 0.50 --0.02 --0.26 --
lbs/hr 1.22 3.04 0.06 0.85 0.65 2.13
*VOC levels reported as non-methane, non-ethane hydrocarbon on a propane basis (NMNEHC C3).
EPA 40 CFR 60, Subpart JJJJ Emission Levels
Emission
Unit
Avg
NOx
Permit
NOx
Avg
CO
Permit
CO
Avg
NMNEHC*
Permit
VOC
g/bhp-hr 0.50 1.0 0.02 2.0 0.26 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)
617 1.5
Engine Load (Averaged Over 3 Test Runs)
Rated BHP Operating
BHP
% Load
1380 1108.6 80.3
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 & 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 Crystal Leonard
Manager of Technical Services Senior EHS Specialist
_________________________
Christopher N. Knott, P.Eng.
Director, Engineering and Operations
SOURCE EMISSION TEST REPORT
Federal Regulation: EPA 40 CFR 60, Subpart JJJJ
UDEQ Approval Order #DAQE-AN116790009-15
Test Performed By:Oasis Emission Consultants, Inc.
Test Company Contact:Chris Knott
2730 Commercial Way
Rock Springs, WY 82901
307.382.3297
Owner/Operator:Scout Energy Management, LLC
Owner/Operator Contact: Chris Breitling
13800 Montfort Drive
Dallas, TX 75240
Facility Name:Ashley Compressor Station
Section 14, Township 9S, Range 15E
Duchesne County, Utah
Emission Source:Caterpillar G3516J
Unit C-4
Date of Test:November 13, 2024
Date of Report:November 25, 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 G3516J engine, operated by
Scout Energy Management, LLC and designated as Unit C-4, located at the Ashley
Compressor Station in Duchesne County, Utah. The purpose of the testing was to
demonstrate ongoing compliance with the emissions limits contained in UDEQ Approval
Order #DAQE-AN116790009-15 and 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 located in the SW¼ NE¼ of Section 14, T9S, R15E, in Duchesne County,
Utah.
Latitude: 40.03559059 Longitude: -110.1895763
Three one hour test runs were performed on November 13, 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 & 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:
Jordan Nix, OEC
Austin B.
2
2.1 Stack Sampling Location
The facility is located in the SW¼ NE¼ of Section 14, T9S, R15E, in Duchesne County,
Utah.
Latitude: 40.03559059 Longitude: -110.1895763
Testing was conducted on the Caterpillar G3516J engine. The sampling port for moisture,
NOx, CO and VOC measurements was approximately 4.5 pipe diameters (72”) downstream
from the nearest flow disturbance (Distance B) and 12.5 pipe diameters (200”) 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.
Figure 1 - Sample Port Location
16"
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 November 13, 2024 to analyze exhaust NOx, CO
and VOC (NMNEHC C3) emission levels to demonstrate ongoing compliance with the
emissions limits contained in the UDEQ Approval Order #DAQE-AN116790009-15 and
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 G3516J, NOx, CO and VOC
The first test was performed from 9:45 to 10:45 for NOx, CO and VOC.
Based on operating parameters recorded during testing, the load was approximated at
1104.0 bhp, and the average NOx and CO levels were found to be 1.21 lbs/hr and
0.06 lbs/hr respectively, below limitations. The VOC level tested at 0.62 lbs/hr,
which tested in compliance.
3.1.2 Source Test 2: Caterpillar G3516J, NOx, CO and VOC
The second test was performed from 10:46 to 11:45 for NOx, CO and VOC.
Based on operating parameters recorded during testing, the load was approximated at
1117.8 bhp, and the average NOx and CO levels were found to be 1.20 lbs/hr and
0.06 lbs/hr respectively, below limitations. The VOC level tested at 0.66 lbs/hr,
which tested in compliance.
3.1.3 Source Test 3: Caterpillar G3516J, NOx, CO and VOC
The third test was performed from 11:46 to 12:45 for NOx, CO and VOC.
Based on operating parameters recorded during testing, the load was approximated at
1104.0 bhp, and the average NOx and CO levels were found to be 1.24 lbs/hr and
0.06 lbs/hr respectively, below limitations. The VOC level tested at 0.67 lbs/hr,
which tested in compliance.
Test
Run
NOx(ppmvd)
NOx(lbs/hr)
CO
(ppmvd)
CO
(lbs-hr)
VOC
(ppmvd)
VOC
(lbs-hr)
O2
(%)
1 72.35 1.21 5.53 0.06 38.50 0.62 8.2
Test
Run
NOx
(ppmvd)
NOx
(lbs/hr)
CO
(ppmvd)
CO
(lbs-hr)
VOC
(ppmvd)
VOC
(lbs-hr)
O2
(%)
2 68.34 1.20 5.55 0.06 38.97 0.66 8.3
Test
Run
NOx(ppmvd)
NOx(lbs/hr)
CO
(ppmvd)
CO
(lbs-hr)
VOC
(ppmvd)
VOC
(lbs-hr)
O2
(%)
3 69.13 1.24 5.52 0.06 38.71 0.67 8.3
5
4.1 Stack Sampling Methods and Procedures
Testing followed EPA 40 CFR 60(A) Methods 1-3 & 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). 9 July 2024. Web. 25 November 2024.
<https://www.epa.gov/emc/emc-promulgated-test-methods>.
ASTM International. “Standards & Publications.” All Environment Standards.
Web. 25 November 2024. <https://www.astm.org/Standards/D6348.htm>.
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 & 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) Enerac 500 Portable O2/CO2 Analyzer
• (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
The engine operating parameters were used 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 76.8%, 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 47.485654 28.15384 75.639494 6.088673 36.747482 12.29509 9:45:06 11-13-2024
2 47.320976 28.031106 75.352081 5.874964 36.127928 12.201529 9:46:06 11-13-2024
3 47.464404 28.114067 75.578471 5.847715 36.273362 11.802677 9:47:06 11-13-2024
4 48.42438 28.44532 76.8697 5.799696 36.222057 11.305372 9:48:06 11-13-2024
5 47.01168 27.77609 74.787769 5.72816 36.729859 11.146569 9:49:06 11-13-2024
6 48.374416 28.431289 76.805706 5.733818 36.589129 11.166625 9:50:06 11-13-2024
7 48.934169 28.693757 77.627927 5.676151 36.344648 11.080886 9:51:06 11-13-2024
8 50.164861 29.375844 79.540705 5.680111 36.592496 11.14784 9:52:06 11-13-2024
9 46.285239 27.071779 73.357018 5.744085 36.758548 11.374621 9:53:06 11-13-2024
10 52.26346 30.488625 82.752086 5.695207 35.487722 11.204583 9:54:07 11-13-2024
11 49.413053 28.768418 78.18147 5.565378 36.664614 11.328765 9:55:07 11-13-2024
12 49.782282 28.959786 78.742068 5.580382 36.464631 11.186301 9:56:07 11-13-2024
13 45.397538 26.644442 72.04198 5.581226 36.960567 12.615115 9:57:07 11-13-2024
14 52.93279 30.827128 83.759919 5.57103 35.449102 13.408594 9:58:07 11-13-2024
15 54.185322 31.644867 85.830188 5.506165 36.078620 11.244894 9:59:07 11-13-2024
16 54.281832 31.820439 86.102272 5.589107 38.438107 11.454995 10:00:07 11-13-2024
17 50.825365 29.898444 80.723809 5.386981 40.208790 11.958584 10:01:07 11-13-2024
18 51.392541 30.22407 81.616611 5.603799 39.426719 13.791426 10:02:07 11-13-2024
19 52.196924 30.883091 83.080015 5.397823 38.449599 13.034033 10:03:07 11-13-2024
20 51.638678 30.55879 82.197468 5.416613 38.288321 11.580927 10:04:08 11-13-2024
21 48.571928 28.803464 77.375392 5.502033 39.006925 11.609789 10:05:07 11-13-2024
22 46.450187 27.510081 73.960268 5.445735 39.265926 11.79306 10:06:08 11-13-2024
23 43.040254 25.593217 68.633471 5.39656 39.278598 11.644284 10:07:08 11-13-2024
24 46.673162 27.676783 74.349945 5.344313 38.833073 11.682513 10:08:08 11-13-2024
25 42.368561 25.295062 67.663622 5.37812 39.748640 11.602115 10:09:08 11-13-2024
26 42.566877 25.578355 68.145232 5.355692 39.573961 11.31681 10:10:08 11-13-2024
27 43.208864 25.814446 69.02331 5.291284 39.056501 11.363627 10:11:08 11-13-2024
28 39.221383 23.239597 62.46098 5.307462 41.178724 11.214188 10:12:08 11-13-2024
29 44.872934 26.488007 71.360941 5.386956 38.799757 11.2717 10:13:08 11-13-2024
30 41.304092 24.471538 65.775631 5.347839 39.438082 11.187437 10:14:08 11-13-2024
31 43.264391 25.564182 68.828573 5.410477 39.745653 11.098475 10:15:08 11-13-2024
32 45.386238 27.02507 72.411309 5.356142 38.213313 10.659825 10:16:09 11-13-2024
33 46.629659 27.708985 74.338643 5.328546 38.954644 11.213204 10:18:20 11-13-2024
34 43.230925 25.967742 69.198667 5.286112 39.504116 11.376055 10:19:20 11-13-2024
35 44.288727 26.370376 70.659102 5.394176 39.013347 11.319093 10:20:20 11-13-2024
36 42.666594 25.554296 68.22089 5.335641 39.590920 11.37658 10:21:21 11-13-2024
37 43.900065 26.288874 70.188939 5.347575 38.760965 11.314343 10:22:21 11-13-2024
38 39.464809 23.438774 62.903582 5.420254 40.280560 11.236017 10:23:21 11-13-2024
39 43.828329 25.893023 69.721352 5.429922 38.729592 11.339105 10:24:21 11-13-2024
40 43.206957 25.550043 68.757001 5.407716 39.210051 11.370336 10:25:21 11-13-2024
41 42.117845 24.963813 67.081658 5.486856 38.852018 11.552832 10:26:21 11-13-2024
42 43.440447 25.509265 68.949712 5.46975 39.062331 11.613837 10:27:21 11-13-2024
43 43.727403 25.673194 69.400596 5.504846 39.915769 11.937665 10:28:21 11-13-2024
44 42.239558 24.75711 66.996668 5.563262 39.479320 11.358387 10:29:21 11-13-2024
45 43.101907 25.283174 68.385082 5.509534 38.790647 11.731931 10:30:21 11-13-2024
46 42.905099 25.102589 68.007688 5.504927 39.098619 11.76762 10:31:22 11-13-2024
47 43.209469 25.170412 68.379881 5.51364 39.471232 11.775957 10:32:22 11-13-2024
48 41.810355 24.584236 66.394591 5.483289 39.552818 11.958663 10:33:22 11-13-2024
49 43.848323 25.491682 69.340004 5.574198 38.969352 12.186401 10:34:22 11-13-2024
50 43.787756 25.469961 69.257718 5.541514 38.445578 12.38879 10:35:22 11-13-2024
51 42.944931 25.095286 68.040216 5.6018 39.094568 12.511877 10:36:22 11-13-2024
52 42.894495 25.033221 67.927716 5.52164 39.210182 12.625734 10:37:22 11-13-2024
53 43.955311 25.557296 69.512606 5.69569 39.295669 12.670001 10:38:22 11-13-2024
54 43.171683 25.17313 68.344812 5.629976 39.623258 12.888772 10:39:22 11-13-2024
55 43.148327 25.036047 68.184374 5.577368 38.621813 13.088589 10:40:23 11-13-2024
56 43.542092 25.204595 68.746687 5.590469 39.530232 12.923772 10:41:23 11-13-2024
57 43.812807 25.439472 69.252279 5.658703 39.414805 12.563981 10:42:23 11-13-2024
58 42.268258 24.679653 66.947911 5.543254 39.179056 12.146455 10:43:22 11-13-2024
59 43.286685 25.248167 68.534852 5.668768 38.900495 11.714678 10:44:23 11-13-2024
60 43.569545 25.375339 68.944884 5.559921 38.918043 11.340466 10:45:23 11-13-2024
AVG 45.55 26.81 72.35 5.53 38.50 11.77
ppm@15% O2 33.61 2.57 17.89
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.50 1.21 0.02 0.06 0.25 0.62
C-4
FTIR Measurements
Calculated Emission Levels
Scout Energy Management, LLC
Ashley Compressor Station
Run 1
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 16 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 0.51 0.58 1047 0.46 0.762
Average O2 8.2 (% dry)A 2 1.68 0.65 0.806
Average CO2 7.1 (% dry)A 3 3.10 0.66 0.812
Average N2 + CO 84.7 (% dry)A 4 5.17 0.67 0.819
Dry Molecular Weight 29.46 lb/lbmol A 5 10.83 0.70 0.837Wet Molecular Weight 28.11 lb/lbmol A 6 12.90 0.78 0.883
EPA REFERENCE METHOD 320 A 7 14.32 0.82 0.906
Barometric Pressure 24.22 in Hg A 8 15.49 0.78 0.883
Moisture Content 11.77 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 72.35 ppm A 11
Calculated NOx Mass Output 1.21 lbs/hr A 12
Calculated NOx Output 0.50 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 5.53 ppm A 15
Calculated CO Mass Output 0.06 lbs/hr A 16
Calculated CO Output 0.02 g/bhp-hr B 1 0.51 0.80 1047 0.46 0.894
EPA REFERENCE METHOD 320 B 2 1.68 0.69 0.831
Average Analyzer NMNEHC Level 38.50 ppm B 3 3.10 0.71 0.843
Calculated NMNEHC Mass Output 0.62 lbs/hr B 4 5.17 0.74 0.860Calculated NMNEHC Output 0.25 g/bhp-hr B 5 10.83 0.86 0.927
LOAD APPROXIMATION B 6 12.90 0.97 0.985
Estimated Engine Load 1104.0 BHP B 7 14.32 0.87 0.933
B 8 15.49 0.82 0.906
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16Averages 0.8 1047 0.5 0.868
Average Stack Gas Velocity 77.23 ft/sec
Average Dry Flowrate 2333.51 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 43.230619 25.037749 68.268368 5.667294 40.090678 11.254193 10:46:23 11-13-2024
2 42.232314 24.594806 66.82712 5.545091 39.480688 11.316057 10:47:23 11-13-2024
3 42.875128 24.733413 67.608541 5.681455 38.673714 11.30403 10:48:23 11-13-2024
4 43.637507 25.153774 68.791281 5.652096 38.863530 11.527763 10:49:23 11-13-2024
5 43.506341 25.034845 68.541186 5.612511 39.057089 11.821077 10:50:23 11-13-2024
6 42.459226 24.626704 67.08593 5.599772 39.258961 12.141181 10:51:24 11-13-2024
7 43.94876 25.259524 69.208284 5.576822 38.567573 11.832376 10:52:23 11-13-2024
8 43.680747 25.194077 68.874825 5.584366 38.862458 11.159933 10:53:23 11-13-2024
9 42.554152 24.494248 67.0484 5.544581 38.853994 10.830255 10:54:23 11-13-2024
10 43.295463 25.035864 68.331327 5.584229 39.042503 10.889248 10:55:24 11-13-2024
11 43.69448 25.313774 69.008254 5.576626 38.617653 11.282615 10:56:24 11-13-2024
12 43.507016 25.167893 68.674909 5.686562 39.022245 11.875534 10:57:24 11-13-2024
13 42.425896 24.631277 67.057173 5.560775 38.794002 11.064151 10:58:24 11-13-2024
14 42.984658 25.04743 68.032088 5.630109 38.739027 10.29856 10:59:24 11-13-2024
15 43.554398 25.310095 68.864493 5.630502 39.073644 10.466459 11:00:24 11-13-2024
16 42.568313 24.806167 67.37448 5.520477 39.029816 11.136131 11:01:24 11-13-2024
17 43.505857 25.345436 68.851293 5.645317 39.088261 10.88203 11:02:24 11-13-2024
18 43.609642 25.380797 68.990438 5.564442 39.601230 10.901911 11:03:24 11-13-2024
19 42.601641 24.769741 67.371382 5.582502 39.758252 11.199185 11:04:24 11-13-2024
20 42.998223 24.965306 67.963529 5.663519 39.076295 11.895562 11:05:24 11-13-2024
21 43.801022 25.565083 69.366105 5.660297 38.919573 11.535895 11:06:24 11-13-2024
22 43.192509 25.136625 68.329134 5.562331 39.493298 11.172184 11:07:25 11-13-2024
23 42.99765 25.036155 68.033805 5.609908 38.278846 10.800483 11:08:25 11-13-2024
24 43.700617 25.401547 69.102164 5.540893 39.146774 10.959735 11:09:25 11-13-2024
25 43.512357 25.348361 68.860718 5.533184 39.180076 10.992497 11:10:25 11-13-2024
26 42.768125 25.016101 67.784225 5.539632 38.571059 11.744671 11:11:25 11-13-2024
27 42.838274 25.173659 68.011932 5.640546 38.213278 11.390578 11:12:25 11-13-2024
28 43.461386 25.42313 68.884516 5.603305 38.398470 11.214339 11:13:25 11-13-2024
29 43.434139 25.262785 68.696924 5.609806 39.443882 10.880275 11:14:25 11-13-2024
30 42.747405 24.839628 67.587033 5.539099 39.245632 10.999622 11:15:26 11-13-2024
31 43.223164 25.121676 68.34484 5.599092 39.525282 11.167462 11:16:25 11-13-2024
32 43.125116 25.129652 68.254768 5.568211 39.471542 11.232559 11:17:26 11-13-2024
33 42.308368 24.678639 66.987007 5.530014 39.676889 11.37647 11:18:26 11-13-2024
34 42.767717 24.909358 67.677075 5.492635 38.454596 11.391361 11:19:26 11-13-2024
35 43.976335 25.627943 69.604278 5.503203 38.279078 11.906787 11:20:26 11-13-2024
36 43.611905 25.477656 69.08956 5.421813 38.828953 12.330148 11:21:26 11-13-2024
37 43.387845 25.219944 68.607789 5.576736 39.017741 12.578375 11:22:26 11-13-2024
38 43.117745 25.129153 68.246898 5.503147 37.824822 11.518848 11:23:26 11-13-2024
39 43.522423 25.507304 69.029726 5.4611 38.840586 11.492146 11:24:26 11-13-2024
40 42.722828 24.778182 67.50101 5.576344 38.187029 12.023089 11:25:26 11-13-2024
41 44.0749 25.630797 69.705697 5.493336 38.321348 12.048445 11:26:26 11-13-2024
42 43.493724 25.236001 68.729725 5.585014 38.517298 12.036627 11:27:26 11-13-2024
43 42.997466 24.979013 67.976479 5.508642 38.286166 11.440763 11:28:26 11-13-2024
44 42.359526 24.902103 67.261629 5.500828 39.100697 11.219806 11:29:26 11-13-2024
45 43.888693 25.739886 69.628579 5.512862 39.021240 10.940268 11:30:27 11-13-2024
46 43.96752 25.695884 69.663404 5.446941 39.136593 10.606899 11:31:27 11-13-2024
47 42.1819 24.727591 66.909492 5.428217 38.921917 10.773374 11:32:27 11-13-2024
48 43.299395 25.301113 68.600508 5.459272 38.478098 11.196941 11:33:27 11-13-2024
49 43.712261 25.546006 69.258267 5.531293 38.599796 12.012639 11:34:27 11-13-2024
50 42.919262 25.127484 68.046745 5.494018 38.794633 11.245413 11:35:27 11-13-2024
51 43.305704 25.356004 68.661708 5.521796 39.218773 10.475055 11:36:27 11-13-2024
52 43.687021 25.483516 69.170537 5.442474 39.565436 10.178476 11:37:27 11-13-2024
53 42.723548 25.050707 67.774256 5.51408 39.214050 10.13098 11:38:28 11-13-2024
54 42.637227 24.90528 67.542507 5.520091 39.346289 11.268932 11:39:27 11-13-2024
55 43.847746 25.683741 69.531486 5.455486 38.891803 11.574021 11:40:28 11-13-2024
56 42.775858 25.0801 67.855959 5.433848 39.207131 11.944771 11:41:28 11-13-2024
57 42.951821 25.078981 68.030801 5.441238 38.913291 11.911393 11:42:28 11-13-2024
58 43.510357 25.481424 68.99178 5.554646 39.514452 11.608682 11:43:28 11-13-2024
59 43.188744 25.088501 68.277246 5.363836 39.756409 11.854268 11:44:28 11-13-2024
60 43.058296 25.013425 68.071721 5.54189 38.830507 12.13643 11:45:28 11-13-2024
AVG 43.19 25.15 68.34 5.55 38.97 11.34
ppm@15% O2 32.00 2.60 18.25
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.49 1.20 0.02 0.06 0.27 0.66
Calculated Emission Levels
Record Date
Scout Energy Management, LLC
Ashley Compressor Station
Run 2
C-4
FTIR Measurements
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 16 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 0.51 0.76 1051 0.48 0.872
Average O2 8.3 (% dry)A 2 1.68 0.69 0.831
Average CO2 7.1 (% dry)A 3 3.10 0.66 0.812
Average N2 + CO 84.6 (% dry)A 4 5.17 0.74 0.860
Dry Molecular Weight 29.47 lb/lbmol A 5 10.83 1.01 1.005Wet Molecular Weight 28.17 lb/lbmol A 6 12.90 1.00 1.000
EPA REFERENCE METHOD 320 A 7 14.32 0.94 0.970
Barometric Pressure 24.22 in Hg A 8 15.49 0.91 0.954
Moisture Content 11.34 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 68.34 ppm A 11
Calculated NOx Mass Output 1.20 lbs/hr A 12
Calculated NOx Output 0.49 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 5.55 ppm A 15
Calculated CO Mass Output 0.06 lbs/hr A 16
Calculated CO Output 0.02 g/bhp-hr B 1 0.51 0.67 1051 0.48 0.819
EPA REFERENCE METHOD 320 B 2 1.68 0.69 0.831
Average Analyzer NMNEHC Level 38.97 ppm B 3 3.10 0.78 0.883
Calculated NMNEHC Mass Output 0.66 lbs/hr B 4 5.17 0.91 0.954Calculated NMNEHC Output 0.27 g/bhp-hr B 5 10.83 0.95 0.975
LOAD APPROXIMATION B 6 12.90 0.94 0.970
Estimated Engine Load 1117.8 BHP B 7 14.32 0.90 0.949
B 8 15.49 0.88 0.938
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16Averages 0.8 1051 0.5 0.914
Average Stack Gas Velocity 81.39 ft/sec
Average Dry Flowrate 2462.03 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 43.977372 25.537274 69.514646 5.401701 39.199898 12.466705 11:46:28 11-13-2024
2 43.205188 25.314602 68.51979 5.455109 39.351627 12.498811 11:47:28 11-13-2024
3 42.410697 24.752239 67.162936 5.395029 38.608681 12.113906 11:48:28 11-13-2024
4 43.899418 25.601627 69.501045 5.505337 38.692104 11.898815 11:49:28 11-13-2024
5 43.610353 25.346498 68.956851 5.564663 38.913104 11.913871 11:50:28 11-13-2024
6 42.104197 24.806656 66.910854 5.493428 39.161943 11.773929 11:51:28 11-13-2024
7 43.944877 25.781543 69.726419 5.507375 38.211738 11.416282 11:52:29 11-13-2024
8 43.421734 25.393935 68.815669 5.384199 38.768303 10.956672 11:53:29 11-13-2024
9 42.78677 25.046087 67.832856 5.435662 39.456415 11.063481 11:54:29 11-13-2024
10 43.109262 25.194574 68.303837 5.461798 38.715971 11.027227 11:55:29 11-13-2024
11 43.258486 25.262729 68.521215 5.412341 39.267806 10.884189 11:56:29 11-13-2024
12 43.673852 25.603398 69.27725 5.453089 38.702808 10.595468 11:57:29 11-13-2024
13 42.420338 25.002965 67.423304 5.499417 38.862314 10.691385 11:58:29 11-13-2024
14 43.803394 25.828588 69.631982 5.47232 38.451368 10.639728 11:59:29 11-13-2024
15 43.654474 25.685838 69.340312 5.464456 38.887669 11.580776 12:00:29 11-13-2024
16 42.334677 24.840487 67.175164 5.414908 38.551618 11.480363 12:01:30 11-13-2024
17 43.767118 25.752879 69.519997 5.400302 37.889638 11.796856 12:02:30 11-13-2024
18 43.844583 25.769257 69.61384 5.399012 38.273163 12.299657 12:03:29 11-13-2024
19 45.842235 26.940525 72.78276 5.40497 38.830443 12.36339 12:04:30 11-13-2024
20 39.886739 23.497867 63.384605 5.312904 39.444606 11.658287 12:05:30 11-13-2024
21 47.017405 27.601498 74.618904 5.421117 37.981346 11.847601 12:06:30 11-13-2024
22 41.129606 24.155583 65.285188 5.442133 40.038473 11.993341 12:07:30 11-13-2024
23 42.505353 24.800177 67.30553 5.389922 38.515976 11.391706 12:08:30 11-13-2024
24 44.574297 26.183866 70.758163 5.390931 37.650455 11.676127 12:09:30 11-13-2024
25 43.267452 25.417442 68.684894 5.333374 38.982377 11.218877 12:10:30 11-13-2024
26 43.354465 25.607241 68.961705 5.415956 39.380912 11.278631 12:11:31 11-13-2024
27 44.015451 26.039434 70.054885 5.412419 38.378780 10.771253 12:12:31 11-13-2024
28 43.816968 25.799308 69.616276 5.410111 39.034576 10.177551 12:13:30 11-13-2024
29 43.468196 25.650834 69.11903 5.454408 38.721269 10.411894 12:14:31 11-13-2024
30 43.402646 25.796203 69.198849 5.405005 38.612087 10.945035 12:15:31 11-13-2024
31 43.918526 25.836801 69.755327 5.300014 38.383616 11.581782 12:16:31 11-13-2024
32 44.201467 26.024207 70.225674 5.432924 39.186171 11.773383 12:17:31 11-13-2024
33 43.538089 25.533806 69.071896 5.415266 38.707702 11.941826 12:18:31 11-13-2024
34 44.228021 25.922384 70.150405 5.382427 38.230633 12.382415 12:19:31 11-13-2024
35 44.149368 25.949116 70.098484 5.427379 38.730551 12.010692 12:20:31 11-13-2024
36 43.37986 25.73028 69.11014 5.280689 38.731833 12.074431 12:21:31 11-13-2024
37 44.020188 26.041396 70.061584 5.45652 37.995084 11.694287 12:22:31 11-13-2024
38 45.882883 27.209846 73.092728 5.384152 37.967490 11.641528 12:23:31 11-13-2024
39 50.296228 29.968654 80.264882 5.430152 37.318617 11.43576 12:24:32 11-13-2024
40 41.265497 24.759045 66.024542 5.319582 39.843269 11.10174 12:25:32 11-13-2024
41 41.902362 25.061408 66.96377 5.321938 39.571283 9.860419 12:26:32 11-13-2024
42 42.631024 25.478557 68.10958 5.520457 38.138087 9.399119 12:27:32 11-13-2024
43 44.898588 26.691375 71.589963 5.36212 38.162809 10.158855 12:28:32 11-13-2024
44 45.20087 26.945348 72.146218 5.351201 38.803619 10.327761 12:29:32 11-13-2024
45 43.827088 26.111894 69.938983 5.451754 39.094417 11.248356 12:30:32 11-13-2024
46 45.483601 26.976138 72.459739 5.362979 38.204752 12.169797 12:31:32 11-13-2024
47 40.965358 23.75503 64.720388 5.610494 39.912422 13.035329 12:32:32 11-13-2024
48 42.959825 24.670617 67.630442 5.74055 38.513962 12.728704 12:33:32 11-13-2024
49 45.479512 25.884912 71.364425 5.823724 38.572245 12.456683 12:34:32 11-13-2024
50 43.822703 24.644279 68.466982 5.929333 38.840661 12.153671 12:35:32 11-13-2024
51 42.41355 23.814139 66.227689 5.971505 39.349651 11.970269 12:36:32 11-13-2024
52 42.525133 23.988683 66.513816 5.928174 38.657482 11.441462 12:37:33 11-13-2024
53 43.782625 24.60315 68.385775 5.905796 37.913619 11.314567 12:38:33 11-13-2024
54 44.076381 24.783303 68.859684 6.068719 38.097222 11.727943 12:39:33 11-13-2024
55 44.682269 25.000987 69.683257 5.871086 38.457922 12.03832 12:40:33 11-13-2024
56 43.293225 24.467611 67.760835 5.880311 38.806431 12.043047 12:41:33 11-13-2024
57 43.738044 24.880624 68.618668 5.880904 38.817074 11.955053 12:42:33 11-13-2024
58 43.768309 24.825211 68.59352 5.891232 38.763148 11.531188 12:43:33 11-13-2024
59 43.366944 24.570512 67.937456 5.853545 38.850148 11.300196 12:44:33 11-13-2024
60 43.534534 24.938961 68.473494 5.714287 38.531302 11.323879 12:45:33 11-13-2024
AVG 43.65 25.48 69.13 5.52 38.71 11.51
ppm@15% O2 32.37 2.58 18.13
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.51 1.24 0.02 0.06 0.27 0.67
FTIR Measurements
C-4
Calculated Emission Levels
Scout Energy Management, LLC
Ashley Compressor Station
Run 3
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 16 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 0.51 0.68 1058 0.49 0.825
Average O2 8.3 (% dry)A 2 1.68 0.70 0.837
Average CO2 7.1 (% dry)A 3 3.10 0.77 0.877
Average N2 + CO 84.6 (% dry)A 4 5.17 0.86 0.927
Dry Molecular Weight 29.47 lb/lbmol A 5 10.83 0.98 0.990Wet Molecular Weight 28.15 lb/lbmol A 6 12.90 1.02 1.010
EPA REFERENCE METHOD 320 A 7 14.32 1.04 1.020
Barometric Pressure 24.23 in Hg A 8 15.49 0.92 0.959
Moisture Content 11.51 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 69.13 ppm A 11
Calculated NOx Mass Output 1.24 lbs/hr A 12
Calculated NOx Output 0.51 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 5.52 ppm A 15
Calculated CO Mass Output 0.06 lbs/hr A 16
Calculated CO Output 0.02 g/bhp-hr B 1 0.51 0.71 1058 0.49 0.843
EPA REFERENCE METHOD 320 B 2 1.68 0.76 0.872
Average Analyzer NMNEHC Level 38.71 ppm B 3 3.10 0.79 0.889
Calculated NMNEHC Mass Output 0.67 lbs/hr B 4 5.17 0.84 0.917Calculated NMNEHC Output 0.27 g/bhp-hr B 5 10.83 0.99 0.995
LOAD APPROXIMATION B 6 12.90 1.01 1.005
Estimated Engine Load 1104.0 BHP B 7 14.32 1.02 1.010
B 8 15.49 0.94 0.970
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16Averages 0.9 1058 0.5 0.934
Average Stack Gas Velocity 83.48 ft/sec
Average Dry Flowrate 2504.73 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)11-13-2024 8:03:53 -0.278614 -0.105992 -0.004824 -0.097225 -1.207039 0.280738 -0.217180 0.221864 0.221853 -0.009679 -0.384606 -0.384588 0.057911 190.130234 0.956807
11-13-2024 8:04:01 -0.366371 -0.057764 -0.008907 -0.023510 -0.590733 -0.421986 0.484830 -0.018808 -0.018806 0.006754 -0.424135 -0.424097 0.030282 190.144775 0.95977511-13-2024 8:04:08 -0.394198 -0.055350 -0.005775 -0.056417 -0.437015 -0.622192 0.241337 -0.072978 -0.072974 -0.026431 -0.449547 -0.449521 0.034418 190.130234 0.96220811-13-2024 8:04:15 -0.377140 -0.077858 -0.004662 -0.028390 -0.475780 -0.107430 0.081515 0.048113 0.048111 -0.033331 -0.454998 -0.454977 0.001571 190.173843 0.96092311-13-2024 8:04:53 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 190.268982 0.95771211-13-2024 8:05:06 -0.037123 0.066498 0.003478 -0.111440 -0.072139 0.126283 0.093975 0.116162 0.116166 0.007656 0.029375 0.029376 0.000733 190.401566 0.961600
11-13-2024 8:05:14 -0.187121 0.046798 -0.005390 -0.271471 0.210002 -0.718697 -0.479896 -0.074887 -0.074883 -0.011702 -0.140323 -0.140316 0.034944 190.522705 0.95725011-13-2024 8:05:21 -0.063397 0.054145 -0.000883 -0.041046 -0.317962 -0.292964 1.330995 0.062485 0.062484 -0.007247 -0.009251 -0.009251 0.061613 190.595383 0.96005011-13-2024 8:05:29 -0.085439 0.108607 0.004924 0.014507 0.351386 -0.307500 -0.511880 0.081335 0.081339 0.015467 0.023168 0.023169 0.004146 190.551773 0.960326
11-13-2024 8:05:36 -0.229597 0.082533 0.004289 0.039418 0.492933 0.150091 0.485900 -0.151507 -0.151514 -0.008043 -0.147064 -0.147070 0.017496 190.566315 0.96170311-13-2024 8:05:44 -0.253814 0.125292 0.002150 -0.044422 -0.032316 -0.150510 0.603400 -0.023499 -0.023499 0.020273 -0.128523 -0.128525 0.015449 190.575394 0.95758311-13-2024 8:05:51 -0.216712 0.057849 0.002611 -0.022789 -0.415917 0.603273 -0.211633 0.119669 0.119672 0.000331 -0.158863 -0.158867 0.078874 190.580841 0.96298811-13-2024 8:05:59 0.043569 0.082385 -0.000216 -0.066805 0.034258 -0.460820 -0.432390 -0.073200 -0.073200 0.002121 0.125954 0.125954 0.008559 190.638992 0.96491611-13-2024 8:06:06 0.182138 0.161810 0.002819 -0.164777 0.259160 -1.248319 -0.606203 0.218976 0.218982 -0.000487 0.343948 0.343958 0.044852 190.668060 0.962070
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)
11-13-2024 8:06:28 484.985548 483.177249 502.081941 190.664429 0.967517 11-13-2024 8:10:26 96.880805 191.029037 0.96529511-13-2024 8:06:36 491.528300 491.103733 507.909211 190.668060 0.971893 11-13-2024 8:10:34 97.277169 191.002380 0.96349311-13-2024 8:06:44 492.662244 494.024618 512.287359 190.726212 0.968818 11-13-2024 8:10:41 97.028907 190.958771 0.965100
11-13-2024 8:06:51 492.239678 492.334762 509.238735 190.726212 0.973408 11-13-2024 8:10:49 97.087773 190.987854 0.96418211-13-2024 8:06:58 493.820123 494.661293 513.716850 190.740738 0.968634 11-13-2024 8:10:56 97.871345 190.886093 0.96386011-13-2024 8:07:06 491.880322 492.061354 505.899876 190.813416 0.974372 11-13-2024 8:11:04 97.939131 190.791611 0.96256411-13-2024 8:07:13 493.007105 494.082397 513.999294 190.711670 0.968634 11-13-2024 8:11:11 98.716422 190.958771 0.96349311-13-2024 8:07:21 490.839403 492.035804 505.716472 190.784348 0.975015 11-13-2024 8:11:18 99.136672 190.944244 0.962345
11-13-2024 8:07:28 491.723760 492.955708 511.189571 190.867920 0.973729 11-13-2024 8:11:26 97.947419 190.886093 0.96427311-13-2024 8:07:36 492.852433 494.069878 512.976674 190.711670 0.971618 11-13-2024 8:11:33 99.544215 190.900635 0.96202411-13-2024 8:07:43 495.155387 494.243766 505.170791 190.813416 0.976529
11-13-2024 8:07:51 499.377216 497.385795 509.459423 190.817047 0.96963311-13-2024 8:07:58 497.889099 497.711816 508.674375 190.842484 0.971373
Date Time NO2 191C span Temp ( C )Pressure (atm)11-13-2024 8:12:01 137.025847 190.791611 0.965295
11-13-2024 8:12:08 142.786085 190.726212 0.96739511-13-2024 8:12:16 143.079984 190.784348 0.96909311-13-2024 8:12:23 143.800852 190.813416 0.96702811-13-2024 8:12:31 143.258695 190.842484 0.97037811-13-2024 8:12:38 143.692501 190.817047 0.967343
11-13-2024 8:12:46 142.935204 190.825531 0.97474711-13-2024 8:12:53 143.785961 190.857025 0.97047011-13-2024 8:13:01 143.362493 190.855209 0.97320711-13-2024 8:13:09 144.200588 190.827957 0.968588
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)11-13-2024 8:13:33 0.902989 118.746822 17.636818 190.867920 0.933484 11-13-2024 8:16:39 1.440223 190.927277 0.92494311-13-2024 8:13:40 140.348112 140.923073 217.520741 190.915161 0.935722 11-13-2024 8:16:46 79.265142 190.900635 0.93177511-13-2024 8:13:48 475.370670 477.112033 495.447277 190.915161 0.928745 11-13-2024 8:16:54 97.705804 190.900635 0.92622011-13-2024 8:13:55 481.238106 482.062515 500.584456 190.900635 0.929893 11-13-2024 8:17:02 98.227759 190.900635 0.926266
11-13-2024 8:14:03 482.137214 482.506555 501.800683 190.900635 0.930168 11-13-2024 8:17:09 98.058569 190.915161 0.92475111-13-2024 8:14:10 484.174949 484.143762 503.145881 190.900635 0.929112 11-13-2024 8:17:17 97.766868 190.929703 0.92732211-13-2024 8:14:18 487.739419 487.479480 505.886335 190.813416 0.923696 11-13-2024 8:17:24 98.285329 190.931519 0.928986
11-13-2024 8:14:25 483.011587 483.522720 499.959245 190.944244 0.932784 11-13-2024 8:17:32 98.759498 190.900635 0.92585311-13-2024 8:14:33 487.004592 486.873957 504.767604 190.871567 0.925670 11-13-2024 8:17:39 98.780557 190.886093 0.92801111-13-2024 8:14:40 485.291430 486.490173 506.145243 190.900635 0.928791 11-13-2024 8:17:47 97.771318 190.900635 0.92759711-13-2024 8:17:54 98.003709 190.827957 0.926679
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)11-13-2024 8:18:17 0.241969 0.561287 0.285914 1.135344 190.880646 0.930191
11-13-2024 8:18:24 0.859800 0.874221 -0.586276 1.545964 190.857025 0.92700111-13-2024 8:18:32 0.418911 0.777053 0.378986 1.017351 190.944244 0.93214211-13-2024 8:18:39 0.458103 0.221992 0.054464 1.593102 190.827957 0.926404
11-13-2024 8:18:47 0.287929 0.772100 -0.320984 0.468295 190.900635 0.92851511-13-2024 8:18:54 0.212013 0.437393 -0.519372 0.999920 190.871567 0.92842411-13-2024 8:19:02 0.482464 0.484571 -0.619899 -0.213386 190.906082 0.925532
Date Time CO2% 191C Propane 191C span Temp ( C )Pressure (atm)
11-13-2024 9:41:23 6.401118 26.776076 191.419067 0.92266711-13-2024 9:41:30 6.429098 27.622173 191.525665 0.92208911-13-2024 9:41:38 6.380698 27.185270 191.467529 0.92488911-13-2024 9:41:45 6.423951 27.097857 191.511139 0.92415511-13-2024 9:41:52 6.372324 26.726077 191.598343 0.925853
11-13-2024 9:42:45 6.376217 27.370064 191.500870 0.92385611-13-2024 9:42:52 6.383682 27.479158 191.469955 0.92167611-13-2024 9:43:00 5.597681 26.019276 191.380310 0.926129
11-13-2024 9:43:07 2.473321 105.379801 191.402115 0.91882411-13-2024 9:43:15 5.788548 65.874973 191.365784 0.91892211-13-2024 9:43:37 5.955517 57.216818 191.396469 0.91961711-13-2024 9:43:45 5.951979 56.026523 191.351242 0.916856
SAMPLE SPIKE RECOVERY
Raw Calibration Data
BACKGROUND / PRE DIRECT ZERO
PRE DIRECT CAL
NO2 CAL
PRE SYSTEM CAL
PRE SYSTEM ZERO
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)11-13-2024 12:52:16 494.402366 491.026641 504.033503 190.723785 0.961921 11-13-2024 12:50:45 96.453085 190.910324 0.95779711-13-2024 12:52:24 495.512701 492.790238 506.667911 190.784348 0.966706 11-13-2024 12:50:53 98.108804 190.871567 0.958627
11-13-2024 12:52:31 495.248644 493.717569 505.963867 190.827957 0.970011 11-13-2024 12:51:00 97.083623 190.857025 0.96115211-13-2024 12:52:39 496.610519 495.247429 509.031533 190.900635 0.965008 11-13-2024 12:51:08 98.135876 190.842484 0.95656211-13-2024 12:52:46 496.880208 494.272122 505.209121 190.755280 0.967119 11-13-2024 12:51:15 98.286778 190.886093 0.95541411-13-2024 12:52:54 498.895980 495.651660 509.698978 190.857025 0.966339 11-13-2024 12:51:22 98.389283 190.886093 0.95766311-13-2024 12:53:01 497.370775 495.950005 506.572997 190.791611 0.965255 11-13-2024 12:51:30 97.564072 190.886093 0.960326
11-13-2024 12:53:09 498.486628 495.325536 508.771267 190.697128 0.967303 11-13-2024 12:51:37 98.784560 190.827957 0.95486311-13-2024 12:53:16 499.917827 497.745457 509.766133 190.726212 0.962483 11-13-2024 12:51:45 98.841176 190.804337 0.95786411-13-2024 12:53:24 501.621109 498.264072 513.271564 190.697128 0.962300 11-13-2024 12:51:53 98.433625 190.857025 0.955644
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)
11-13-2024 12:51:08 0.169017 0.192588 -1.345131 190.842484 0.956562 2024-11-13 12:55:16 0.428087 190.698349 0.9585211-13-2024 12:51:15 0.391907 0.394336 -0.967879 190.886093 0.955414 2024-11-13 12:55:24 -0.579369 190.697128 0.96064711-13-2024 12:51:22 -0.092983 0.344101 0.225047 190.886093 0.957663 2024-11-13 12:55:31 0.279506 190.726212 0.9623
11-13-2024 12:51:30 0.341013 0.186751 -0.423519 190.886093 0.960326 2024-11-13 12:55:38 0.586876 190.769806 0.95968311-13-2024 12:51:37 0.222060 0.290955 -0.197283 190.827957 0.954863 2024-11-13 12:55:46 0.520371 190.813416 0.95871911-13-2024 12:51:45 0.169680 0.350002 -0.055529 190.804337 0.957864 2024-11-13 12:55:53 0.972314 190.813416 0.9610611-13-2024 12:51:53 0.259871 0.236770 -1.179535 190.857025 0.955644 2024-11-13 12:56:01 0.37934 190.931519 0.959069
POST SYSTEM CAL
POST SYSTEM ZERO
PRE TEST 1 503.1 6.4 27.2 5.9 59.7 0.078 76.8%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 497.7 504.5 -0.1 -1.35 -0.01
CO 497.9 506.4 0.0 -1.68 0.00
Propane 508.7 503.1 -0.1 1.11 -0.03
Ethylene 99.5 100.1 0.0 -0.56 0.03
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 487.5 504.5 0.6 -3.37 0.12
CO 487.7 506.4 0.4 -3.68 0.08
Propane 505.9 503.1 -0.2 0.55 -0.04
Ethylene*97.8 100.1 0.9 -2.33 0.93
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 498.3 504.5 0.3 -1.24 0.06 2.14 0.06
CO 501.6 506.4 0.2 -0.94 0.04 2.74 0.04
Propane 513.3 503.1 -0.6 2.02 -0.11 1.47 0.07
Ethylene*98.8 100.1 0.4 -1.26 0.37 1.07 0.57
*CTS Scans are conducted with Ethylene through the sample line.
Lf
5.11
Lr Cr Tr Pr Lr/Lf
5.34 99.5 190.9 1.0 1.04
Ls Cs Ts Ps Ls/Lf
5.64 97.8 190.9 0.9 1.10
% Recovery
Propane
PRE DIRECT CAL
FTIR QA/QC SUMMARY
SAMPLE RECOVERY CALCULATIONS
Period Spike #Concentration of
Propane Cylinder
Stack CO2
Concentration
Pathlength
Stack Propane
Concentration
Stack + Spike CO2
Concentration
Stack + Propane
Concentration
DF
Calculated
POST SYSTEM CAL
PRE SYSTEM CAL
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
Part Number:E05NI99E15A0000 Reference Number:153-403072999-1
Cylinder Number:CC207614 Cylinder Volume:144.0 CF
Laboratory:124 - Tooele (SAP) - UT Cylinder Pressure:2015 PSIG
PGVP Number:B72024 Valve Outlet:660
Gas Code:CH4,CO,NO,NOX,PPN,BALN Certification Date:Jun 25, 2024
Expiration Date:Jun 25, 2032
Certification performed in accordance with “EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)” document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder below 100 psig, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
NOX 500.0 PPM 504.5 PPM G1 +/- 1.0% NIST Traceable 06/18/2024, 06/25/2024
CARBON MONOXIDE 500.0 PPM 506.4 PPM G1 +/- 0.8% NIST Traceable 06/18/2024
METHANE 500.0 PPM 501.7 PPM G1 +/- 0.9% NIST Traceable 06/18/2024
NITRIC OXIDE 500.0 PPM 504.5 PPM G1 +/- 1.0% NIST Traceable 06/18/2024, 06/25/2024
PROPANE 500.0 PPM 503.1 PPM G1 +/- 0.7% NIST Traceable 06/19/2024
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NTRM 15060532 CC450607 491.9 PPM CARBON MONOXIDE/NITROGEN 0.6%Mar 05, 2027
PRM 12409 D913660 15.01 PPM NITROGEN DIOXIDE/AIR 1.5%Feb 17, 2023
NTRM 16060404 CC471136 500.5 PPM METHANE/AIR 0.6%Dec 03, 2027
NTRM 22060727 CC745222 495.3 PPM NITRIC OXIDE/NITROGEN 0.9%Apr 26, 2026
GMIS 1531022022103 CC517868 4.914 PPM NITROGEN DIOXIDE/NITROGEN 1.6%Feb 17, 2026
NTRM 12010921 ND46380 487 PPM PROPANE/AIR 0.6%Dec 04, 2031
The SRM, NTRM, PRM, or RGM noted above is only in reference to the GMIS used in the assay and not part of the analysis.
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
Nicolet iS50 AUP2110269 CO MCO FTIR May 30, 2024
Nicolet iS50 AUP2110269 CH4 M1CH4 FTIR Jun 05, 2024
Nicolet iS50 AUP2110269 NO MNO FTIR Jun 11, 2024
Nicolet iS50 AUP2110269 NO2 impurity FTIR NO2 impurity Jun 12, 2024
MKS FTIR C3H8 018143349 FTIR Jun 05, 2424
Triad Data Available Upon Request
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84074
Airgas.com
Signature on file
Approved for Release Page 1 of 1
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
Part Number:E02AI99E15W0077 Reference Number:153-402928833-1
Cylinder Number:CC168787 Cylinder Volume:146.0 CF
Laboratory:124 - Tooele (SAP) - UT Cylinder Pressure:2015 PSIG
PGVP Number:B72024 Valve Outlet:660
Gas Code:NO2,O2,BALN Certification Date:Jan 11, 2024
Expiration Date:Jan 11, 2027
Certification performed in accordance with “EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)” document EPA
600/R-12/531, using the assay procedures listed. Analytical Methodology does not require correction for analytical interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 95%. There are no significant impurities which affect the use of this calibration mixture. All concentrations are on a
mole/mole basis unless otherwise noted. The results relate only to the items tested. The report shall not be reproduced except in full without approval of the laboratory. Do
Not Use This Cylinder below 100 psig, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
NITROGEN DIOXIDE 150.0 PPM 143.0 PPM G1 +/- 2.0% NIST Traceable 01/03/2024, 01/11/2024
AIR Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
GMIS 1534002023108 CC510760 201.3 PPM NITROGEN DIOXIDE/NITROGEN 1.1%Jan 27, 2026
PRM 12398 D887666 197.3 PPM NITROGEN DIOXIDE/AIR 1.0%Jan 28, 2023
The SRM, NTRM, PRM, or RGM noted above is only in reference to the GMIS used in the assay and not part of the analysis.
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
MKS FTIR NO2 018143349 FTIR Jan 02, 2024
Triad Data Available Upon Request
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84074
Airgas.com
Signature on file
Approved for Release Page 1 of 1
CERTIFICATE OF ANALYSIS
Grade of Product: PRIMARY STANDARD
Part Number:X02NI99P15AD524 Reference Number:153-403021542-1
Cylinder Number:CC188939 Cylinder Volume:144.4 CF
Laboratory:124 - Tooele (SAP) - UT Cylinder Pressure:2015 PSIG
Analysis Date:Apr 19, 2024 Valve Outlet:350
Lot Number:153-403021542-1
Expiration Date:Apr 19, 2027
Primary Standard Gas Mixtures are traceable to N.I.S.T. weights and/or N.I.S.T. Gas Mixture reference materials.
ANALYTICAL RESULTS
Component Req Conc Actual Concentration Analytical
(Mole %)Uncertainty
ETHYLENE 100.0 PPM 100.1 PPM +/- 1%
NITROGEN Balance
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84074
Airgas.com
Signature on file
Approved for Release Page 1 of 1
Scout – Ashley
11-13-2024
Scout – Ashley
11-13-2024
Scout – Ashley
11-13-2024
Spectral Fit
Run 1
Spectral Fit
Run 2
Spectral Fit
Run 3
Analysis Validation Report - Run 1
Sample Filename: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000160.LAB
Filename for noise: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000007.LAB
Interferences Filenames: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000091.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000092.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000093.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000094.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000095.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000096.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000097.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000098.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 36.89 3.2 -0.84 1.15 4.36 4.36 -1.54 --0-2795 1.04 Good
NO2 191C 21.96 0.39 -0.07 0.08 0.41 0.41 -0.44 --0-488 0.98 Good
N2O 191C 0.21 0.53 0.34 0.1 0.11 0.61 0.61 0.35 0.44 0.01 0.11 0-200 -Close to DL
NH3 TE 191C -4.27 19.22 8.51 12.68 21.65 32.8 32.8 10.68 10.68 2.17 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C12.51 0.14 -0.05 0.08 0.23 0.23 -0.25 --0-40 -Good
FORMALDEHYDE 191C2.74 1.02 2.68 0.72 0.81 1.16 1.16 3.04 3.04 0.36 0.89 0-69 -Close to DL
FORMIC ACID 191C TE0.56 10.79 1.68 3.88 4.55 12.63 12.63 2.22 6.98 0.54 0.56 0-466 -Close to DL
CH4 2900 CM-1 191C849.18 18.8 -4 5.82 34.83 34.83 -16.98 --0-3143 0.98 Good
PROPANE 191C27.99 1.29 -0.59 0.71 1.54 1.54 -0.56 --0-4976 0.96 Good
PROPYLENE 191C TE-0.91 10.84 6.33 4.3 5.08 12.83 12.83 6.6 6.6 0.27 2.11 0-194 -Close to DL
ETHANE 191C78.76 2.89 -1.49 2.32 4.5 4.5 -1.58 --0-1004 -Good
ETHYLENE 191C TE4.47 15.79 2.19 5.58 6.89 19.49 19.49 3.28 10.12 1.09 0.73 0-900 -Close to DL
CO PPM 191C (1OF2)4.95 1.97 5.57 0.61 1.33 4.25 4.25 6.64 6.64 1.08 1.86 0-5010 1.03 Close to DL
CO2% 191C 6.25 0.25 -0.04 0.06 0.34 0.34 -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 191C-0.81 2.85 2.27 1.78 2.29 3.66 3.66 2.59 2.59 0.32 0.76 0-186 1.01 Close to DL
ACETYLENE 191C0.07 2.18 0.65 2.3 3.04 2.89 3.04 0.86 0.86 0.21 0.22 0-1016 -Close to DL
SO2 191C 1.77 3.36 2.82 0.7 0.86 4.1 4.1 2.89 2.89 0.07 0.94 0-964 1.02 Close to DL
HEXANE 191C 1.51 0.88 1.9 0.35 0.47 1.19 1.19 2.2 2.2 0.3 0.63 0-1000 -Close to DL
Analysis Validation Report - Run 2
Sample Filename: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000220.LAB
Filename for noise: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000007.LAB
Interferences Filenames: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000091.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000092.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000093.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000094.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000095.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000096.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000097.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000098.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 38.2 2.85 -0.84 1.15 3.89 3.89 -1.23 --0-2795 1.04 Good
NO2 191C 22.7 0.36 -0.07 0.08 0.38 0.38 -0.45 --0-488 0.98 Good
N2O 191C 0.24 0.49 0.34 0.1 0.11 0.56 0.56 0.35 0.39 0.01 0.11 0-200 -Close to DL
NH3 TE 191C -3.82 19.31 8.51 12.68 21.65 32.95 32.95 10.68 10.68 2.17 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C10.48 0.13 -0.05 0.08 0.21 0.21 -0.21 --0-40 -Good
FORMALDEHYDE 191C2.49 1.02 2.68 0.72 0.81 1.16 1.16 3.04 3.04 0.36 0.89 0-69 -Close to DL
FORMIC ACID 191C TE-0.37 11.03 1.68 3.88 4.55 12.91 12.91 2.22 7.23 0.54 0.56 0-466 -Close to DL
CH4 2900 CM-1 191C882.4 16.75 -4 5.82 31.03 31.03 -17.65 --0-3143 0.98 Good
PROPANE 191C28.89 1.33 -0.59 0.71 1.59 1.59 -0.58 --0-4976 0.96 Good
PROPYLENE 191C TE-1.32 10.94 6.33 4.3 5.08 12.94 12.94 6.6 6.67 0.27 2.11 0-194 -Close to DL
ETHANE 191C 81.31 2.91 -1.49 2.32 4.53 4.53 -1.63 --0-1004 -Good
ETHYLENE 191C TE4.37 15.75 2.19 5.58 6.89 19.43 19.43 3.28 10.08 1.09 0.73 0-900 -Close to DL
CO PPM 191C (1OF2)5 1.88 5.57 0.61 1.33 4.06 4.06 6.64 6.64 1.08 1.86 0-5010 1.03 Close to DL
CO2% 191C 6.42 0.24 -0.04 0.06 0.33 0.33 -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 191C-1.37 2.8 2.27 1.78 2.29 3.6 3.6 2.59 2.59 0.32 0.76 0-186 1.01 Close to DL
ACETYLENE 191C0.18 2.2 0.65 2.3 3.04 2.91 3.04 0.86 0.86 0.21 0.22 0-1016 -Close to DL
SO2 191C 1.03 2.9 2.82 0.7 0.86 3.54 3.54 2.89 2.89 0.07 0.94 0-964 1.02 Close to DL
HEXANE 191C 1.65 0.9 1.9 0.35 0.47 1.22 1.22 2.2 2.2 0.3 0.63 0-1000 -Close to DL
Analysis Validation Report - Run 3
Sample Filename: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000280.LAB
Filename for noise: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000007.LAB
Interferences Filenames: C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000091.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000092.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000093.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000094.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000095.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000096.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000097.LAB
C:\OLT\2024 Data\Scout\Ashley CS C-4 11-13-24\ASHLEY CS C-4 11-13-24_000098.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConcMDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 36.69 2.96 -0.84 1.15 4.04 4.04 -1.33 --0-2795 1.04 Good
NO2 191C 20.96 0.36 -0.07 0.08 0.38 0.38 -0.42 --0-488 0.98 Good
N2O 191C 0.2 0.52 0.34 0.1 0.11 0.6 0.6 0.35 0.43 0.01 0.11 0-200 -Close to DL
NH3 TE 191C -5.61 20.57 8.51 12.68 21.65 35.12 35.12 10.68 10.68 2.17 2.84 0-2995 -Close to DL
H2O% (HIGH) 191C11.97 0.14 -0.05 0.08 0.23 0.23 -0.24 --0-40 -Good
FORMALDEHYDE 191C2.93 1.02 2.68 0.72 0.81 1.15 1.15 3.04 3.04 0.36 0.89 0-69 -Close to DL
FORMIC ACID 191C TE-0.21 10.86 1.68 3.88 4.55 12.71 12.71 2.22 7.06 0.54 0.56 0-466 -Close to DL
CH4 2900 CM-1 191C857.31 18.04 -4 5.82 33.42 33.42 -17.15 --0-3143 0.98 Good
PROPANE 191C28.64 1.3 -0.59 0.71 1.56 1.56 -0.57 --0-4976 0.96 Good
PROPYLENE 191C TE-1.11 10.9 6.33 4.3 5.08 12.9 12.9 6.6 6.64 0.27 2.11 0-194 -Close to DL
ETHANE 191C 78.03 2.89 -1.49 2.32 4.5 4.5 -1.56 --0-1004 -Good
ETHYLENE 191C TE3.98 15.93 2.19 5.58 6.89 19.66 19.66 3.28 10.28 1.09 0.73 0-900 -Close to DL
CO PPM 191C (1OF2)5.31 1.76 5.57 0.61 1.33 3.79 3.79 6.64 6.64 1.08 1.86 0-5010 1.03 Close to DL
CO2% 191C 6.29 0.24 -0.04 0.06 0.33 0.33 -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 191C-1.32 2.82 2.27 1.78 2.29 3.62 3.62 2.59 2.59 0.32 0.76 0-186 1.01 Close to DL
ACETYLENE 191C0.22 2.18 0.65 2.3 3.04 2.88 3.04 0.86 0.86 0.21 0.22 0-1016 -Close to DL
SO2 191C 1.14 3.35 2.82 0.7 0.86 4.09 4.09 2.89 2.89 0.07 0.94 0-964 1.02 Close to DL
HEXANE 191C 1.66 0.88 1.9 0.35 0.47 1.2 1.2 2.2 2.2 0.3 0.63 0-1000 -Close to DL
APPENDIX C
Test Run Load %Site Rated Load, bhp Load Approx., bhp
1 80 1380 1104.0
2 81 1380 1117.8
3 80 1380 1104.0
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 2333.51 1104.0 8.2 72.35 0.50 1.21 5.53 0.02 0.06 38.50 0.25 0.62 11.77
2 2462.03 1117.8 8.3 68.34 0.49 1.20 5.55 0.02 0.06 38.97 0.27 0.66 11.34
3 2504.73 1104.0 8.3 69.13 0.51 1.24 5.52 0.02 0.06 38.71 0.27 0.67 11.51
1108.6 8.3 69.94 0.50 1.22 5.53 0.02 0.06 38.73 0.26 0.65 11.54
Summary
Average Levels
Example Calculations: Scout Energy Management, LLC, Ashley Compressor Station, C-4
The following is a step-by-step calculation for the first test run conducted on the Ashley
Compressor Station C-4.
Test Parameters
Stack Diameter = 16 inchesTraverse Points = 16Ports = 2Barometric Pressure = 24.22 in HgAverage O2 = 8.2%Average CO2 = 7.1%Load Approximation = 1104.0 bhpMoisture Content = 11.77%
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 = 7.1%
%O2 – Oxygen Content Of The Gas = 8.2%
%N2 – Nitrogen Content Of The Gas%CO – Carbon Monoxide Content Of The Gas
(%N2 +%CO) = (100 - %O2 - %CO2)
= (100 – 8.2 – 7.1)
= 84.7% Dry
= (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO))
= (0.44 * 7.1) + (0.32 * 8.2) + (0.28 * 84.7)
= 29.46 lb/lbmol
Wet Molecular Weight (lb/lbmol)
= MD * (1-BWS) + (18) * BWS
Where:
MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 29.46 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 11.77%
= MD * (1-BWS) + (18) * BWS
= 29.46 * (1 – (11.77/ 100)) + (18 * (11.77/ 100))
= 28.11 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) = 0.868 in H2O
TS – Average stack temperature (R) = 1047 RPB– Barometric pressure (in Hg) = 24.22 in Hg
PS– Stack pressure relative to barometric pressure (inches water) = 0.5 in H2OMA– Molecular weight of the wet gas (lb/lbmol) = 28.11 lb/lbmol
= Cp * (85.49) *∆PAVG *(TS / (((PS / 13.6) + PB) * MA))
= 0.84 * (85.49) * 0.868 *( 1047 / (((0.5/ 13.6) + 24.22) * 28.11))
=77.23 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) = 16 inchesBWS – Moisture content of the gas (%) = 11.77%
TSTD– Standard temperature (528R)
TS – Average stack temperature (R) = 1047 R
PB – Barometric pressure (in Hg) = 24.22 in Hg
PS– Stack pressure relative to barometric pressure (inches water) = 0.5 in H2O
VS– Average Stack gas velocity (ft/sec) = 77.23 ft/sec
= 60 * (1-BWS) * VS * * (((DS / 2) / 12))2)* TSTD / TS * (PB + (PS / 13.6)) / 29.92
= 60 * (1 - (11.77/ 100)) * 77.23 * * (((16 / 2) / 12))2) * 528 / 1047 * (24.22 + (0.5 /
13.6)) / 29.92
=2333.51 dscfm
Conversion of Dry Flowrate to m3/hr
= Q * 60 * 2.83168*10 -2
Where:
Q – Volumetric Flowrate = 2333.51 dscfm
2.83168*10 -2 – Conversion factor for cubic feet to cubic meter60 – Minutes in an hour
= Q * 60 * 2.83168*10 -2
= 2333.51 *60 * 2.83168*10 -2
=3964.657 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 = 72.35 ppm1.92*10 -3 - Conversion constant for ppm to g/m3 NOxQ – VolumetricFlowrate = 3964.657 m3/hr
T – Time in Hours of Test Run = 1 hrHP-hr – Unit Brake Horsepower = 1104.0 Bhp
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
= (72.35 * 1.912*10 -3 * 3964.657 * 1) / 1104.0
=0.50 g/Bhp-hr
NOx Emission Rate (lbs/hr)
= g/Bhp-hr / 454 * Bhp
Where:g/Bhp-hr = 0.50 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1104.0 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.50 / 454 * 1104.0
= 1.21 lbs/hr
CO Emission Rate (g/Bhp-hr)= (Cd * 1.164*10 -3 * Q * T) / HP-hr
Where:Cd – Measured CO concentration in ppm = 5.53 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 COQ – VolumetricFlowrate = 3964.657 m3/hrT – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1104.0 Bhp
= (Cd * 1.164*10 -3 * Q * T) / HP-hr
= (5.53 * 1.164*10 -3 * 3964.657 * 1) / 1104.0
=0.02 g/Bhp-hr
CO Emission Rate (lbs/hr)= g/Bhp-hr / 454 * Bhp
Where:g/Bhp-hr = 0.02 g/Bhp-hr454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1104.0 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.02 / 454 * 1104.0
= 0.06 lbs/hr
VOC Emission Rate (g/Bhp-hr)= (Cd * 1.833*10 -3 * Q * T) / HP-hr
Where:Cd – Measured VOC concentration in ppm = 38.50 ppm1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – VolumetricFlowrate = 3964.657 m3/hr
T – Time in Hours of Test Run = 1 hrHP-hr – Unit Brake Horsepower = 1104.0 Bhp
= (Cd * 1.833*10 -3 * Q * T) / HP-hr
= (38.50 * 1.833*10 -3 * 3964.657 * 1) / 1104.0
=0.25 g/Bhp-hr
VOC Emission Rate (lbs/hr)
= g/Bhp-hr / 454 * Bhp
Where:
g/Bhp-hr = 0.25 g/Bhp-hr454 – Conversion factor for g to lbsBhp - Unit Brake Horsepower = 1104.0 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.25 / 454 * 1104.0
= 0.62 lbs/hr
APPENDIX E
FTIR Engine Test Sheet
-~-l
II! •..,q ) , .
~ Location I Unit l.D..
h\fpe of Test Completed
. v Vv
M, he
~v I J4.5h/pi/ c5 C, -
3X I.'rJ! JI/{/V'H \ .. -e­r ) o(dof1 Iv,·",Field Technician (s)
',/1 t1Client Rep and/or State Rep '" (I/I~/zq[Date .
/z-qq Stack Diagram
[Enqine Make If/fir
!Non-~esettable Run Time Hours
-~.Ie. I . -rt::JI. r ­~Engine Mode,
"'>:lUI, w7rFFO 3Z-7f/lEngine SIN • Verified: U1/
IPon: Distance p,___. v ZCO" :.~~~~..~~~~~,~
iPoft Distance B 72 " lC:xh-;:;-:-:S:;--IJ'ame+:>r (inches) 16 1/ ..IL-',:OLJ ~ ,i,..... Le. " ...., ...... -.-LCalibratlon Gas I Cylinder # i Concentration
~NO loom! !cC207614 1: 504.5
~-..:",,--,.....­CC207614 506.4~CCr (;.::,on1)--------_... ~Propane (p~__. !cC207614 503.1
-·l '" Ii ~

:r-------',~

~N02 (porn) IcC168787 iL__ 143 ~ ". iCC188939 ~ 100.1lcthy:ene (ppm)
ci;,~,~ .1~i;,'HI0fiMethane (ppm) iCC2076'14 I 501.7
IAcetaidehyde (porn) 01/24/2025 .CC321163 196.7~
\
.­.......
I
t
A
e
j I
\ 1
\
-,
6 Ih
!C02 % Dry _ L.----7,i 7./ ;z., / I~O,b,.D % .(Paoe~) or (Estimated) C-I?I ,_~O '3 / I ~O
giqrlition TillJlng ( l-) I zl),() .....
IAFR Setting mV (Left Bank) tie5/!/G71l ~ ~JI'Yn ;'IArR Setting mV (Right Bank) i z..£: I .:r­-
,....!,-_,"'_~ _C_Cl_'_T_em_;-'-p-'-(__r-"-! -'-=--'---_.J~-U!L
!post e2Z Temp CF) ! 7'171­leal Differentiai Pres. (" G··,f"'"H-;-:;2""O")---------....L:"-!--1 t. Cj
bu......,;d,·.v' 0/ -'-----­i-e'! ll;l l. 10. '---­,
!02% I~ t6. Z
r Test 1 Test 2 Test 3
[Time of Readinq OQf{4 lif') t/ t( 11'11-(
[Atm Pressure (in Hg) ; ~Cf,ZZ-z. 't, ~.Z-7-tt·;!..3
!.A.tm Temp (OF) ~ I-fJ) 1§;-0 R3
IEngine RPM \ i 13f.-( =t­13 ~9
(Manifo!d Pres. Vact"] or Boost(~ Boost (psia) , 33·~ 3,5'• 6 33· sz­
'Manifold Temp CF) .. I iL3. -f / l..f I/~--_._~
Psuction (psi) Staqe 1 I~ Ie;­/ s:':
Tsuction CF) Stage 1 --' -_.
Pdischarqe fEB Stage ~ I!...-­q +­L1.. '1 Q?
Psuction (psi) Stage 2 i --_.
!Tsuction CF\ Stage 2 j -­I --­~discharge (psi) Stage2 ~ z..1:1.."'1 zs-0 »: C;-O
!Psuction (psi) Stage 3 Ii --[rsuct!on CF) Stage 3 +-­_. -teJ~~~.'?::.sf';fpsQ S~age ~. _ iL....--'-l.M 4.,+q:: 'R<~O
!o"', iction (n",i' Staoe 4 f ,... d ·u.,..JI: C".... } ..... ~;;, •
~ Tsuction e'F) Staqe 4 -lfPd.scnaroe (as;) Staae ,j I--~·· I ,
lGas 1hf5iJg~put (mmcf/~! or ( t6-4£ ) ~---36zsu I r.:fl--. ~_ .~ 3;82 I
0.­~.. .~, -
SorT:E.~ un~.ts show boost ill inches of Hg. In this situation pfease indicate if it is
cositive (+) or negat!ve(-.) Eg: (+12") or (- 5")
9i17/2019
COMPANY NAME:Scout COMPANY LOCATION:Ashley CS C-4 DATE:November 13, 2024
STACK DIAMETER (inches):16 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:8.2 AVERAGE O2:8.3 AVERAGE O2:8.3
AVERAGE CO2:7.1 AVERAGE CO2:7.1 AVERAGE CO2:7.1
BARO PRESSURE:24.22 BARO PRESSURE:24.22 BARO PRESSURE:24.23
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 0.512 0.58 587 0.46 1 0.512 0.76 591 0.48 1 0.512 0.68 598 0.49
2 1.68 0.65 2 1.68 0.69 2 1.68 0.7
3 3.104 0.66 3 3.104 0.66 3 3.104 0.77
4 5.168 0.67 4 5.168 0.74 4 5.168 0.86
5 10.832 0.7 5 10.832 1.01 5 10.832 0.98
6 12.896 0.78 6 12.896 1 6 12.896 1.02
7 14.32 0.82 7 14.32 0.94 7 14.32 1.04
8 15.488 0.78 8 15.488 0.91 8 15.488 0.92
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 0.512 0.8 587 0.46 1 0.512 0.67 591 0.48 1 0.512 0.71 598 0.49
2 1.68 0.69 2 1.68 0.69 2 1.68 0.76
3 3.104 0.71 3 3.104 0.78 3 3.104 0.79
4 5.168 0.74 4 5.168 0.91 4 5.168 0.84
5 10.832 0.86 5 10.832 0.95 5 10.832 0.99
6 12.896 0.97 6 12.896 0.94 6 12.896 1.01
7 14.32 0.87 7 14.32 0.9 7 14.32 1.02
8 15.488 0.82 8 15.488 0.88 8 15.488 0.94
9 9 9
10 10 10
11 11 11
12 12 12
13 13 13
14 14 14
15 15 15
16 16 16
Worksheet: O2 Stratification
Client:Scout
Location:Ashley CS C-4
Date:2024-11-13
PD:16
DD:72 YES Method 1 Criteria Met
UD:200 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 2.66 8.20
A 2 8.00 8.30
A 3 13.33 8.30
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 8.27
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)