DAQ-2024-004315

1

DAQC-1322-23
Site ID: 15938 (B4)

MEMORANDUM

TO: STACK TEST FILE – UINTA WAX OPERATING, LLC – North Randlett
Compressor Station

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

FROM: Kyle Greenberg, Environmental Scientist

DATE: December 7, 2023

SUBJECT: Sources: Compressor Engine: Unit #4 Caterpillar G3516B; SN: JEF01634
Contact: Karen Pratt: 720-990-9927
Location: Remote location in Uintah County, UT
Test Contractor: Oasis Emissions Consultants, Inc.
Permit/AO#: Approval Order DAQE-AN159380001-19 dated March 28, 2019
Action Code: TR
Subject: Review of Stack Test Reports dated November 6, 2023

On November 6, 2023, Utah Division of Air Quality (DAQ) received a test report for the above listed
unit. Testing was performed on October 16, 2023, to demonstrate compliance with the emission limits
found in Condition II.B.2.b of Approval Order DAQE-AN159380001-19 and 40 CFR Part 60 Subpart
JJJJ. The DAQ calculated test results are:

Source Test Date Test
Method
Pollutant Tester
Results
DAQ Results Limits
Unit ID: #4
SN: JEF01634
Oct. 16,
2023
320 NOx
0.38 g/bhp-hr
1.12 lb/hr
32.20 ppmvd
@15% O2
0.380 g/bhp-hr
1.114 lb/hr
32.201 ppmvd
@15% O2
1.0 g/bhp-hr
1.52 lb/hr
41 ppmvd
@15% O2
320 CO
0.03 g/bhp-hr
0.10 lb/hr
4.57 ppmvd
@15% O2
0.033 g/bhp-hr
0.096 lb/hr
4.572 ppmvd
@15% O2
2.0 g/bhp-hr
1.37 lb/hr
61 ppmvd
@15% O2
320 VOC
0.32 g/bhp-hr
0.93 lb/hr
27.94 ppmvd
@15% O2
0.316 g/bhp-hr
0.926 lb/hr
27.940 ppmvd
@15% O2
0.7 g/bhp-hr
2.13 lb/hr
60 ppmvd
@15% O2

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The emissions from Unit 4 should be considered to have been in
compliance with the emission limits of the AO and 40 CFR Part 60
subpart JJJJ during the stack test.

2

HPV: N/A

ATTACHMENTS: DAQ Stack Test Review Excel Spreadsheets, Uinta Wax Operating,
LLC’s Stack Test Reports.

Emissions
Uinta Wax Operating, LLC
North Randlett Compressor Station
Uintah County, Utah
Compressor Engine E4 SN: JEF01634
Test Date: 10/16/23
Run #1 2 3 Average
Start Time 7:18 8:18 9:18
Stop Time 8:17 9:17 9:17
Sample Duration (minutes)60 60 60
BHP Engine Load - Actual (bhp) 1325 1325 1339 1329
DS Stack Diameter (inches)14.0 14.0 14.0 14.0
PAVG Average (Delta P)½ (" H2O)½1.2600 1.3220 1.3310 1.3043
CP Pitot Tube Constant (unitless)0.84 0.84 0.84 0.84
TS Stack Temperature (°F)656 663 672 664
Pbar Barometric Pressure (" Hg)25.40 25.42 25.42 25.41
Ps Stack Pressure ('' H2O)0.76 0.70 0.72 0.73
O2%vd O2 (%vd)10.3 10.3 10.3 10.3
CO2%vd CO2 (%vd)6.3 6.3 6.3 6.3
N2%vd N2 (%vd)83.4 83.4 83.4 83.4
dry NOX (ppmvd)57.7 57.9 58.0 57.9
dry CO (ppmvd) 8.2 8.3 8.2 8.2
wet NMNEOC (ppmvd as C3H8)49.5 50.2 50.9 50.2
Run #1 2 3 Average
Bws Measured Moisture Content (%/100)0.092 0.108 0.111 0.104
Bws Saturated Moisture Content (%/100)179.554 187.684 198.652 188.630
Bws Actual Moisture Content (%/100)0.092 0.108 0.111 0.104
MD Molecular Weight Dry (lb/lb-mole)29.42 29.42 29.42 29.42
MA Molecular Weight Wet (lb/lb-mole)28.37 28.19 28.16 28.24
VS Gas Velocity (ft/sec)112.5 118.7 120.1 117.1
FACFM Gas Flow (acfm)7216 7616 7703 7512
FDSCFM Gas Flow (dscfm)2635 2718 2717 2690
FWSCFM Gas Flow (wscfm)2903 3047 3058 3003
FKWSCFH Gas Flow (kwscfh)174 183 183 180
FKWSCFM Gas Flow (kwscfm)3 3 3 3
lb/hr Gas Flow (lb/hr) 12828 13379 13408 13205
Fo Fo (unitless)1.683 1.683 1.683 1.683
wet O2 (%vw)9.4 9.2 9.2 9.2
wet CO2 (%vw)5.7 5.6 5.6 5.6
wet NOX (ppmvw)52.383 51.628 51.577 51.863
15 NOX (ppmvd @ 15% O2)32.110 32.205 32.289 32.201 41.0
lb/hr NOX (lb/hr)1.088 1.126 1.128 1.114 1.52
g/bhp-hr NOX (g/bhp-hr)0.373 0.385 0.382 0.380 1.0
wet CO (ppmvw) 7.418 7.397 7.273 7.363
15 CO (ppmvd @ 15% O2)4.547 4.614 4.553 4.572 61.0
lb/hr CO (lb/hr) 0.094 0.098 0.097 0.096 1.37
g/bhp-hr CO (g/bhp-hr) 0.032 0.034 0.033 0.033 2.0
dry NMEOC (ppmvd as C3H8)49.530 50.170 50.890 50.197
15 NMEOC (ppmvd as C3H8 @ 15% O2)27.569 27.925 28.326 27.940 60
lb/hr NMEOC (lb/hr as C3H8)0.895 0.935 0.948 0.926 2.13
g/bhp-hr NMEOC (g/bhp-hr as C3H8)0.306 0.320 0.321 0.316 0.7
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1

Source Test Report
For
Uinta Wax Operating, LLC
North Randlett Compressor Station
Uintah County, Utah

Test Date: October 16, 2023
Report Date: November 6, 2023

UDEQ Permit: #DAQE-AN159380001-19
Engine: Caterpillar G3516B
SN: JEF01634
Unit ID: #4

Prepared By:

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

November 6, 2023

Ms. Karen Pratt
Uinta Wax Operating, LLC

Dear Ms. Pratt:

Re: Engine Emission Testing For Uinta Wax Operating, LLC, North Randlett
Compressor Station, Unit #4, Permit #DAQE-AN159380001-19.

An air emissions test program was conducted on a Caterpillar G3516B engine, operated by
Uinta Wax Operating, LLC and designated as Unit #4, located at the North Randlett
Compressor Station in Uintah County, Utah. The purpose of the testing was to demonstrate
initial compliance with the emissions limits contained in UDEQ Permit #DAQE-
AN159380001-19 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 October 16, 2023.

UDEQ Permit #DAQE-AN159380001-19 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
ppm @
15% O2
32.20 41 4.57 61 27.94 60
lbs/hr 1.12 1.52 0.10 1.37 0.93 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 0.38 1.0 0.03 2.0 0.32 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)
877 4.2

Engine Load (Averaged Over 3 Test Runs)

Rated BHP Operating
BHP
% Load
1380 1329.4 96.3

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 Cember Crawley
Manager of Technical Services Environmental Scientist

_________________________

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

SOURCE EMISSION TEST REPORT

UDEQ Permit #DAQE-AN159380001-19

Test Performed By: Oasis Emission Consultants, Inc.

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

Owner/Operator: Uinta Wax Operating, LLC

Owner/Operator Contact: Karen Pratt
[phone]

Facility Name: North Randlett Compressor Station
Latitude: 40.223 Longitude: -109.899
Uintah County, Utah

Emission Source: Caterpillar G3516B
Unit #4

Date of Test: October 16, 2023

Date of Report: November 6, 2023

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 ..................................................................... 2
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 G3516B engine, operated by
Uinta Wax Operating, LLC and designated as Unit #4, located at the North Randlett
Compressor Station in Uintah County, Utah. The purpose of the testing was to demonstrate
initial compliance with the emissions limits contained in UDEQ Permit #DAQE-
AN159380001-19 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 five (5) miles west of Randlett, in Uintah County, Utah.
Latitude: 40.223 Longitude: -109.899

Three one hour test runs were performed on October 16, 2023 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
John Grady, Archrock

2

2.1 Stack Sampling Location

The facility is located five (5) miles west of Randlett, in Uintah County, Utah.
Latitude: 40.223 Longitude: -109.899

Testing was conducted on the Caterpillar G3516B engine. The sampling port for moisture,
NOx, CO and VOC measurements was approximately 3.4 pipe diameters (48”) downstream
from the nearest flow disturbance (Distance B) and 1.4 pipe diameters (20”) 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

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

14"
A
B

Oxidation
Catalyst
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 October 16, 2023 to analyze exhaust NOx, CO
and VOC (NMNEHC C3) emission levels to demonstrate initial compliance with the
emissions limits contained in the WDEQ Permit #DAQE-AN159380001-19 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 G3516B, NOx, CO and VOC

The first test was performed from 7:18 to 8:17 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1324.8 bhp, and the average NOx and CO levels were found to be 0.37 g/bhp-hr and
0.03 g/bhp-hr respectively, below limitations. The VOC level tested at 0.31 g/bhp-
hr, which tested in compliance.

3.1.2 Source Test 2: Caterpillar G3516B, NOx, CO and VOC

The second test was performed from 8:18 to 9:17 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1324.8 bhp, and the average NOx and CO levels were found to be 0.39 g/bhp-hr and
0.03 g/bhp-hr respectively, below limitations. The VOC level tested at 0.32 g/bhp-
hr, which tested in compliance.

3.1.3 Source Test 3: Caterpillar G3516B, NOx, CO and VOC

The third test was performed from 9:18 to 10:17 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1338.6 bhp, and the average NOx and CO levels were found to be 0.38 g/bhp-hr and
0.03 g/bhp-hr respectively, below limitations. The VOC level tested at 0.32 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 57.69 0.37 8.17 0.03 49.53 0.31 10.3
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
2 57.86 0.39 8.29 0.03 50.17 0.32 10.3
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
3 58.01 0.38 8.18 0.03 50.89 0.32 10.3
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). 10 December 2020. Web. 26 October 2023.
<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 & 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 86.3%, 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 48.905606 7.55399 56.459596 8.148797 49.359949 4.09796 7:18:24 10/16/2023
2 48.623147 7.628822 56.251969 8.053974 49.160088 5.190409 7:19:24 10/16/2023
3 48.408329 7.696061 56.10439 8.040519 49.489534 5.957427 7:20:24 10/16/2023
4 48.521234 7.768538 56.289772 7.993516 50.162364 5.942604 7:21:24 10/16/2023
5 49.827605 8.10639 57.933995 8.170579 48.993998 6.943234 7:22:24 10/16/2023
6 50.761155 8.343994 59.105149 8.184042 48.903737 7.091751 7:23:25 10/16/2023
7 50.454887 8.353353 58.80824 8.213744 49.243374 8.140546 7:24:25 10/16/2023
8 50.572346 8.462036 59.034382 8.259675 49.044434 7.565904 7:25:26 10/16/2023
9 50.766903 8.511895 59.278798 8.264207 48.716867 10.057193 7:26:26 10/16/2023
10 51.422638 8.526758 59.949396 8.383718 49.559106 15.145202 7:27:26 10/16/2023
11 50.716637 8.478314 59.194951 8.204628 48.655840 10.778828 7:28:26 10/16/2023
12 51.475173 8.8026 60.277773 8.266444 48.763389 9.288448 7:29:26 10/16/2023
13 51.327696 8.951297 60.278993 8.210821 48.924719 8.21694 7:30:27 10/16/2023
14 50.021247 8.805919 58.827166 8.101132 49.034318 7.656673 7:31:27 10/16/2023
15 49.832443 8.749702 58.582145 8.136043 49.421829 9.849403 7:32:27 10/16/2023
16 50.549685 9.107164 59.656849 8.241931 48.876094 11.894525 7:33:27 10/16/2023
17 49.793179 8.806057 58.599236 8.169455 49.120643 10.990619 7:34:27 10/16/2023
18 49.585541 8.825622 58.411163 8.191811 48.855123 8.171793 7:35:28 10/16/2023
19 49.670314 8.909003 58.579317 8.151178 48.727279 7.940623 7:36:28 10/16/2023
20 49.015831 8.905678 57.921509 8.158551 49.296238 7.904394 7:37:28 10/16/2023
21 48.374997 8.751361 57.126358 8.126695 49.192046 8.366771 7:38:28 10/16/2023
22 48.88297 8.890225 57.773195 8.126946 48.548888 8.367265 7:39:28 10/16/2023
23 49.100363 8.966018 58.066381 8.110142 49.124315 8.621633 7:40:29 10/16/2023
24 47.816628 8.779461 56.596089 8.101589 49.550931 8.628294 7:41:29 10/16/2023
25 48.400289 8.832378 57.232667 8.086106 49.004683 8.512829 7:42:29 10/16/2023
26 48.955495 8.957487 57.912982 8.144923 48.940695 8.873219 7:43:29 10/16/2023
27 48.524012 8.985419 57.509431 8.116814 48.754236 8.465088 7:44:29 10/16/2023
28 47.962038 9.221415 57.183453 8.035674 49.773177 16.735003 7:45:29 10/16/2023
29 49.021903 8.858549 57.880452 8.243422 49.223478 12.080823 7:46:30 10/16/2023
30 48.05583 8.761471 56.817301 8.070649 49.279293 9.235789 7:47:30 10/16/2023
31 49.289453 9.126894 58.416347 8.281207 50.034824 12.534601 7:48:30 10/16/2023
32 48.289145 8.963617 57.252762 8.165069 49.553367 10.651724 7:49:30 10/16/2023
33 47.935619 8.872446 56.808065 8.109869 49.685968 9.109723 7:50:30 10/16/2023
34 47.892177 9.006847 56.899024 8.080757 49.564147 8.922358 7:51:31 10/16/2023
35 47.295218 8.927886 56.223104 8.024185 49.599430 8.652965 7:52:31 10/16/2023
36 47.937802 9.054155 56.991957 8.10317 49.403123 8.553176 7:53:31 10/16/2023
37 47.747607 9.014127 56.761734 8.113956 49.347859 8.718685 7:54:31 10/16/2023
38 48.282742 9.134513 57.417255 8.165899 49.512725 9.048908 7:55:31 10/16/2023
39 47.210403 8.972536 56.182939 8.083557 49.895696 8.948504 7:56:31 10/16/2023
40 47.771733 9.052885 56.824618 8.082695 49.420225 8.765414 7:57:32 10/16/2023
41 48.638306 9.154728 57.793034 8.110449 49.002314 8.517484 7:58:32 10/16/2023
42 48.282392 9.167243 57.449635 8.12805 49.640134 9.130685 7:59:32 10/16/2023
43 47.11358 8.998594 56.112174 8.133384 50.057657 8.783141 8:00:32 10/16/2023
44 47.122213 9.012915 56.135128 8.120671 49.604359 8.483681 8:01:32 10/16/2023
45 47.259946 9.073464 56.33341 8.138622 49.534631 8.849213 8:02:32 10/16/2023
46 48.182846 9.266814 57.44966 8.219713 50.017122 8.379328 8:03:33 10/16/2023
47 48.202678 9.297597 57.500275 8.17071 50.499150 8.508071 8:04:33 10/16/2023
48 48.080024 9.128907 57.208931 8.291545 49.267637 16.171695 8:05:33 10/16/2023
49 47.711142 9.044733 56.755875 8.173407 50.018833 10.194606 8:06:33 10/16/2023
50 46.886213 9.034973 55.921186 8.081781 50.067540 8.547851 8:07:33 10/16/2023
51 47.262068 9.08588 56.347948 8.055027 49.485939 8.516492 8:08:33 10/16/2023
52 48.012163 9.156329 57.168492 8.064163 49.182039 8.553161 8:09:34 10/16/2023
53 49.054295 9.415415 58.46971 8.267487 49.967899 9.327141 8:10:34 10/16/2023
54 48.894845 9.401437 58.296282 8.283311 50.108497 9.013275 8:11:34 10/16/2023
55 48.885177 9.428904 58.314081 8.316938 50.584219 9.605717 8:12:34 10/16/2023
56 50.059396 9.57253 59.631926 8.301251 50.265274 9.039288 8:13:34 10/16/2023
57 50.17679 9.583329 59.760119 8.412623 51.227500 8.937066 8:14:34 10/16/2023
58 48.411215 9.378381 57.789596 8.261588 51.581523 8.647868 8:15:34 10/16/2023
59 47.947856 9.312175 57.260031 8.345322 51.343907 14.070593 8:16:35 10/16/2023
60 47.265403 9.200464 56.465867 8.235197 50.909866 10.185215 8:17:35 10/16/2023
AVG 48.81 8.89 57.69 8.17 49.53 9.20
ppm@15% O2 32.11 4.55 27.57
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 1.09 0.03 0.09 0.31 0.90
#4
FTIR Measurements
Calculated Emission Levels
Uinta Wax Operating, LLC
North Randlett Compressor Station
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 1.38 1115 0.76 1.175
Average O2 10.3 (% dry)A 2 1.47 1.34 1115 0.76 1.158
Average CO2 6.3 (% dry)A 3 2.72 1.28 1115 0.76 1.131
Average N2 + CO 83.4 (% dry)A 4 4.52 1.37 1115 0.76 1.170
Dry Molecular Weight 29.42 lb/lbmol A 5 9.48 1.33 1115 0.76 1.153
Wet Molecular Weight 28.37 lb/lbmol A 6 11.28 1.39 1115 0.76 1.179
EPA REFERENCE METHOD 320 A 7 12.53 1.40 1115 0.76 1.183
Barometric Pressure 25.4 in Hg A 8 13.50 1.35 1115 0.76 1.162
Moisture Content 9.20 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 57.69 ppm A 11
Calculated NOx Mass Output 1.09 lbs/hr A 12
Calculated NOx Output 0.37 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 8.17 ppm A 15
Calculated CO Mass Output 0.09 lbs/hr A 16
Calculated CO Output 0.03 g/bhp-hr B 1 0.50 1.86 1115 0.76 1.364
EPA REFERENCE METHOD 320 B 2 1.47 1.83 1115 0.76 1.353
Average Analyzer NMNEHC Level 49.53 ppm B 3 2.72 1.91 1115 0.76 1.382
Calculated NMNEHC Mass Output 0.90 lbs/hr B 4 4.52 1.99 1115 0.76 1.411
Calculated NMNEHC Output 0.31 g/bhp-hr B 5 9.48 1.90 1115 0.76 1.378
LOAD APPROXIMATION B 6 11.28 1.86 1115 0.76 1.364
Estimated Engine Load 1324.8 BHP B 7 12.53 1.74 1115 0.76 1.319
B 8 13.50 1.65 1115 0.76 1.285
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 1.6 1115 0.8 1.260
Average Stack Gas Velocity 112.47 ft/sec
Average Dry Flowrate 2638.93 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 47.79369 9.146399 56.940089 8.150852 50.850042 8.921363 8:18:35 10/16/2023
2 48.264218 9.323583 57.587801 8.216217 50.028631 9.77019 8:19:35 10/16/2023
3 48.477864 9.500233 57.978097 8.336352 50.587666 12.975382 8:20:35 10/16/2023
4 47.199112 9.177459 56.376571 8.253349 50.291429 10.687014 8:21:35 10/16/2023
5 47.758988 9.209509 56.968497 8.274004 49.771187 11.305656 8:22:35 10/16/2023
6 48.655549 9.34078 57.996329 8.270542 49.536330 9.99733 8:23:36 10/16/2023
7 48.681925 9.506512 58.188437 8.338978 49.750247 15.328558 8:24:36 10/16/2023
8 47.537701 9.203588 56.741289 8.196112 49.690874 10.995399 8:25:36 10/16/2023
9 48.65576 9.36226 58.01802 8.304257 49.481342 11.570905 8:26:36 10/16/2023
10 47.802517 9.328812 57.131329 8.293403 49.253184 10.846695 8:27:36 10/16/2023
11 47.795673 9.296196 57.091869 8.228944 49.586014 11.54986 8:28:36 10/16/2023
12 48.458051 9.476729 57.93478 8.283557 49.509004 12.634932 8:29:36 10/16/2023
13 47.44643 9.458557 56.904987 8.407739 50.335460 15.58655 8:30:37 10/16/2023
14 47.656386 9.271941 56.928327 8.290537 49.868652 11.964158 8:31:37 10/16/2023
15 48.115331 9.344488 57.459819 8.172836 49.522810 10.330266 8:32:37 10/16/2023
16 48.842371 9.563225 58.405596 8.277529 49.466111 10.317555 8:33:37 10/16/2023
17 48.109669 9.466002 57.575671 8.262977 50.191211 10.487201 8:34:37 10/16/2023
18 49.585048 9.927942 59.51299 8.481276 50.186899 15.570559 8:35:37 10/16/2023
19 48.001607 9.38587 57.387477 8.2392 50.025315 11.427051 8:36:38 10/16/2023
20 47.888654 9.437669 57.326323 8.223956 49.911523 10.171996 8:37:38 10/16/2023
21 47.524541 9.356221 56.880762 8.197493 50.268847 10.438161 8:38:38 10/16/2023
22 48.409972 9.590073 58.000045 8.206981 49.920168 10.08684 8:39:38 10/16/2023
23 47.93256 9.464742 57.397302 8.173021 50.302735 10.07592 8:40:38 10/16/2023
24 47.945492 9.494457 57.439949 8.21709 49.938750 10.371666 8:41:38 10/16/2023
25 48.44483 9.673402 58.118232 8.336285 51.000049 9.859627 8:42:38 10/16/2023
26 48.092688 9.611087 57.703775 8.330449 51.381760 9.637317 8:43:38 10/16/2023
27 48.634906 9.652127 58.287033 8.372045 51.309397 9.983644 8:44:39 10/16/2023
28 49.393398 9.764704 59.158102 8.347413 50.975376 10.063847 8:45:39 10/16/2023
29 48.566627 9.681388 58.248015 8.339109 51.097845 9.720075 8:46:39 10/16/2023
30 49.000194 9.78306 58.783254 8.336917 51.007604 9.906536 8:47:39 10/16/2023
31 48.873145 9.691555 58.5647 8.301007 51.024684 9.902514 8:48:39 10/16/2023
32 48.749034 9.731317 58.480351 8.326538 51.280064 9.9072 8:49:39 10/16/2023
33 48.949269 9.727943 58.677212 8.34982 50.983601 10.30751 8:50:39 10/16/2023
34 48.402754 9.683676 58.08643 8.35749 50.947704 10.211178 8:51:40 10/16/2023
35 49.161435 9.787983 58.949418 8.395117 50.837826 10.210335 8:52:40 10/16/2023
36 48.822 9.727605 58.549605 8.367111 50.860601 10.474283 8:53:40 10/16/2023
37 48.423248 9.643532 58.06678 8.334371 50.779501 10.232534 8:54:40 10/16/2023
38 48.358689 9.665768 58.024457 8.362731 50.672935 10.56858 8:55:40 10/16/2023
39 48.72817 9.802196 58.530366 8.344973 50.626042 10.275512 8:56:40 10/16/2023
40 48.525833 9.703375 58.229208 8.376541 51.115223 10.049618 8:57:40 10/16/2023
41 49.29307 9.814346 59.107416 8.365363 50.987752 10.414642 8:58:41 10/16/2023
42 48.293162 9.622875 57.916037 8.349488 50.965780 10.236351 8:59:41 10/16/2023
43 49.42442 9.880285 59.304705 8.398901 50.518085 10.958614 9:00:41 10/16/2023
44 48.20808 9.622871 57.830951 8.223159 49.619981 10.869567 9:01:41 10/16/2023
45 47.959676 9.621531 57.581207 8.242287 49.675291 10.164198 9:02:41 10/16/2023
46 48.405004 9.588052 57.993056 8.244398 49.401927 10.083563 9:03:41 10/16/2023
47 47.775283 9.598554 57.373837 8.280381 49.341049 10.072326 9:04:41 10/16/2023
48 48.140383 9.622179 57.762562 8.269906 49.692155 10.09697 9:05:42 10/16/2023
49 48.745143 9.70838 58.453523 8.252007 49.785936 10.149035 9:06:42 10/16/2023
50 48.071642 9.646055 57.717697 8.218915 49.435048 10.203401 9:07:42 10/16/2023
51 48.180588 9.642392 57.82298 8.242298 48.919539 10.344883 9:08:42 10/16/2023
52 47.513877 9.496784 57.010661 8.190995 49.821785 10.712335 9:09:42 10/16/2023
53 48.53444 9.715141 58.249581 8.269403 49.280496 11.099366 9:10:42 10/16/2023
54 48.352212 9.715216 58.067428 8.368485 50.007905 13.27635 9:11:42 10/16/2023
55 47.640743 9.517679 57.158422 8.266349 49.834993 10.972231 9:12:43 10/16/2023
56 48.6464 9.660452 58.306852 8.241986 49.106164 10.978344 9:13:43 10/16/2023
57 47.767526 9.676138 57.443664 8.258852 49.300190 10.461298 9:14:43 10/16/2023
58 47.376149 9.558928 56.935077 8.226371 49.584580 10.383936 9:15:43 10/16/2023
59 47.580796 9.619295 57.200091 8.238231 50.101927 10.12258 9:16:43 10/16/2023
60 47.849666 9.617698 57.467364 8.189796 50.346819 9.845213 9:17:43 10/16/2023
AVG 48.29 9.57 57.86 8.29 50.17 10.77
ppm@15% O2 32.20 4.61 27.92
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.39 1.13 0.03 0.10 0.32 0.94
Calculated Emission Levels
Record Date
Uinta Wax Operating, LLC
North Randlett Compressor Station
Run 2
#4
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 1.53 1122 0.70 1.237
Average O2 10.3 (% dry)A 2 1.47 1.59 1122 0.70 1.261
Average CO2 6.3 (% dry)A 3 2.72 1.59 1122 0.70 1.261
Average N2 + CO 83.4 (% dry)A 4 4.52 1.75 1122 0.70 1.323
Dry Molecular Weight 29.42 lb/lbmol A 5 9.48 1.78 1122 0.70 1.334
Wet Molecular Weight 28.19 lb/lbmol A 6 11.28 1.89 1122 0.70 1.375
EPA REFERENCE METHOD 320 A 7 12.53 1.97 1122 0.70 1.404
Barometric Pressure 25.42 in Hg A 8 13.50 1.82 1122 0.70 1.349
Moisture Content 10.77 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 57.86 ppm A 11
Calculated NOx Mass Output 1.13 lbs/hr A 12
Calculated NOx Output 0.39 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 8.29 ppm A 15
Calculated CO Mass Output 0.10 lbs/hr A 16
Calculated CO Output 0.03 g/bhp-hr B 1 0.50 1.87 1122 0.70 1.367
EPA REFERENCE METHOD 320 B 2 1.47 1.92 1122 0.70 1.386
Average Analyzer NMNEHC Level 50.17 ppm B 3 2.72 1.83 1122 0.70 1.353
Calculated NMNEHC Mass Output 0.94 lbs/hr B 4 4.52 1.72 1122 0.70 1.311
Calculated NMNEHC Output 0.32 g/bhp-hr B 5 9.48 1.91 1122 0.70 1.382
LOAD APPROXIMATION B 6 11.28 1.98 1122 0.70 1.407
Estimated Engine Load 1324.8 BHP B 7 12.53 1.47 1122 0.70 1.212
B 8 13.50 1.40 1122 0.70 1.183
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 1.8 1122 0.7 1.322
Average Stack Gas Velocity 118.64 ft/sec
Average Dry Flowrate 2720.16 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 47.731575 9.652296 57.383871 8.191684 49.671930 9.804824 9:18:43 10/16/2023
2 47.782752 9.729142 57.511894 8.192901 50.053934 9.809826 9:19:44 10/16/2023
3 48.054291 9.717917 57.772208 8.13889 49.662412 9.999238 9:20:44 10/16/2023
4 47.717104 9.712692 57.429796 8.214245 49.312987 10.438407 9:21:44 10/16/2023
5 47.451031 9.674015 57.125046 8.180936 49.987649 10.625333 9:22:44 10/16/2023
6 48.204542 9.675382 57.879924 8.18871 49.505783 10.917249 9:23:44 10/16/2023
7 47.644305 9.655192 57.299497 8.138639 49.052977 10.910737 9:24:44 10/16/2023
8 46.851938 9.633798 56.485736 8.16175 48.635677 12.98854 9:25:44 10/16/2023
9 47.388213 9.550409 56.938622 8.27273 49.335987 11.475862 9:26:44 10/16/2023
10 47.242078 9.513782 56.75586 8.210736 49.082826 11.32564 9:27:45 10/16/2023
11 47.41413 9.660713 57.074843 8.178219 51.251258 11.005782 9:28:45 10/16/2023
12 47.427044 9.671654 57.098698 8.137674 48.907350 11.135647 9:29:45 10/16/2023
13 47.07795 9.670207 56.748157 8.141424 50.265318 11.036733 9:30:45 10/16/2023
14 47.763401 9.716628 57.480029 8.14734 49.240779 11.001923 9:31:45 10/16/2023
15 47.669455 9.747919 57.417374 8.179881 50.314977 11.215068 9:32:45 10/16/2023
16 47.530021 9.651439 57.18146 8.16237 50.403016 10.937028 9:33:45 10/16/2023
17 47.67126 9.750017 57.421277 8.208422 51.216066 10.775922 9:34:46 10/16/2023
18 47.504768 9.641754 57.146522 8.209926 51.560366 11.025872 9:35:46 10/16/2023
19 49.602974 9.954584 59.557558 8.160052 50.668660 11.224287 9:36:46 10/16/2023
20 48.690472 9.76139 58.451862 8.157153 51.200520 11.225754 9:37:46 10/16/2023
21 47.541085 9.595314 57.136399 8.123322 51.851953 11.416757 9:38:46 10/16/2023
22 47.743638 9.550602 57.29424 8.149751 52.132568 11.354936 9:39:46 10/16/2023
23 48.372622 9.673018 58.04564 8.147764 52.009044 11.49466 9:40:46 10/16/2023
24 49.156567 9.770267 58.926834 8.131966 51.886121 11.379104 9:41:47 10/16/2023
25 49.402234 9.922275 59.324509 8.166376 52.129957 11.399993 9:42:47 10/16/2023
26 49.10841 9.761181 58.869591 8.246373 52.122888 11.329417 9:43:47 10/16/2023
27 48.400691 9.74029 58.140981 8.222056 53.311394 12.083754 9:44:47 10/16/2023
28 48.973426 9.898386 58.871812 8.222291 52.874464 13.645366 9:45:47 10/16/2023
29 50.064835 9.88906 59.953895 8.185626 52.558625 11.417455 9:46:47 10/16/2023
30 49.966273 9.977563 59.943836 8.232267 52.763547 11.42148 9:47:47 10/16/2023
31 48.840842 9.849735 58.690577 8.141987 53.656895 11.449989 9:48:48 10/16/2023
32 49.354969 9.886896 59.241865 8.21902 53.595477 11.282676 9:49:48 10/16/2023
33 48.97941 9.860077 58.839487 8.160385 53.214514 11.032719 9:50:48 10/16/2023
34 48.625381 9.874475 58.499856 8.174846 54.014025 10.853008 9:51:48 10/16/2023
35 48.161551 9.798612 57.960163 8.174374 54.767132 10.891078 9:52:48 10/16/2023
36 47.804368 9.681762 57.48613 8.210587 54.821165 11.091051 9:53:48 10/16/2023
37 47.697695 9.703231 57.400926 8.129205 54.834350 11.273607 9:54:48 10/16/2023
38 48.910135 9.96446 58.874595 8.145783 54.195584 11.431993 9:55:49 10/16/2023
39 49.0922 9.939188 59.031388 8.227381 54.718958 11.448875 9:56:49 10/16/2023
40 48.120482 9.744153 57.864635 8.220153 55.289726 11.459923 9:57:49 10/16/2023
41 49.256928 9.974363 59.231291 8.208673 54.489496 11.491619 9:58:49 10/16/2023
42 49.901657 10.06294 59.964597 8.250403 54.524869 11.539805 9:59:49 10/16/2023
43 49.288271 10.004901 59.293172 8.191364 54.866286 11.489763 10:00:49 10/16/2023
44 49.384877 10.095144 59.480021 8.179062 54.516138 11.358307 10:01:49 10/16/2023
45 48.202962 9.924211 58.127173 8.193565 55.971067 11.284526 10:02:49 10/16/2023
46 47.036081 9.686099 56.72218 8.198362 56.334879 11.18811 10:03:50 10/16/2023
47 48.281665 9.918246 58.199911 8.21688 55.697735 11.057198 10:04:50 10/16/2023
48 47.683149 9.807859 57.491008 8.169984 56.044409 10.624247 10:05:50 10/16/2023
49 47.024521 9.787766 56.812287 8.112544 55.758857 10.394568 10:06:50 10/16/2023
50 47.635738 9.850706 57.486444 8.246383 55.932449 10.301796 10:07:50 10/16/2023
51 47.59234 9.839231 57.431571 8.188581 55.914882 10.209658 10:08:50 10/16/2023
52 48.337233 10.018859 58.356092 8.212586 55.529843 10.384106 10:09:50 10/16/2023
53 48.520685 10.066938 58.587623 8.181073 55.498718 10.720773 10:10:51 10/16/2023
54 48.776436 10.114671 58.891107 8.206504 55.973827 10.853205 10:11:51 10/16/2023
55 49.374249 10.209065 59.583314 8.249203 55.325978 11.08591 10:12:51 10/16/2023
56 47.892396 10.034302 57.926698 8.162298 55.607692 11.121745 10:13:51 10/16/2023
57 47.238666 9.8326 57.071266 8.180443 56.113687 10.940152 10:14:51 10/16/2023
58 47.840416 9.824412 57.664828 8.210099 55.806601 10.396497 10:15:51 10/16/2023
59 47.789482 9.843825 57.633307 8.106903 56.380983 10.295997 10:16:51 10/16/2023
60 46.490112 9.593884 56.083996 8.133007 55.880593 10.678071 10:17:52 10/16/2023
AVG 48.20 9.81 58.01 8.18 50.89 11.09
ppm@15% O2 32.29 4.55 28.33
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.38 1.13 0.03 0.10 0.32 0.95
FTIR Measurements
#4
Calculated Emission Levels
Uinta Wax Operating, LLC
North Randlett Compressor Station
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 1.48 1131 0.72 1.217
Average O2 10.3 (% dry)A 2 1.47 1.67 1131 0.72 1.292
Average CO2 6.3 (% dry)A 3 2.72 1.69 1131 0.72 1.300
Average N2 + CO 83.4 (% dry)A 4 4.52 1.99 1131 0.72 1.411
Dry Molecular Weight 29.42 lb/lbmol A 5 9.48 1.89 1131 0.72 1.375
Wet Molecular Weight 28.15 lb/lbmol A 6 11.28 1.96 1131 0.72 1.400
EPA REFERENCE METHOD 320 A 7 12.53 1.73 1131 0.72 1.315
Barometric Pressure 25.42 in Hg A 8 13.50 1.57 1131 0.72 1.253
Moisture Content 11.09 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 58.01 ppm A 11
Calculated NOx Mass Output 1.13 lbs/hr A 12
Calculated NOx Output 0.38 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 8.18 ppm A 15
Calculated CO Mass Output 0.10 lbs/hr A 16
Calculated CO Output 0.03 g/bhp-hr B 1 0.50 1.76 1131 0.72 1.327
EPA REFERENCE METHOD 320 B 2 1.47 1.84 1131 0.72 1.356
Average Analyzer NMNEHC Level 50.89 ppm B 3 2.72 1.63 1131 0.72 1.277
Calculated NMNEHC Mass Output 0.95 lbs/hr B 4 4.52 1.89 1131 0.72 1.375
Calculated NMNEHC Output 0.32 g/bhp-hr B 5 9.48 1.92 1131 0.72 1.386
LOAD APPROXIMATION B 6 11.28 1.93 1131 0.72 1.389
Estimated Engine Load 1338.6 BHP B 7 12.53 1.79 1131 0.72 1.338
B 8 13.50 1.67 1131 0.72 1.292
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 1.8 1131 0.7 1.331
Average Stack Gas Velocity 120.07 ft/sec
Average Dry Flowrate 2721.42 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) span CO ppm Dry CO2% 191C NOx Wet NOx Dry NM NE HC C3 Temp ( C )Pressure (atm)
10/16/2023 7:00:53 -0.112033 -0.067596 -0.062889 -0.017908 -0.201041 -0.160463 0.274525 -0.112695 -0.112624 0.010928 -0.179629 -0.179516 -0.011074 191.125397 1.098681
10/16/2023 7:01:01 -0.241397 -0.052825 -0.063479 -0.065197 -0.029808 0.253091 0.160055 -0.096489 -0.096427 0.000063 -0.294223 -0.294036 -0.005688 191.137054 1.098226
10/16/2023 7:01:08 -0.120825 -0.104509 -0.071702 -0.013142 -0.614322 -0.079401 0.437048 -0.157274 -0.157162 -0.003485 -0.225334 -0.225172 -0.010406 191.137054 1.097862
10/16/2023 7:01:16 -0.188709 -0.109448 -0.068318 0.016822 -0.2743 0.303652 0.210535 -0.075541 -0.075489 0.017527 -0.298157 -0.297953 -0.002622 191.137054 1.097693
10/16/2023 7:01:52 0 0 0 0 0 0 0 0 0 0 0 0 0 191.068466 1.096608
10/16/2023 7:02:06 -0.030669 0.009942 0.001544 0.043136 0.447751 0.087862 0.638679 0.039425 0.039425 -0.001946 -0.020727 -0.020727 0.018506 191.129639 1.095207
10/16/2023 7:02:13 0.049413 -0.010332 -0.002187 0.026755 0.020399 -0.065149 -0.175519 -0.009968 -0.009968 0.001736 0.039081 0.039081 0.004782 191.123428 1.094532
10/16/2023 7:02:21 0.152089 0.015855 0.00021 -0.044339 0.501132 -0.179149 0.633963 -0.060227 -0.060227 -0.002047 0.167944 0.167944 0.007807 191.073471 1.09436
10/16/2023 7:02:28 0.018364 -0.080138 0.001513 -0.023752 0.318904 0.210702 0.204051 0.193742 0.193745 0.001223 -0.061775 -0.061776 -0.001134 191.073471 1.093924
10/16/2023 7:02:36 0.044551 -0.002456 0.002261 0.012001 0.090939 0.466075 0.449891 0.076697 0.076699 0.006552 0.042095 0.042096 0.031684 191.073471 1.094037
10/16/2023 7:02:43 0.076306 -0.062594 -0.001315 -0.149228 0.361595 0.8491 0.022776 0.189575 0.189573 -0.003798 0.013712 0.013712 0.268876 191.073471 1.093267
10/16/2023 7:02:51 0.002782 -0.030366 -0.002857 0.02192 0.011732 0.163327 0.252131 0.086009 0.086006 0.007283 -0.027583 -0.027582 0.005263 191.073471 1.092911
10/16/2023 7:02:58 -0.021112 -0.008435 0.000742 -0.128506 0.516538 -0.115583 -0.021598 0.086539 0.08654 -0.001251 -0.029547 -0.029548 -0.00134 191.071655 1.092318
10/16/2023 7:03:06 0.012469 -0.094472 0.000756 -0.05402 0.124339 -0.274763 0.255003 0.061331 0.061331 0.003717 -0.082002 -0.082003 0.002493 191.058029 1.092266
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)
10/16/2023 7:03:27 469.55929 448.113717 463.80407 191.086182 1.038582 10/16/2023 7:06:41 94.320267 191.013077 1.007672
10/16/2023 7:03:35 500.555589 506.239311 504.599739 191.086182 0.993536 10/16/2023 7:06:48 97.489386 191.009888 1.008456
10/16/2023 7:03:42 501.068995 506.671754 505.577664 191.086182 0.993128 10/16/2023 7:06:56 97.129471 191.001724 1.008594
10/16/2023 7:03:50 501.23943 506.796928 505.226306 191.086182 0.992988 10/16/2023 7:07:03 97.322852 190.93541 1.008608
10/16/2023 7:03:57 500.811288 507.410122 504.708745 191.086182 0.992793 10/16/2023 7:07:11 97.696276 190.999557 1.008514
10/16/2023 7:04:05 501.213095 507.199831 507.620362 191.086182 0.992652 10/16/2023 7:07:19 97.645406 191.022614 1.008491
10/16/2023 7:04:12 501.007653 507.684069 505.359497 191.15976 0.992494 10/16/2023 7:07:26 97.383145 191.022614 1.008402
10/16/2023 7:04:20 502.01954 507.754958 505.308829 191.123428 0.992168 10/16/2023 7:07:34 96.95219 191.022614 1.008398
10/16/2023 7:04:27 500.850124 507.377884 508.531118 191.105255 0.99218 10/16/2023 7:07:41 97.591505 191.022614 1.00833
10/16/2023 7:04:35 500.65473 507.802727 506.618627 191.105255 0.991912 10/16/2023 7:07:49 97.520494 191.018066 1.00829
Date Time NO2 191C span Temp ( C )Pressure (atm)
10/16/2023 7:05:07 128.545979 191.080353 1.003139
10/16/2023 7:05:14 143.441694 191.041687 1.002493
10/16/2023 7:05:22 145.371518 191.087997 1.002338
10/16/2023 7:05:29 146.501454 191.054398 1.002318
10/16/2023 7:05:37 147.139521 191.053604 1.002194
10/16/2023 7:05:44 147.574341 190.995361 1.002074
10/16/2023 7:05:52 148.034794 191.031693 1.001905
10/16/2023 7:05:59 148.524054 191.067108 1.001712
10/16/2023 7:06:07 148.823726 191.034409 1.001621
10/16/2023 7:06:14 149.006632 190.990814 1.001452
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)
10/16/2023 7:08:15 64.064578 22.225825 32.462928 191.013077 0.989642 10/16/2023 7:09:56 94.969211 190.989227 1.015499
10/16/2023 7:08:23 403.710395 377.950408 378.816897 191.035324 0.994453 10/16/2023 7:10:04 97.721476 191.067108 1.016852
10/16/2023 7:08:30 445.303559 444.903777 449.054446 191.035324 0.994118 10/16/2023 7:10:11 97.541395 191.067108 1.016932
10/16/2023 7:08:38 445.822702 447.063316 447.844855 191.040085 0.994291 10/16/2023 7:10:19 97.550853 191.067108 1.01694
10/16/2023 7:08:45 446.391236 447.259863 447.280476 191.103439 0.99419 10/16/2023 7:10:26 98.074578 191.065521 1.016876
10/16/2023 7:08:53 446.545373 448.024352 450.380163 191.09436 0.994112 10/16/2023 7:10:34 97.36046 191.028061 1.016743
10/16/2023 7:09:01 446.881899 448.022385 449.651254 191.054398 0.994206 10/16/2023 7:10:41 97.07102 190.990814 1.016668
10/16/2023 7:09:08 445.181481 447.280402 447.823583 191.054398 0.994195 10/16/2023 7:10:49 97.546002 190.990814 1.016628
10/16/2023 7:09:16 462.278896 465.950562 463.920941 191.054398 1.001458 10/16/2023 7:10:56 97.443322 190.990814 1.01649
10/16/2023 7:09:23 495.714698 501.120524 499.057538 191.052017 0.997044 10/16/2023 7:11:04 97.362316 190.990814 1.016373
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)
10/16/2023 7:11:26 0.227416 -0.037338 -0.448556 0.054725 191.006256 1.009314
10/16/2023 7:11:34 0.148373 0.075847 -0.632808 -0.195595 191.086182 1.009363
10/16/2023 7:11:41 -0.005938 -0.040795 0.166836 0.056016 191.084595 1.009314
10/16/2023 7:11:49 0.374913 0.042006 0.041865 0.369205 191.058029 1.009242
10/16/2023 7:11:56 0.195489 0.143561 -0.038069 -0.363207 191.00354 1.009248
10/16/2023 7:12:04 0.020357 0.249554 0.05631 -0.213427 191.064728 1.009191
10/16/2023 7:12:12 0.059527 0.037398 0.008392 0.002165 191.096176 1.009116
10/16/2023 7:12:19 0.047383 0.066755 0.141055 -0.390756 191.061661 1.008907
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)
10/16/2023 7:14:20 6.153976 38.437675 190.990814 0.998167
10/16/2023 7:14:28 6.168336 37.693801 191.048035 0.997847
10/16/2023 7:14:35 6.142963 37.838917 191.041687 0.9977
10/16/2023 7:15:06 6.148052 38.179595 191.00354 0.997394
10/16/2023 7:15:13 6.152263 37.813291 190.997177 0.99715
10/16/2023 7:15:21 5.843463 54.693204 190.952667 0.997654
10/16/2023 7:15:28 0.925628 365.932192 191.00444 0.995793
10/16/2023 7:15:36 0.617723 392.494199 191.016251 0.994126
10/16/2023 7:15:43 4.999675 109.830955 191.016251 0.996025
10/16/2023 7:15:51 5.507778 78.572095 191.016251 0.99676
10/16/2023 7:15:58 5.515533 76.913176 191.016251 0.996653
10/16/2023 7:16:06 5.521965 77.386682 191.014664 0.996414
10/16/2023 7:16:13 5.530889 76.39476 191.066208 0.996487
10/16/2023 7:16:21 5.554994 76.235695 191.035324 0.99661
10/16/2023 7:16:51 5.563156 73.182683 191.018036 0.996998
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)
10/16/2023 10:30:28 431.178662 433.554346 423.208939 191.035324 1.006845 10/16/2023 10:24:52 96.858485 190.971741 0.991918
10/16/2023 10:30:35 478.702123 483.403311 477.378307 191.035324 1.004013 10/16/2023 10:24:59 98.672501 190.971741 1.009274
10/16/2023 10:30:43 480.666147 485.286286 480.139783 191.035324 1.003798 10/16/2023 10:25:07 98.030772 190.971741 1.009248
10/16/2023 10:30:51 480.993167 484.892084 479.907593 191.035324 1.003683 10/16/2023 10:25:14 98.547789 190.971741 1.009228
10/16/2023 10:30:58 480.37489 484.48823 479.06289 190.990814 1.003316 10/16/2023 10:25:22 98.151327 190.971741 1.009061
10/16/2023 10:31:06 480.609807 484.566881 479.261142 190.939957 1.003024 10/16/2023 10:25:29 98.676145 190.971741 1.009033
10/16/2023 10:31:13 487.856833 490.202864 483.997851 190.939957 1.019453 10/16/2023 10:25:37 98.178532 190.971741 1.008818
10/16/2023 10:31:21 493.489959 496.747127 489.499586 190.939957 1.021439 10/16/2023 10:25:44 98.785302 190.971741 1.008737
10/16/2023 10:31:28 493.593556 496.443285 489.883308 190.939957 1.021194 10/16/2023 10:25:52 98.295876 190.971741 1.008544
10/16/2023 10:31:36 493.659422 495.838652 487.967479 190.939957 1.020698 10/16/2023 10:25:59 98.763932 190.971741 1.008347
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)
10/16/2023 10:25:07 -0.02741 0.028312 -0.574612 190.971741 1.009248 10/16/2023 10:32:14 0.670716 190.939957 1.029374
10/16/2023 10:25:14 0.054051 0.082786 0.013755 190.971741 1.009228 10/16/2023 10:32:22 0.075089 190.939957 1.029446
10/16/2023 10:25:22 -0.080809 0.012998 -0.751462 190.971741 1.009061 10/16/2023 10:32:29 -0.028888 190.939957 1.029106
10/16/2023 10:25:29 0.054826 0.335749 -0.024904 190.971741 1.009033 10/16/2023 10:32:37 0.219021 190.939957 1.029087
10/16/2023 10:25:37 -0.097789 0.253527 0.261675 190.971741 1.008818 10/16/2023 10:32:44 0.344512 190.939957 1.028766
10/16/2023 10:25:44 0.035284 0.217661 -0.389593 190.971741 1.008737 10/16/2023 10:32:52 0.532106 190.939957 1.028641
10/16/2023 10:25:52 0.19561 0.018118 -0.401205 190.971741 1.008544 10/16/2023 10:32:59 0.755312 190.939957 1.028462
10/16/2023 10:25:59 0.153278 0.108172 -0.640693 190.971741 1.008347 10/16/2023 10:33:07 0.88685 190.939957 1.028347
SAMPLE SPIKE RECOVERY
POST SYSTEM CAL
POST SYSTEM ZERO
PRE TEST 1 508.7 6.1 37.8 5.6 76.2 0.096 86.3%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 507.8 509.3 0.0 -0.29 0.00
CO 500.7 506.0 0.1 -1.06 0.01
Propane 506.6 508.7 0.2 -0.41 0.03
Ethylene 97.5 99.84 0.3 -2.32 0.28
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 501.1 509.3 0.1 -1.61 0.01
CO 495.7 506.0 0.2 -2.03 0.03
Propane 499.1 508.7 -0.1 -1.90 -0.03
Ethylene*97.4 99.84 0.0 -2.48 -0.05
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 495.8 509.3 0.1 -2.64 0.03 1.04 0.01
CO 493.7 506.0 0.0 -2.44 0.00 0.41 0.04
Propane 488.0 508.7 -0.2 -4.08 -0.04 2.18 0.01
Ethylene*98.8 99.84 0.2 -1.08 0.24 1.40 0.29
*CTS Scans are conducted with Ethylene through the sample line.
Lf
10.00
Lr Cr Tr Pr Lr/Lf
10.15 97.5 191.0 1.0 1.02
Ls Cs Ts Ps Ls/Lf
10.09 97.4 191.0 1.0 1.01
% 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: 153-402600698-1
Cylinder Number: CC89245 Cylinder Volume: 144.0 CF
Laboratory: 124 - Tooele (SAP) - UT Cylinder Pressure: 2015 PSIG
PGVP Number: B72022 Valve Outlet: 660
Gas Code:CH4,CO,NO,NOX,PPN,BALN Certification Date: Dec 06, 2022
Expiration Date:Dec 06, 2030
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 509.3 PPM G1 +/- 0.6% NIST Traceable 11/29/2022, 12/06/2022
CARBON MONOXIDE 500.0 PPM 506.0 PPM G1 +/- 0.8% NIST Traceable 11/29/2022
METHANE 500.0 PPM 504.7 PPM G1 +/- 0.9% NIST Traceable 11/29/2022
NITRIC OXIDE 500.0 PPM 509.3 PPM G1 +/- 0.6% NIST Traceable 11/29/2022, 12/06/2022
PROPANE 500.0 PPM 508.7 PPM G1 +/- 0.7% NIST Traceable 11/29/2022
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NTRM 15060527 CC450559 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 08011609 K020818 496.5 PPM METHANE/NITROGEN 0.6%Aug 08, 2024
NTRM 15010116 KAL003474 494.6 PPM NITRIC OXIDE/NITROGEN 0.5%Aug 16, 2027
GMIS 1534012021103 ND73012 4.956 PPM NITROGEN DIOXIDE/NITROGEN 1.6%Jun 15, 2025
NTRM 12010921 ND46380 487 PPM PROPANE/AIR 0.6%Apr 24, 2024
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 Nov 03, 2022
Nicolet iS50 AUP2110269 CH4 M1CH4 FTIR Nov 16, 2022
Nicolet iS50 AUP2110269 NO MNO FTIR Nov 10, 2022
Nicolet iS50 AUP2110269 NO2 impurity FTIR NO2 impurity Nov 11, 2022
MKS FTIR C3H8 018143349 FTIR Nov 03, 2022
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: E02NI99E15W0051 Reference Number: 153-402674021-1
Cylinder Number: CC725232 Cylinder Volume: 144.0 CF
Laboratory: 124 - Tooele (SAP) - UT Cylinder Pressure: 2015 PSIG
PGVP Number: B72023 Valve Outlet: 660
Gas Code:NO2,BALN Certification Date: Mar 15, 2023
Expiration Date:Mar 15, 2026
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 148.6 PPM G1 +/- 2.0% NIST Traceable 03/07/2023, 03/15/2023
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
GMIS 1534012021601 CC502090 100.5 PPM NITROGEN DIOXIDE/NITROGEN 1.1%Dec 17, 2024
PRM 12389 D685050 99.0 PPM NITROGEN DIOXIDE/NITROGEN 1.0%Feb 19, 2020
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 Mar 09, 2023
Triad Data Available Upon Request
PERMANENT NOTES:OXYGEN ADDED TO MAINTAIN STABILITY
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: 153-402805170-1
Cylinder Number: EB0122984 Cylinder Volume:140.0 CF
Laboratory:124 - Tooele (SAP) - UT Cylinder Pressure:2015 PSIG
Analysis Date:Aug 01, 2023 Valve Outlet:350
Lot Number:153-402805170-1
Expiration Date: Aug 01, 2026
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 99.84 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
Finley – North Randlett CS
10-16-2023

Finley – North Randlett CS
10-16-2023

Finley – North Randlett CS
10-16-2023

Spectral Fit

Run 1

Spectral Fit

Run 2

Spectral Fit

Run 3

Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000140.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum\New FTIR 09-13-23\NEW FTIR 09-13-23_000003.LAB
Interferences Filenames: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000068.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000069.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000070.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000071.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000072.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000073.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000074.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_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 42.78 1.53 -0.18 0.25 2.08 2.08 -0.86 --0-2795 1.04 Good
NO2 191C 8.31 0.16 -0.02 0.02 0.17 0.17 -0.17 --0-488 1.02 Good
N2O 191C 0.08 0.18 0.17 0.02 0.02 0.21 0.21 0.2 0.2 0.03 0.06 0-200 -Close to DL
NH3 TE 191C -1.82 18.49 2.48 2.05 3.49 31.55 31.55 3.53 16.56 1.04 0.83 0-2995 -Close to DL
H2O% (HIGH) 191C8.52 0.13 -0.01 0.01 0.22 0.22 -0.17 --0-40 -Good
FORMALDEHYDE 191C3.47 0.7 2.37 0.13 0.15 0.79 0.79 2.61 2.61 0.23 0.79 0-69 -Close to DL
FORMIC ACID 191C TE0.11 11.98 1.37 0.7 0.82 14.03 14.03 1.9 11.3 0.53 0.46 0-466 -Close to DL
CH4 2900 CM-1 191C898.63 19.4 -0.84 1.22 35.93 35.93 -17.97 --0-3143 0.97 Good
PROPANE 191C36.95 1.44 -0.11 0.13 1.73 1.73 -0.77 --0-4976 0.96 Good
PROPYLENE 191C TE0.74 11.52 2.39 0.78 0.93 13.63 13.63 2.53 10.73 0.14 0.8 0-194 -Close to DL
ETHANE 191C 82.93 3.08 -0.26 0.4 4.8 4.8 -1.69 --0-1004 -Good
ETHYLENE 191C TE5.88 16.83 5.85 1.01 1.24 20.77 20.77 6.43 15.67 0.58 1.95 0-900 -Close to DL
CO PPM 191C (1OF2)7.42 0.67 -0.15 0.33 1.45 1.45 -0.34 --0-5010 1.03 Good
CO2% 191C 5.75 0.1 -0.01 0.01 0.14 0.14 -0.12 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C0.34 1.82 1.55 0.36 0.47 2.33 2.33 1.66 1.66 0.11 0.52 0-186 0.99 Close to DL
ACETYLENE 191C 0 1.86 0.65 0.36 0.48 2.46 2.46 0.75 1.52 0.1 0.22 0-1016 -Close to DL
SO2 191C 0.83 2.42 1.33 0.24 0.29 2.95 2.95 1.67 2.19 0.34 0.44 0-964 1.02 Close to DL
HEXANE 191C 2.3 0.94 2.54 0.06 0.09 1.27 1.27 2.82 2.82 0.28 0.85 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000200.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum\New FTIR 09-13-23\NEW FTIR 09-13-23_000003.LAB
Interferences Filenames: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000068.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000069.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000070.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000071.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000072.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000073.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000074.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_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 42.64 1.66 -0.18 0.25 2.26 2.26 -0.88 --0-2795 1.04 Good
NO2 191C 8.64 0.2 -0.02 0.02 0.22 0.22 -0.17 --0-488 1.02 Good
N2O 191C 0.07 0.2 0.17 0.02 0.02 0.23 0.23 0.2 0.2 0.03 0.06 0-200 -Close to DL
NH3 TE 191C -3.05 21.13 2.48 2.05 3.49 36.06 36.06 3.53 19.17 1.04 0.83 0-2995 -Close to DL
H2O% (HIGH) 191C10.34 0.17 -0.01 0.01 0.27 0.27 -0.21 --0-40 -Good
FORMALDEHYDE 191C3.97 0.71 2.37 0.13 0.15 0.8 0.8 2.61 2.61 0.23 0.79 0-69 -Close to DL
FORMIC ACID 191C TE0.16 12.19 1.37 0.7 0.82 14.27 14.27 1.9 11.5 0.53 0.46 0-466 -Close to DL
CH4 2900 CM-1 191C868.76 20.78 -0.84 1.22 38.51 38.51 -17.38 --0-3143 0.97 Good
PROPANE 191C35.71 1.48 -0.11 0.13 1.78 1.78 -0.78 --0-4976 0.96 Good
PROPYLENE 191C TE1.31 11.63 2.39 0.78 0.93 13.75 13.75 2.53 10.82 0.14 0.8 0-194 -Close to DL
ETHANE 191C 82.07 3.11 -0.26 0.4 4.84 4.84 -1.69 --0-1004 -Good
ETHYLENE 191C TE5.66 17.45 5.85 1.01 1.24 21.53 21.53 6.43 16.29 0.58 1.95 0-900 -Close to DL
CO PPM 191C (1OF2)7.44 0.73 -0.15 0.33 1.57 1.57 -0.38 --0-5010 1.03 Good
CO2% 191C 5.63 0.11 -0.01 0.01 0.15 0.15 -0.11 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C0.48 1.83 1.55 0.36 0.47 2.35 2.35 1.66 1.66 0.11 0.52 0-186 0.99 Close to DL
ACETYLENE 191C-0.16 1.99 0.65 0.36 0.48 2.63 2.63 0.75 1.64 0.1 0.22 0-1016 -Close to DL
SO2 191C 1.39 2.92 1.33 0.24 0.29 3.56 3.56 1.67 2.68 0.34 0.44 0-964 1.02 Close to DL
HEXANE 191C 2.26 0.95 2.54 0.06 0.09 1.28 1.28 2.82 2.82 0.28 0.85 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000260.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum\New FTIR 09-13-23\NEW FTIR 09-13-23_000003.LAB
Interferences Filenames: C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000068.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000069.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000070.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000071.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000072.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000073.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_000074.LAB
C:\OLT\Data\Finley\North Randlett U4 10-16-23\NORTH RANDLETT U4 10-16-23_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 42.18 1.66 -0.18 0.25 2.27 2.27 -0.88 --0-2795 1.04 Good
NO2 191C 8.83 0.22 -0.02 0.02 0.23 0.23 -0.18 --0-488 1.02 Good
N2O 191C 0.05 0.2 0.17 0.02 0.02 0.23 0.23 0.2 0.2 0.03 0.06 0-200 -Close to DL
NH3 TE 191C -3.31 25.2 2.48 2.05 3.49 43.01 43.01 3.53 23.23 1.04 0.83 0-2995 -Close to DL
H2O% (HIGH) 191C10.21 0.19 -0.01 0.01 0.31 0.31 -0.2 --0-40 -Good
FORMALDEHYDE 191C4.42 0.77 2.37 0.13 0.15 0.87 0.87 2.61 2.61 0.23 0.79 0-69 -Close to DL
FORMIC ACID 191C TE-1.08 12.59 1.37 0.7 0.82 14.74 14.74 1.9 11.88 0.53 0.46 0-466 -Close to DL
CH4 2900 CM-1 191C881.49 22.03 -0.84 1.22 40.81 40.81 -17.63 --0-3143 0.97 Good
PROPANE 191C36.09 1.56 -0.11 0.13 1.87 1.87 -0.81 --0-4976 0.96 Good
PROPYLENE 191C TE7.46 12.55 2.39 0.78 0.93 14.84 14.84 2.53 11.56 0.14 0.8 0-194 -Close to DL
ETHANE 191C 81.11 3.35 -0.26 0.4 5.21 5.21 -1.75 --0-1004 -Good
ETHYLENE 191C TE6.29 17.98 5.85 1.01 1.24 22.18 22.18 6.43 16.8 0.58 1.95 0-900 -Close to DL
CO PPM 191C (1OF2)7.4 0.74 -0.15 0.33 1.59 1.59 -0.39 --0-5010 1.03 Good
CO2% 191C 5.7 0.12 -0.01 0.01 0.16 0.16 -0.11 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C0.73 2 1.55 0.36 0.47 2.57 2.57 1.66 1.66 0.11 0.52 0-186 0.99 Close to DL
ACETYLENE 191C-0.06 2.37 0.65 0.36 0.48 3.13 3.13 0.75 2.02 0.1 0.22 0-1016 -Close to DL
SO2 191C 0.64 2.95 1.33 0.24 0.29 3.6 3.6 1.67 2.73 0.34 0.44 0-964 1.02 Close to DL
HEXANE 191C 1.53 0.96 2.54 0.06 0.09 1.3 1.3 2.82 2.82 0.28 0.85 0-1000 -Close to DL

APPENDIX C

Test Run Load %Site Rated Load, bhp Load Approx., bhp
1 96 1380 1324.8
2 96 1380 1324.8
3 97 1380 1338.6
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 2638.93 1324.8 10.3 57.69 0.37 1.09 8.17 0.03 0.09 49.53 0.31 0.90 9.20
2 2720.16 1324.8 10.3 57.86 0.39 1.13 8.29 0.03 0.10 50.17 0.32 0.94 10.77
3 2721.42 1338.6 10.3 58.01 0.38 1.13 8.18 0.03 0.10 50.89 0.32 0.95 11.09
1329.4 10.3 57.85 0.38 1.12 8.21 0.03 0.10 50.20 0.32 0.93 10.35
Summary
Average Levels
Example Calculations: Uinta Wax Operating, LLC, North Randlett Compressor Station,
#4

The following is a step-by-step calculation for the first test run conducted on the North Randlett
Compressor Station #4.

Test Parameters

• Stack Diameter = 14 inches
• Traverse Points = 16
• Ports = 2
• Barometric Pressure = 25.4 in Hg
• Average O2 = 10.3%
• Average CO2 = 6.3%
• Load Approximation = 1324.8 bhp
• Moisture Content = 9.20%

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 = 6.3%
%O2 – Oxygen Content Of The Gas = 10.3%
%N2 – Nitrogen Content Of The Gas
%CO – Carbon Monoxide Content Of The Gas

(%N2 +%CO) = (100 - %O2 - %CO2)

= (100 – 10.3 – 6.3)

= 83.4% Dry

= (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO))

= (0.44 * 6.3) + (0.32 * 10.3) + (0.28 * 83.4)

= 29.42 lb/lbmol

Wet Molecular Weight (lb/lbmol)
= MD * (1-BWS) + (18) * BWS

Where:
MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 29.42 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 9.20%

= MD * (1-BWS) + (18) * BWS

= 29.42 * (1 – (9.20/ 100)) + (18 * (9.20/ 100))

= 28.37 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) = 1.260 in H2O
TS – Average stack temperature (R) = 1115 R
PB – Barometric pressure (in Hg) = 25.4 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.8 in H2O
MA – Molecular weight of the wet gas (lb/lbmol) = 28.37 lb/lbmol

= Cp * (85.49) * ∆PAVG * (TS / (((PS / 13.6) + PB) * MA))

= 0.84 * (85.49) * 1.260 * ( 1115 / (((0.8/ 13.6) + 25.4) * 28.37))

= 112.47 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 (%) = 9.20%
TSTD – Standard temperature (528R)
TS – Average stack temperature (R) = 1115 R
PB – Barometric pressure (in Hg) = 25.4 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.8 in H2O
VS– Average Stack gas velocity (ft/sec) = 112.47 ft/sec

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

= 60 * (1 - (9.20/ 100)) * 112.47 *  * (((14 / 2) / 12))2) * 528 / 1115 * (25.4 + (0.8 /
13.6)) / 29.92

= 2638.93 dscfm

Conversion of Dry Flowrate to m3/hr
= Q * 60 * 2.83168*10 -2

Where:
Q – Volumetric Flowrate = 2638.93 dscfm
2.83168*10 -2 – Conversion factor for cubic feet to cubic meter
60 – Minutes in an hour

= Q * 60 * 2.83168*10 -2

= 2638.93 *60 * 2.83168*10 -2

= 4483.56 m3/hr

EPA Method 320: 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 = 57.69 ppm
1.92*10 -3 - Conversion constant for ppm to g/m3 NOx
Q – Volumetric Flowrate = 4483.56 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1324.8 Bhp

= (Cd * 1.912*10 -3 * Q * T) / HP-hr

= (57.69 * 1.912*10 -3 * 4483.56 * 1) / 1324.8

= 0.37 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.37 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1324.8 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.37 / 454 * 1324.8

= 1.09 lbs/hr

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

Where:
Cd – Measured CO concentration in ppm = 8.17 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 CO
Q – Volumetric Flowrate = 4483.56 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1324.8 Bhp

= (Cd * 1.164*10 -3 * Q * T) / HP-hr

= (8.17 * 1.164*10 -3 * 4483.56 * 1) / 1324.8

= 0.03 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.03 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1324.8 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.03 / 454 * 1324.8

= 0.09 lbs/hr

VOC Emission Rate (g/Bhp-hr)
= (Cd * 1.833*10 -3 * Q * T) / HP-hr

Where:
Cd – Measured VOC concentration in ppm = 49.53 ppm
1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – Volumetric Flowrate = 4483.56 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1324.8 Bhp

= (Cd * 1.833*10 -3 * Q * T) / HP-hr

= (49.53 * 1.833*10 -3 * 4483.56 * 1) / 1324.8

= 0.31 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.31 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 1324.8 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.31 / 454 * 1324.8

= 0.90 lbs/hr

APPENDIX E

FTIR Engine Test Sheet
Company Name ~I J11e-v
Location / Unit 1.0. R/o{+n R.. Cf YJoIle #-/:<s til.!
3X/fJr '~A/
Jordan Nix
John &-fCtdY nr~.J1rouf:..
Ir)//IJ /z..."3
Type of Test Completed
Field Technician (s)
Client Rep and/or State Rep
Date
Non-Resettable Run Time Hours In? ':;9­
Engine Make
Engine Model
Enoine SIN
Port Distance A
Port Distance B
Exhaust Diameter (inches)
Calibration Gas
NO (ppm) 509.3
CO (ppm)
CC89245
CC89245 506
Propane (ppm) 508.7
N02 (ppm)
CC89245
148.6
Ethylene (ppm)
CC725232
99.84
Methane (ppm)
EB0122984
CC89245 504.7
Acetaldehyde (ppm) 30.33SG9142412BAL
c-o r
1r-:5f>/6/A
JT.Fo /6 :5 '1
z, 0 I'"~" /eI"
Cvlinder# Concentration
Stack Diagram
"'~~~'»,=~~-'''''..~m,,',,''','_''.'''''',
-". T
t
A
"
'~\, ..
t 1 is
,.. --__1
Test 1 Test 2 Test 3
Time of Reading
Atm Pressure (in Hg)
o r-1"6
LtJ,tt
o <;JIZZ
Z-"7F, -z;; Z­
09/9
~L,?
Atm Temp CF) ~26 ~ ~/
Engine RPM /2--31) /'2.-~ i:=:­t! Z-".;. 1::::'
*Manifold Pres. Vac(") or Boos~) or Boost (psia) ~ ~. 3C1.. ~ 3~'~
Manifold Temp CF)
Psuction (psi) Stage 1
f3~
'Gf-
rs»
,4­
I <""T­
19­
Tsuction CF) Stage 1 -----... ~
Pdischarae (psi) Staae 1 '9:1=\ crF '"b~
Psuction (psi) Stage 2
Tsuction CF) Stage 2
l'""o­
"­-­-­--­------Pdischarae (psi) Staae 2 ;S~-r -~2..-L .5 7_ q
Psuction (psi) Stage 3
Tsuction CF) Stage 3
-..-.
,..-. --
'-­-Pdischarae (psi) Staae 3 ~::rO q~f.? 'Q66
Psuction (psi) Stage 4 I I
Tsuction ('F) Stage 4
Pdischarge (psi) Stage 4
Gas Throuohnut (mmcf/d\ or (,..-tQ55 tvet flow \ 16TIJ "3 tj 3<:~'-1 3<:;:;>«)
Pre CatTemp ('F) i:~ fl.6 <&2 J "'lf~Z;z
Post Cat Temp CF)
Cat Differential Pres. (n of H2O)
6")1;
?
~~"£.-.
't . z­
6
~
;2/
"f' 'l-
Humidity %
02%
C02 % Dry
LOAD % lJ'aiie1) or (Estimated)
Ignition Timing ('F)
I~H 7
6(J
I' .-3
.3
q6
tctJI
;;0
1/').3
&. 3
wt:
,l:j '..;z.
10, ~
"::;·3qr­
/
AFR Setting mV (Left Bank) Oe5 Ifj() If. to ~f>m
AFR Settina mV (Rlaht Bank) /IFf!.. 2,. -1' , 'Z
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'')
911712019
COMPANY NAME:Finley COMPANY LOCATION:North Randlett CS U4 DATE:10/16/2023
STACK DIAMETER (inches):14 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:10.3 AVERAGE O2:10.3 AVERAGE O2:10.3
AVERAGE CO2:6.3 AVERAGE CO2:6.3 AVERAGE CO2:6.3
BARO PRESSURE:25.4 BARO PRESSURE:25.42 BARO PRESSURE:25.42
Point Insertion DepthDP (H2O)Ts (deg F)Stat P (H2O)Point Insertion DepthDP (H2O)Ts (deg F)Stat P (H2O)Point Insertion DepthDP (H2O)Ts (deg F)Stat P (H2O)
1 0.5 1.38 655 0.76 1 0.5 1.53 662 0.7 1 0.5 1.48 671 0.72
2 1.47 1.34 2 1.47 1.59 2 1.47 1.67
3 2.716 1.28 3 2.716 1.59 3 2.716 1.69
4 4.522 1.37 4 4.522 1.75 4 4.522 1.99
5 9.478 1.33 5 9.478 1.78 5 9.478 1.89
6 11.284 1.39 6 11.284 1.89 6 11.284 1.96
7 12.53 1.4 7 12.53 1.97 7 12.53 1.73
8 13.5 1.35 8 13.5 1.82 8 13.5 1.57
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 1.86 655 0.076 1 0.5 1.87 662 0.7 1 0.5 1.76 671 0.72
2 1.47 1.83 2 1.47 1.92 2 1.47 1.84
3 2.716 1.91 3 2.716 1.83 3 2.716 1.63
4 4.522 1.99 4 4.522 1.72 4 4.522 1.89
5 9.478 1.9 5 9.478 1.91 5 9.478 1.92
6 11.284 1.86 6 11.284 1.98 6 11.284 1.93
7 12.53 1.74 7 12.53 1.47 7 12.53 1.79
8 13.5 1.65 8 13.5 1.4 8 13.5 1.67
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:Finley
Location:North Randlett CS U4
Date:10/16/2023
PD:14
DD:48 YES Method 1 Criteria Met
UD:20 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 2.32 10.30
A 2 7.00 10.30
A 3 11.66 10.30
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 10.30
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)