DAQ-2024-004300

1

DAQC-1305-23
Site ID 14408 (B4)
MEMORANDUM

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

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

FROM: Kyle Greenberg, Environmental Scientist

DATE: November 30, 2023

SUBJECT: Sources: Unit 1: Caterpillar G3516J SN: N6W01612
Contact: Jennifer McQueen 303-308-6285
Location: Uintah County, UT
Test Contractor: Oasis Emissions Consultants
Permit/AO#: DAQE-AN144080005-15, dated November 2, 2015
Action Code: TR
Subject: Review of Stack Test Report dated October 30, 2023

On October 30, 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 of the Approval Order DAQE-AN144080005-15 and 40 CFR Part 60, Subpart JJJJ. The
calculated test results are:

Source Test
Date
Test
Method
Pollutant Tester
Results
DAQ Results Limits
Unit: 1 SN:
N6W01612
Oct. 16,
2023
RM320/
ASTM
D6348-03
NOx
0.44 g/bhp-hr
0.78 lb/hr
0.442 g/bhp-hr
0.775 lb/hr
34.682 ppmvd
@ 15% O2
1.00 g/bhp-hr
3.04 lb/hr
82 ppmvd @
15% O2
CO 0.06 g/bhp-hr
0.10 lb/hr
0.059 g/bhp-hr
0.104 lb/hr
7.652 ppmvd
@ 15% O2
0.45 g/bhp-hr
1.37 lb/hr
270 ppmvd @
15% O2
VOC 0.25 g/bhp-hr
0.278 g/bhp-hr
22.814 ppmvd
@ 15% O2
0.7 g/bhp-hr
60 ppmvd @
15% O2

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: It is recommended the emissions from Unit 1 should be considered to
have been in compliance with the emission limits of the AO and 40 CFR
Part 60, Subpart JJJJ during the time of testing.

ATTACHMENTS: DAQ Stack Test Review Excel Spreadsheets, Crescent Point Energy
Source Test Reports

Emissions
Uinta Wax Operating LLC
Randlett Compressor Station
Uintah County, Utah
Unit 1; Caterpillar G3516J SN: N6W01612
Test Date: 10/16/23
Run #1 2 3 Average
Start Time 11:22 12:22 13:23
Stop Time 12:22 13:22 14:23
Sample Duration (minutes)60 60 60
BHP Engine Load - Actual (bhp) 800.4 800.4 786.6 796
DS Stack Diameter (inches)16.0 16.0 16.0 16.0
PAVG Average (Delta P)½ (" H2O)½0.5620 0.5760 0.5830 0.5737
CP Pitot Tube Constant (unitless)0.84 0.84 0.84 0.84
TS Stack Temperature (°F)503 506 508 506
Pbar Barometric Pressure (" Hg)25.30 25.29 25.28 25.29
Ps Stack Pressure ('' H2O)0.11 0.13 0.11 0.12
O2%vd O2 (%vd)9.8 9.8 9.8 9.8
CO2%vd CO2 (%vd)6.5 6.6 6.6 6.6
N2%vd N2 (%vd)83.7 83.6 83.6 83.6
dry NOX (ppmvd)65.4 65.4 65.0 65.3
dry CO (ppmvd) 14.5 14.4 14.3 14.4
wet NMEOC (ppmvw as C3H8)38.4 38.6 38.3 38.4
Run #1 2 3 Average
Bws Measured Moisture Content (%/100)0.100 0.107 0.109 0.105
Bws Saturated Moisture Content (%/100)56.645 58.191 59.253 58.029
Bws Actual Moisture Content (%/100)0.100 0.107 0.109 0.105
MD Molecular Weight Dry (lb/lb-mole)29.43 29.45 29.45 29.44
MA Molecular Weight Wet (lb/lb-mole)28.29 28.22 28.20 28.24
VS Gas Velocity (ft/sec)46.8 48.1 48.8 47.9
FACFM Gas Flow (acfm)3922 4031 4087 4013
FDSCFM Gas Flow (dscfm)1636 1662 1677 1658
FWSCFM Gas Flow (wscfm)1818 1862 1883 1855
FKWSCFH Gas Flow (kwscfh)109 112 113 111
FKWSCFM Gas Flow (kwscfm)2 2 2 2
lb/hr Gas Flow (lb/hr) 8010 8186 8271 8156
Fo Fo (unitless)1.708 1.682 1.682 1.690
wet O2 (%vw)8.823 8.750 8.730 8.768
wet CO2 (%vw)5.852 5.893 5.879 5.875
wet NOX (ppmvw)58.844 58.431 57.857 58.377
15 NOX (ppmvd @ 15% O2)34.741 34.783 34.523 34.682 82.0
lb/hr NOX (lb/hr)0.765 0.779 0.780 0.775 3.04
g/bhp-hr NOX (g/bhp-hr)0.434 0.441 0.450 0.442 1.0
wet CO (ppmvw) 13.018 12.885 12.738 12.880
15 CO (ppmvd @ 15% O2)7.686 7.670 7.601 7.652 270.0
lb/hr CO (lb/hr) 0.103 0.105 0.105 0.104 1.37
g/bhp-hr CO (g/bhp-hr) 0.058 0.059 0.060 0.059 0.45
dry NMEOC (ppmvd as C3H8)42.597 43.196 42.973 42.922
15 NMEOC (ppmvd as C3H8 @ 15% O2)22.642 22.960 22.841 22.814 60
lb/hr NMEOC (lb/hr as C3H8)0.478 0.492 0.494 0.488
g/bhp-hr NMEOC (g/bhp-hr as C3H8)0.271 0.279 0.285 0.278 0.7
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1

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

Test Date: October 16, 2023
Report Date: October 30, 2023

UDEQ Permit: #DAQE-AN144080005-15
Engine: Caterpillar G3516J
SN: N6W01612
Unit ID: #1

Prepared By:

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

October 30, 2023

Ms. Karen Pratt
Uinta Wax Operating, LLC

Dear Ms. Pratt:

Re: Engine Emission Testing For Uinta Wax Operating, LLC, Randlett Compressor
Station, Unit #1, Permit #DAQE-AN144080005-15.

An air emissions test program was conducted on a Caterpillar G3516J engine, operated by
Uinta Wax Operating, LLC and designated as Unit #1, located at the 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-AN144080005-15
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 October 16, 2023.

UDEQ Permit #DAQE-AN144080005-15 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
g/bhp-hr 0.44 1.0 0.06 0.45
lbs/hr 0.78 3.04 0.10 1.37

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 0.44 1.0 0.06 2.0 0.25 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)
978 9.2

Engine Load (Averaged Over 3 Test Runs)

Rated BHP Operating
BHP
% Load
1380 795.8 57.7

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-AN144080005-15

Test Performed By: Oasis Emission Consultants, Inc.

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

Owner/Operator: Uinta Wax Operating, LLC

Owner/Operator Contact: Karen Pratt
[phone]

Facility Name: Randlett Compressor Station
Latitude: 40.174 Longitude: -109.808
Uintah County, Utah

Emission Source: Caterpillar G3516J
Unit #1

Date of Test: October 16, 2023

Date of Report: October 30, 2023

TABLE OF CONTENTS

1.1 Introduction .......................................................................................................................... 1
2.1 Stack Sampling Location ..................................................................................................... 2
3.1 Discussion of NOx, CO and VOC Test Results ................................................................... 3
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

APPENDIX E: Field Notes

1

1.1 Introduction

An air emissions test program was conducted on a Caterpillar G3516J engine, operated by
Uinta Wax Operating, LLC and designated as Unit #1, located at the 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-AN144080005-15
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 SE¼ of Section 31, T3S, R2E, near Ft. Duchesne, in Uintah
County, Utah. Latitude: 40.174 Longitude: -109.808

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 dated February 2, 2023. 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

2

2.1 Stack Sampling Location

The facility is located in the SE¼ of Section 31, T3S, R2E, near Ft. Duchesne, in Uintah
County, Utah. Latitude: 40.174 Longitude: -109.808

Testing was conducted on the Caterpillar G3516J engine. The sampling port for moisture,
NOx, CO and VOC measurements was approximately 1.5 pipe diameters (24”) downstream
from the nearest flow disturbance (Distance B) and 2.3 pipe diameters (36”) 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

16"
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-AN144080005-15 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 11:22 to 12:21 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
800.4 bhp, and the average NOx and CO levels were found to be 0.43 g/bhp-hr and
0.06 g/bhp-hr respectively, below limitations. The VOC level tested at 0.24 g/bhp-
hr, which tested in compliance.

3.1.2 Source Test 2: Caterpillar G3516J, NOx, CO and VOC

The second test was performed from 12:22 to 13:22 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
800.4 bhp, and the average NOx and CO levels were found to be 0.44 g/bhp-hr and
0.06 g/bhp-hr respectively, below limitations. The VOC level tested at 0.25 g/bhp-
hr, which tested in compliance.

3.1.3 Source Test 3: Caterpillar G3516J, NOx, CO and VOC

The third test was performed from 13:23 to 14:22 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
786.6 bhp, and the average NOx and CO levels were found to be 0.45 g/bhp-hr and
0.06 g/bhp-hr respectively, below limitations. The VOC level tested at 0.25 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 65.36 0.43 14.46 0.06 38.35 0.24 9.8
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
2 65.44 0.44 14.43 0.06 38.57 0.25 9.8
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-hr)
CO
(ppmvd)
CO
(g/bhp-hr)
VOC
(ppmvd)
VOC
(g/bhp-hr)
O2
(%)
3 64.95 0.45 14.30 0.06 38.28 0.25 9.8
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. 27 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 70.0%, 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 43.275338 22.759437 66.034775 14.728815 38.101822 7.287944 11:22:50 10/16/2023
2 43.057397 22.995079 66.052476 14.692205 38.255028 7.325221 11:23:50 10/16/2023
3 42.111395 22.515671 64.627066 14.498109 37.708664 7.407307 11:24:51 10/16/2023
4 41.853384 22.359741 64.213125 14.478262 37.328283 7.915463 11:25:51 10/16/2023
5 43.004786 23.413474 66.41826 14.795625 38.074072 8.42268 11:26:51 10/16/2023
6 41.578929 22.97768 64.556609 14.42013 37.650732 8.151559 11:27:51 10/16/2023
7 42.368057 23.447453 65.81551 14.513986 37.737843 8.670038 11:28:51 10/16/2023
8 42.754172 23.767892 66.522064 14.660732 37.831086 8.613542 11:29:51 10/16/2023
9 42.682217 23.051243 65.73346 14.489815 37.673726 9.176422 11:30:52 10/16/2023
10 42.360901 22.602751 64.963652 14.452383 37.715086 9.083412 11:31:52 10/16/2023
11 43.328314 23.107954 66.436268 14.653769 37.902312 9.06053 11:32:52 10/16/2023
12 42.618721 22.692868 65.311589 14.595823 38.208042 9.344263 11:33:52 10/16/2023
13 42.892399 23.289506 66.181905 14.533817 38.062161 11.010739 11:34:52 10/16/2023
14 42.996873 22.975127 65.972 14.527889 38.629235 13.775602 11:35:52 10/16/2023
15 41.746506 22.839603 64.586109 14.297188 38.186876 9.095664 11:36:52 10/16/2023
16 42.659664 23.386968 66.046632 14.563866 38.459585 8.681236 11:37:53 10/16/2023
17 42.110102 23.169227 65.279329 14.51243 38.893615 8.911843 11:38:53 10/16/2023
18 42.227389 23.368979 65.596368 14.524149 38.506732 8.972535 11:39:53 10/16/2023
19 42.285834 23.361807 65.647641 14.465281 38.015652 9.533275 11:40:53 10/16/2023
20 42.753133 23.485199 66.238332 14.503966 38.781185 9.976352 11:41:53 10/16/2023
21 42.40278 23.539154 65.941934 14.581878 38.856170 9.372794 11:42:53 10/16/2023
22 42.512713 23.864629 66.377342 14.449995 37.837238 9.048781 11:43:54 10/16/2023
23 42.788667 24.004725 66.793392 14.556064 38.247640 9.515453 11:44:54 10/16/2023
24 42.778344 24.016964 66.795308 14.525852 38.337279 9.164051 11:45:54 10/16/2023
25 42.097598 23.724932 65.82253 14.347968 37.852445 8.960235 11:46:54 10/16/2023
26 42.571538 23.766503 66.338041 14.466988 38.366303 10.033762 11:47:54 10/16/2023
27 42.527762 23.620105 66.147867 14.518392 38.926570 10.176337 11:48:54 10/16/2023
28 42.268383 23.636818 65.905201 14.448286 38.541223 9.094996 11:49:54 10/16/2023
29 42.177581 23.422482 65.600063 14.429059 38.243996 9.595218 11:50:55 10/16/2023
30 42.088046 23.201654 65.2897 14.477006 38.151612 9.134867 11:51:55 10/16/2023
31 42.192498 23.095133 65.287631 14.435996 38.384998 9.878512 11:52:55 10/16/2023
32 41.382068 22.945943 64.328011 14.252522 38.284586 11.429207 11:53:55 10/16/2023
33 43.051914 22.893717 65.945631 14.421348 37.875174 16.127423 11:54:55 10/16/2023
34 44.123972 23.702692 67.826664 14.513815 37.878113 11.708839 11:55:55 10/16/2023
35 39.956722 21.570409 61.527131 14.248373 38.767268 10.732019 11:56:55 10/16/2023
36 41.916439 23.053223 64.969662 14.283777 38.465918 10.57136 11:57:56 10/16/2023
37 42.355886 23.035919 65.391805 14.461241 38.624340 10.664608 11:58:56 10/16/2023
38 42.657465 23.197604 65.855069 14.513746 38.528576 10.405246 11:59:56 10/16/2023
39 42.395645 23.07362 65.469265 14.417362 38.358780 10.091323 12:00:56 10/16/2023
40 41.90427 23.092242 64.996512 14.351638 38.092699 9.519781 12:01:56 10/16/2023
41 42.556149 22.676545 65.232694 14.596615 38.571280 14.098151 12:02:56 10/16/2023
42 42.119998 23.165508 65.285506 14.467223 38.195640 12.782603 12:03:57 10/16/2023
43 41.780322 23.378278 65.1586 14.391564 38.403588 9.777967 12:04:57 10/16/2023
44 41.549586 23.276387 64.825973 14.427969 38.472305 11.254446 12:05:57 10/16/2023
45 41.72506 23.572666 65.297726 14.405512 38.760298 9.710116 12:06:57 10/16/2023
46 42.345601 23.696163 66.041764 14.640834 39.342209 12.039338 12:07:57 10/16/2023
47 42.034335 23.772197 65.806532 14.520275 38.819885 9.456246 12:08:57 10/16/2023
48 42.338001 23.926819 66.26482 14.483588 38.864844 9.491698 12:09:57 10/16/2023
49 41.870823 23.361823 65.232646 14.288033 38.289745 9.687263 12:10:58 10/16/2023
50 42.584635 23.394281 65.978916 14.404094 38.405213 9.389472 12:11:58 10/16/2023
51 42.397821 23.413532 65.811353 14.560727 39.134524 9.935853 12:12:58 10/16/2023
52 43.571389 23.933015 67.504404 14.504857 37.881332 9.908164 12:13:58 10/16/2023
53 40.195998 21.823851 62.019849 14.262236 39.548656 9.768991 12:14:58 10/16/2023
54 40.975778 22.493473 63.469251 14.276579 38.763884 9.646717 12:15:58 10/16/2023
55 41.890894 23.017674 64.908568 14.429461 38.420396 9.922544 12:16:59 10/16/2023
56 41.507698 22.808817 64.316515 14.276579 38.420992 9.966877 12:17:59 10/16/2023
57 41.075208 22.575643 63.650851 14.236756 38.067455 10.510334 12:18:59 10/16/2023
58 40.554834 22.514153 63.068987 14.186797 38.209963 9.664676 12:19:59 10/16/2023
59 40.935298 22.640146 63.575444 14.340947 38.962533 10.226352 12:20:59 10/16/2023
60 40.91459 22.562709 63.477299 14.427767 39.148375 15.530402 12:21:59 10/16/2023
AVG 42.20 0.00 65.36 14.46 38.35 9.97
ppm@15% O2 34.74 7.69 20.38
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.43 0.77 0.06 0.10 0.24 0.43
#1
FTIR Measurements
Calculated Emission Levels
Uinta Wax Operating, LLC
Randlett 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 0.34 962 0.11 0.583
Average O2 9.8 (% dry)A 2 1.68 0.38 962 0.11 0.616
Average CO2 6.5 (% dry)A 3 3.10 0.35 962 0.11 0.592
Average N2 + CO 83.7 (% dry)A 4 5.17 0.35 962 0.11 0.592
Dry Molecular Weight 29.43 lb/lbmol A 5 10.83 0.32 962 0.11 0.566
Wet Molecular Weight 28.29 lb/lbmol A 6 12.90 0.30 962 0.11 0.548
EPA REFERENCE METHOD 320 A 7 14.32 0.28 962 0.11 0.529
Barometric Pressure 25.3 in Hg A 8 15.49 0.24 962 0.11 0.490
Moisture Content 9.97 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 65.36 ppm A 11
Calculated NOx Mass Output 0.77 lbs/hr A 12
Calculated NOx Output 0.43 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 14.46 ppm A 15
Calculated CO Mass Output 0.10 lbs/hr A 16
Calculated CO Output 0.06 g/bhp-hr B 1 0.51 0.29 962 0.11 0.539
EPA REFERENCE METHOD 320 B 2 1.68 0.31 962 0.11 0.557
Average Analyzer NMNEHC Level 38.35 ppm B 3 3.10 0.33 962 0.11 0.574
Calculated NMNEHC Mass Output 0.43 lbs/hr B 4 5.17 0.28 962 0.11 0.529
Calculated NMNEHC Output 0.24 g/bhp-hr B 5 10.83 0.36 962 0.11 0.600
LOAD APPROXIMATION B 6 12.90 0.38 962 0.11 0.616
Estimated Engine Load 800.4 BHP B 7 14.32 0.29 962 0.11 0.539
B 8 15.49 0.28 962 0.11 0.529
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.3 962 0.1 0.562
Average Stack Gas Velocity 46.81 ft/sec
Average Dry Flowrate 1639.09 dscfm
TEST RUN # 1
NO Dry
(ppm)
NO2 Dry
(ppm)
NOx Dry
(ppm)
CO Dry
(ppm)
NMNEHC C3 Dry
(ppm)
H2O% (High)
191C
Time
1 41.1933 23.233564 64.426864 14.367448 38.837691 11.57001 12:22:59 10/16/2023
2 41.210812 23.361427 64.572239 14.333838 38.401537 10.636353 12:24:00 10/16/2023
3 41.694613 23.518443 65.213056 14.394498 38.334152 10.465506 12:25:00 10/16/2023
4 42.054537 23.341647 65.396184 14.291006 38.591764 10.736147 12:26:00 10/16/2023
5 41.75441 23.254317 65.008727 14.423449 38.875006 11.27674 12:27:00 10/16/2023
6 41.878002 23.232489 65.110491 14.345135 38.920812 11.046025 12:28:00 10/16/2023
7 41.821416 23.304678 65.126094 14.415172 38.466205 10.917749 12:29:00 10/16/2023
8 42.025851 23.201735 65.227586 14.519026 38.301079 10.654217 12:30:00 10/16/2023
9 42.297168 23.45615 65.753318 14.51694 38.308775 10.455119 12:31:01 10/16/2023
10 42.129868 23.662598 65.792466 14.392812 38.620935 10.374117 12:32:01 10/16/2023
11 41.758075 23.643207 65.401282 14.423925 38.644757 10.512272 12:33:01 10/16/2023
12 42.546724 24.01573 66.562454 14.530181 38.816601 11.547529 12:34:01 10/16/2023
13 41.568242 23.437134 65.005376 14.350811 38.341686 11.155098 12:35:01 10/16/2023
14 42.403125 23.998615 66.40174 14.513274 38.604941 10.401912 12:36:01 10/16/2023
15 42.285738 23.89478 66.180518 14.416277 38.940802 10.034794 12:37:02 10/16/2023
16 41.970656 24.027409 65.998065 14.351559 38.660359 9.496584 12:38:02 10/16/2023
17 42.46428 24.19869 66.66297 14.505178 38.870294 10.343338 12:39:02 10/16/2023
18 42.347901 23.969696 66.317597 14.446415 38.444886 10.25187 12:40:02 10/16/2023
19 42.732928 23.856149 66.589077 14.434274 38.760160 9.989292 12:41:02 10/16/2023
20 42.435058 23.597887 66.032945 14.462107 38.546242 9.672561 12:42:02 10/16/2023
21 41.887444 23.344904 65.232348 14.467019 39.331623 15.575056 12:43:02 10/16/2023
22 42.354111 23.613806 65.967917 14.412069 38.225044 14.284126 12:44:03 10/16/2023
23 42.132562 23.714164 65.846726 14.45225 38.464707 10.60423 12:45:03 10/16/2023
24 41.972669 23.734711 65.70738 14.437771 39.013295 9.523621 12:46:03 10/16/2023
25 42.085338 23.81411 65.899448 14.338632 38.200569 10.169615 12:47:03 10/16/2023
26 42.138688 23.856057 65.994745 14.401807 37.990982 10.338656 12:48:03 10/16/2023
27 41.719924 23.531561 65.251485 14.277011 38.240156 10.636075 12:49:03 10/16/2023
28 42.393204 23.481853 65.875057 14.421926 38.158222 9.877254 12:50:03 10/16/2023
29 42.418298 23.313597 65.731895 14.432581 38.580582 10.142481 12:51:04 10/16/2023
30 42.827512 23.522207 66.349719 14.575506 38.751120 9.676587 12:52:04 10/16/2023
31 42.521682 23.449203 65.970885 14.574815 38.747720 10.024572 12:53:04 10/16/2023
32 42.709868 23.570831 66.280699 14.558471 38.514226 10.032847 12:54:04 10/16/2023
33 42.670523 23.393788 66.064311 14.431132 37.915293 12.247095 12:55:04 10/16/2023
34 42.399984 23.550812 65.950796 14.500944 38.046645 10.608652 12:56:04 10/16/2023
35 42.36589 23.65284 66.01873 14.476824 38.485640 9.810161 12:57:04 10/16/2023
36 41.685381 23.060292 64.745673 14.420166 38.817417 10.203513 12:58:05 10/16/2023
37 42.377265 23.141118 65.518383 14.533015 38.643066 10.037725 12:59:05 10/16/2023
38 42.86731 22.992599 65.859909 14.47925 38.339061 10.791421 13:00:05 10/16/2023
39 43.399428 23.332695 66.732123 14.549141 38.654368 10.164884 13:01:05 10/16/2023
40 42.974797 22.963938 65.938735 14.494087 38.373476 10.84553 13:02:05 10/16/2023
41 42.496928 23.268406 65.765334 14.401156 38.282876 9.255231 13:03:05 10/16/2023
42 42.283068 22.823614 65.106682 14.424749 38.563649 8.691111 13:04:06 10/16/2023
43 43.83718 23.587544 67.424724 14.722935 39.124397 8.983089 13:05:06 10/16/2023
44 42.466151 23.01878 65.484931 14.503247 38.883613 9.522486 13:06:06 10/16/2023
45 42.082886 21.80722 63.890106 14.413186 39.114462 16.864781 13:07:06 10/16/2023
46 42.216072 22.118056 64.334128 14.265606 38.051723 12.327547 13:08:06 10/16/2023
47 44.973225 23.243696 68.216921 14.578376 37.802814 9.945825 13:09:06 10/16/2023
48 40.451027 21.173104 61.624131 14.259371 39.218958 9.469444 13:10:06 10/16/2023
49 41.842091 22.461943 64.304034 14.351186 38.737318 10.454814 13:11:07 10/16/2023
50 42.883679 22.617822 65.501501 14.392257 37.981976 10.357513 13:12:07 10/16/2023
51 40.01543 21.661142 61.676572 14.220425 39.033042 10.092569 13:13:07 10/16/2023
52 42.093782 22.753893 64.847675 14.395342 38.369365 10.541272 13:14:07 10/16/2023
53 41.91407 22.674109 64.588179 14.379265 38.581098 9.514047 13:15:07 10/16/2023
54 42.253899 22.820951 65.07485 14.387685 38.735387 10.107711 13:16:07 10/16/2023
55 42.396357 22.706167 65.102524 14.417474 38.613225 10.663646 13:17:07 10/16/2023
56 42.517547 22.1487 64.666247 14.431943 38.734639 14.979521 13:18:08 10/16/2023
57 42.199471 22.442282 64.641753 14.413092 38.576281 10.369856 13:19:08 10/16/2023
58 42.462519 22.857127 65.319646 14.368928 38.755191 9.385068 13:20:08 10/16/2023
59 41.796096 22.519533 64.315629 14.386697 38.701637 12.068462 13:21:08 10/16/2023
60 41.933786 22.746172 64.679958 14.501145 38.690570 12.141391 13:22:08 10/16/2023
AVG 42.23 0.00 65.44 14.43 38.57 10.71
ppm@15% O2 34.78 7.67 20.50
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.44 0.78 0.06 0.10 0.25 0.44
Calculated Emission Levels
Record Date
Uinta Wax Operating, LLC
Randlett Compressor Station
Run 2
#1
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 0.27 965 0.13 0.520
Average O2 9.8 (% dry)A 2 1.68 0.30 965 0.13 0.548
Average CO2 6.6 (% dry)A 3 3.10 0.34 965 0.13 0.583
Average N2 + CO 83.6 (% dry)A 4 5.17 0.36 965 0.13 0.600
Dry Molecular Weight 29.45 lb/lbmol A 5 10.83 0.33 965 0.13 0.574
Wet Molecular Weight 28.22 lb/lbmol A 6 12.90 0.37 965 0.13 0.608
EPA REFERENCE METHOD 320 A 7 14.32 0.31 965 0.13 0.557
Barometric Pressure 25.29 in Hg A 8 15.49 0.25 965 0.13 0.500
Moisture Content 10.71 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 65.44 ppm A 11
Calculated NOx Mass Output 0.78 lbs/hr A 12
Calculated NOx Output 0.44 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 14.43 ppm A 15
Calculated CO Mass Output 0.10 lbs/hr A 16
Calculated CO Output 0.06 g/bhp-hr B 1 0.51 0.33 965 0.13 0.574
EPA REFERENCE METHOD 320 B 2 1.68 0.36 965 0.13 0.600
Average Analyzer NMNEHC Level 38.57 ppm B 3 3.10 0.39 965 0.13 0.624
Calculated NMNEHC Mass Output 0.44 lbs/hr B 4 5.17 0.34 965 0.13 0.583
Calculated NMNEHC Output 0.25 g/bhp-hr B 5 10.83 0.31 965 0.13 0.557
LOAD APPROXIMATION B 6 12.90 0.36 965 0.13 0.600
Estimated Engine Load 800.4 BHP B 7 14.32 0.38 965 0.13 0.616
B 8 15.49 0.32 965 0.13 0.566
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.3 965 0.1 0.576
Average Stack Gas Velocity 48.06 ft/sec
Average Dry Flowrate 1663.23 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 42.38428 22.980973 65.365253 14.398651 38.623561 10.000592 13:23:08 10/16/2023
2 42.394577 23.039143 65.43372 14.466313 38.400038 11.192809 13:24:08 10/16/2023
3 42.122949 22.691824 64.814773 14.46006 38.619247 10.210932 13:25:09 10/16/2023
4 42.528441 22.887531 65.415972 14.52218 38.557384 10.455526 13:26:09 10/16/2023
5 42.422649 22.676915 65.099564 14.444713 38.518524 10.707218 13:27:09 10/16/2023
6 42.49833 23.044183 65.542513 14.441154 38.283940 11.102754 13:28:09 10/16/2023
7 42.900542 23.135603 66.036145 14.474982 38.600558 11.028522 13:29:09 10/16/2023
8 42.244926 22.979553 65.224479 14.410292 38.631435 9.966329 13:30:09 10/16/2023
9 42.395499 23.101822 65.497321 14.28917 38.165567 9.600364 13:31:09 10/16/2023
10 41.601169 22.858299 64.459468 14.148245 38.069848 9.159725 13:32:10 10/16/2023
11 41.588403 22.62911 64.217513 14.195701 37.865501 9.013469 13:33:10 10/16/2023
12 42.199802 23.11804 65.317842 14.24972 37.965247 9.545229 13:34:10 10/16/2023
13 41.7658 22.844205 64.610005 14.336934 38.594423 10.7134 13:35:10 10/16/2023
14 42.339205 23.069293 65.408498 14.450023 38.592308 10.610539 13:36:10 10/16/2023
15 42.207483 23.019706 65.227189 14.280544 38.096778 9.847036 13:37:10 10/16/2023
16 41.978328 22.589442 64.56777 14.201515 37.753537 10.403865 13:38:11 10/16/2023
17 41.992015 22.872368 64.864383 14.284499 37.738749 9.171268 13:39:11 10/16/2023
18 41.929131 22.777568 64.706699 14.306844 38.229543 11.677719 13:40:11 10/16/2023
19 41.831566 23.09643 64.927996 14.345752 38.369110 13.038353 13:41:11 10/16/2023
20 42.456341 23.813318 66.269659 14.372965 38.695379 10.039411 13:42:11 10/16/2023
21 42.297177 23.293322 65.590499 14.337047 38.871889 10.854346 13:43:11 10/16/2023
22 41.577224 22.748449 64.325673 14.236418 38.602614 15.02842 13:44:11 10/16/2023
23 42.648468 23.250346 65.898814 14.379002 38.225067 12.663684 13:45:12 10/16/2023
24 43.077369 23.630505 66.707874 14.374131 38.098972 10.844593 13:46:12 10/16/2023
25 42.800772 23.822784 66.623556 14.35715 38.321461 10.463447 13:47:12 10/16/2023
26 42.632285 23.92077 66.553055 14.380478 38.239289 9.945718 13:48:12 10/16/2023
27 41.895359 23.330633 65.225992 14.38941 38.622057 17.447158 13:49:12 10/16/2023
28 42.271625 23.509373 65.780998 14.378644 38.641242 15.0567 13:50:12 10/16/2023
29 42.137737 23.531067 65.668804 14.316605 37.857365 13.452799 13:51:12 10/16/2023
30 42.419924 23.767457 66.187381 14.373158 38.253973 9.887696 13:52:13 10/16/2023
31 42.374931 23.696617 66.071548 14.431931 38.271128 11.216367 13:53:13 10/16/2023
32 41.928978 23.81679 65.745768 14.368897 38.437929 9.581036 13:54:13 10/16/2023
33 42.528994 24.213749 66.742743 14.395376 38.164745 10.000581 13:55:13 10/16/2023
34 41.564264 23.764429 65.328693 14.277019 38.270630 9.795341 13:56:13 10/16/2023
35 42.195995 23.99935 66.195345 14.378545 38.182225 9.572903 13:57:13 10/16/2023
36 42.548518 23.863703 66.412221 14.425084 38.433827 9.818084 13:58:13 10/16/2023
37 42.314396 23.815427 66.129823 14.453749 38.653069 9.677122 13:59:14 10/16/2023
38 41.644017 23.6662 65.310217 14.287378 38.435637 10.324772 14:00:14 10/16/2023
39 41.152468 23.195521 64.347989 14.163769 37.883035 9.669784 14:01:14 10/16/2023
40 41.765971 23.319393 65.085364 14.217617 37.997753 9.729523 14:02:14 10/16/2023
41 41.624491 23.151924 64.776415 14.226945 38.390500 10.455522 14:03:14 10/16/2023
42 41.599332 23.099251 64.698583 14.298659 38.042740 9.26032 14:04:14 10/16/2023
43 41.113379 22.772929 63.886308 14.22776 38.290721 9.549946 14:05:14 10/16/2023
44 40.491981 22.658128 63.150109 14.125536 38.168202 9.64403 14:06:15 10/16/2023
45 40.552727 22.852795 63.405522 14.106565 38.694096 9.26273 14:07:15 10/16/2023
46 40.23702 22.741149 62.978169 14.141488 38.429239 9.788856 14:08:15 10/16/2023
47 39.709305 22.230985 61.94029 14.04356 38.283974 14.290307 14:09:15 10/16/2023
48 40.387037 22.586237 62.973274 14.04353 38.186986 12.653351 14:10:15 10/16/2023
49 40.143727 22.686404 62.830131 14.057258 37.824483 10.429378 14:11:15 10/16/2023
50 40.318545 22.80988 63.128425 14.120293 38.490484 10.464153 14:12:15 10/16/2023
51 40.240756 22.980926 63.221682 14.117809 38.393288 10.515593 14:13:16 10/16/2023
52 40.955175 23.226541 64.181716 14.246464 37.889258 13.341891 14:14:16 10/16/2023
53 40.928772 23.091816 64.020588 14.316835 38.734356 16.011257 14:15:16 10/16/2023
54 40.968324 23.055392 64.023716 14.204696 37.667017 15.804571 14:16:16 10/16/2023
55 41.120509 23.346927 64.467436 14.239883 38.063781 10.296963 14:17:16 10/16/2023
56 40.929774 23.20264 64.132414 14.191763 37.734091 10.335242 14:18:16 10/16/2023
57 41.423024 23.669963 65.092987 14.318583 37.985887 10.366789 14:19:16 10/16/2023
58 41.197481 23.621461 64.818942 14.227062 38.027471 10.483235 14:20:17 10/16/2023
59 41.483297 23.726442 65.209739 14.347315 38.399910 10.051635 14:21:17 10/16/2023
60 41.474487 23.797657 65.272144 14.350261 38.134429 9.887088 14:22:17 10/16/2023
AVG 41.74 0.00 64.95 14.30 38.28 10.92
ppm@15% O2 34.52 7.60 20.35
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.45 0.78 0.06 0.10 0.25 0.44
FTIR Measurements
#1
Calculated Emission Levels
Uinta Wax Operating, LLC
Randlett 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 0.25 967 0.11 0.500
Average O2 9.8 (% dry)A 2 1.68 0.34 967 0.11 0.583
Average CO2 6.6 (% dry)A 3 3.10 0.30 967 0.11 0.548
Average N2 + CO 83.6 (% dry)A 4 5.17 0.33 967 0.11 0.574
Dry Molecular Weight 29.45 lb/lbmol A 5 10.83 0.37 967 0.11 0.608
Wet Molecular Weight 28.20 lb/lbmol A 6 12.90 0.40 967 0.11 0.632
EPA REFERENCE METHOD 320 A 7 14.32 0.37 967 0.11 0.608
Barometric Pressure 25.28 in Hg A 8 15.49 0.34 967 0.11 0.583
Moisture Content 10.92 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 64.95 ppm A 11
Calculated NOx Mass Output 0.78 lbs/hr A 12
Calculated NOx Output 0.45 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 14.30 ppm A 15
Calculated CO Mass Output 0.10 lbs/hr A 16
Calculated CO Output 0.06 g/bhp-hr B 1 0.51 0.28 967 0.11 0.529
EPA REFERENCE METHOD 320 B 2 1.68 0.31 967 0.11 0.557
Average Analyzer NMNEHC Level 38.28 ppm B 3 3.10 0.35 967 0.11 0.592
Calculated NMNEHC Mass Output 0.44 lbs/hr B 4 5.17 0.38 967 0.11 0.616
Calculated NMNEHC Output 0.25 g/bhp-hr B 5 10.83 0.36 967 0.11 0.600
LOAD APPROXIMATION B 6 12.90 0.41 967 0.11 0.640
Estimated Engine Load 786.6 BHP B 7 14.32 0.37 967 0.11 0.608
B 8 15.49 0.30 967 0.11 0.548
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.3 967 0.1 0.583
Average Stack Gas Velocity 48.75 ft/sec
Average Dry Flowrate 1678.96 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 11:00:52 0.006633 -0.020326 -0.007951 -0.0052 0.563569 0.440761 -0.666746 0.154679 0.154667 0.00602 -0.013693 -0.013692 5.728127 190.991058 1.020784
10/16/2023 11:01:00 -0.100948 -0.028791 -0.003646 -0.032747 1.143663 0.066857 -0.930703 0.159388 0.159382 0.011611 -0.129739 -0.129734 5.147304 191.016251 1.020207
10/16/2023 11:01:07 0.10468 0.013438 -0.005792 -0.015394 1.15474 0.946187 -0.935516 0.161944 0.161934 0.023481 0.118118 0.118111 6.443657 190.95903 1.02054
10/16/2023 11:01:15 -0.029094 0.04093 -0.003823 0.000784 1.432259 0.644315 -0.650414 -0.102211 -0.102207 0.005854 0.011836 0.011836 5.589855 190.920883 1.020345
10/16/2023 11:01:56 0 0 0 0 0 0 0 0 0 0 0 0 0 190.990631 1.020342
10/16/2023 11:02:09 -0.239899 -0.042559 0.000426 0.065665 -0.614958 0.387272 -0.14488 -0.141048 -0.141049 -0.003513 -0.282458 -0.282459 0.008793 190.997177 1.020095
10/16/2023 11:02:16 -0.018038 0.017511 0.001177 0.030253 0.065257 -0.099279 -0.127632 -0.161864 -0.161866 0.004455 -0.000527 -0.000527 0.009519 190.997177 1.019926
10/16/2023 11:02:24 -0.236378 -0.024679 -0.001152 0.057347 -0.215847 0.009555 0.284817 -0.104609 -0.104608 0.005044 -0.261057 -0.261054 -0.003701 190.938141 1.019657
10/16/2023 11:02:31 -0.160506 0.032168 0.000132 0.03662 -0.052579 -0.064192 -0.56891 0.128307 0.128307 0.005724 -0.128338 -0.128338 -0.011264 190.90181 1.019714
10/16/2023 11:02:39 -0.173134 -0.081157 0.000305 -0.094524 -0.905964 -0.182889 -0.25876 -0.111652 -0.111652 0.00054 -0.254291 -0.254292 -0.000835 190.903625 1.019774
10/16/2023 11:02:46 0.030296 0.023968 0.007424 0.069376 -0.351729 0.597621 0.358624 -0.151522 -0.151533 -0.001675 0.054264 0.054268 0.06366 190.980484 1.019878
10/16/2023 11:02:54 -0.190544 -0.078593 0.003196 -0.042166 -0.297299 -0.255712 -0.863268 -0.079972 -0.079974 -0.00308 -0.269136 -0.269145 0.002201 190.984467 1.019703
10/16/2023 11:03:01 -0.18141 -0.007821 0.002291 0.048344 0.032166 -0.171549 -0.165291 -0.037257 -0.037258 0.001369 -0.189232 -0.189236 0.006403 190.984467 1.019677
10/16/2023 11:03:09 -0.066807 -0.007307 0.004736 0.061407 -0.218648 0.137399 0.619797 -0.15765 -0.157657 0.000355 -0.074115 -0.074118 -0.005298 190.98764 1.019491
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 11:04:53 486.54607 490.486031 482.004098 191.048035 1.014416 10/16/2023 11:08:48 93.184515 190.988174 1.013735
10/16/2023 11:05:01 511.316019 515.395995 507.621747 191.048035 1.015839 10/16/2023 11:08:56 97.256941 191.033508 1.01265
10/16/2023 11:05:08 511.682853 515.829091 508.943062 191.048035 1.016086 10/16/2023 11:09:03 98.398872 191.06076 1.01285
10/16/2023 11:05:16 512.438055 516.367003 510.390104 191.048035 1.016373 10/16/2023 11:09:11 97.929219 191.06076 1.012653
10/16/2023 11:05:23 511.220024 516.497831 510.444822 191.000351 1.016326 10/16/2023 11:09:18 97.46648 191.06076 1.012183
10/16/2023 11:05:31 512.544798 516.386963 509.794236 190.952667 1.016373 10/16/2023 11:09:26 98.057458 191.06076 1.012021
10/16/2023 11:05:38 510.651675 516.264944 510.964573 190.952667 1.01639 10/16/2023 11:09:33 97.91719 191.06076 1.012025
10/16/2023 11:05:46 511.224947 515.955851 510.082867 190.952667 1.012805 10/16/2023 11:09:41 97.760988 191.06076 1.011763
10/16/2023 11:05:53 510.700123 514.608205 511.434943 190.952667 1.008597 10/16/2023 11:09:48 98.165011 191.06076 1.011869
10/16/2023 11:06:01 509.876498 514.900594 509.357642 190.952667 1.008826 10/16/2023 11:09:56 97.990132 191.026245 1.012042
Date Time NO2 191C span Temp ( C )Pressure (atm)
10/16/2023 11:06:37 132.208595 190.933594 1.005907
10/16/2023 11:06:44 147.983211 190.972656 1.005711
10/16/2023 11:06:52 149.273819 191.016251 1.005728
10/16/2023 11:06:59 149.728727 191.016251 1.005812
10/16/2023 11:07:07 150.411472 191.016251 1.006024
10/16/2023 11:07:14 150.604983 191.008987 1.00617
10/16/2023 11:07:22 150.701736 190.954483 1.006764
10/16/2023 11:07:29 150.856269 190.986282 1.008439
10/16/2023 11:07:37 150.629313 190.997177 1.01074
10/16/2023 11:07:44 151.287072 190.997177 1.011018
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 11:10:32 54.75402 34.423604 42.53898 190.971741 1.00623 10/16/2023 11:12:05 93.723519 190.963791 1.012952
10/16/2023 11:10:39 385.054575 370.159259 364.825856 190.971741 1.010301 10/16/2023 11:12:13 96.827798 191.00354 1.013255
10/16/2023 11:10:47 445.550543 446.775381 443.634184 190.969025 1.01505 10/16/2023 11:12:20 97.24235 191.00354 1.012873
10/16/2023 11:10:54 502.946268 507.425122 502.122216 190.900223 1.009292 10/16/2023 11:12:28 97.843873 190.990814 1.01275
10/16/2023 11:11:02 509.541433 514.283151 508.804694 190.952667 1.00868 10/16/2023 11:12:35 97.865278 190.954483 1.012598
10/16/2023 11:11:09 511.001731 514.843675 509.372529 190.952667 1.008445 10/16/2023 11:12:43 97.980933 190.984467 1.012635
10/16/2023 11:11:17 509.765334 514.958545 506.671918 190.952667 1.008671 10/16/2023 11:12:50 97.790333 190.984467 1.012581
10/16/2023 11:11:24 510.251113 515.834445 508.77636 191.007172 1.008597 10/16/2023 11:12:58 97.960498 190.99559 1.012466
10/16/2023 11:11:32 507.749073 512.410351 509.087658 190.962997 1.008739 10/16/2023 11:13:05 97.319461 191.061661 1.012578
10/16/2023 11:11:39 506.860115 512.518945 509.149447 190.939957 1.00917 10/16/2023 11:13:13 98.243613 191.067108 1.012538
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)
10/16/2023 11:13:35 0.204788 0.112332 0.286063 -0.338938 190.971741 1.00821
10/16/2023 11:13:43 0.197114 0.350001 -0.239511 -0.131703 190.994446 1.008433
10/16/2023 11:13:50 0.215208 -0.04652 0.171269 0.268065 191.048035 1.008439
10/16/2023 11:13:58 0.04054 -0.018535 0.672869 -0.33141 191.028961 1.008187
10/16/2023 11:14:05 0.028481 -0.010369 -0.406431 -0.494871 190.975372 1.008416
10/16/2023 11:14:13 0.059052 -0.235583 0.251511 0.121415 191.035324 1.008201
10/16/2023 11:14:20 0.069562 0.084701 -0.50024 0.280359 191.035324 1.008087
10/16/2023 11:14:28 -0.03276 -0.115789 -0.085716 0.035751 191.035324 1.008531
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 11:18:04 6.410516 29.453822 190.965912 1.007916
10/16/2023 11:18:11 6.410497 29.260926 190.94722 1.007386
10/16/2023 11:18:19 6.406011 29.937763 191.016251 1.007522
10/16/2023 11:18:26 6.350833 29.695419 191.022614 1.007215
10/16/2023 11:19:11 6.291055 29.74374 191.006393 1.007108
10/16/2023 11:19:19 6.298339 29.04904 190.990814 1.00756
10/16/2023 11:19:26 6.286948 29.316013 190.941772 1.007584
10/16/2023 11:19:34 4.888664 114.086238 190.990814 1.006948
10/16/2023 11:19:41 4.188284 156.036313 190.990814 1.006664
10/16/2023 11:19:49 5.474097 75.941653 190.990814 1.007805
10/16/2023 11:19:56 5.584658 68.545032 190.994003 1.007414
10/16/2023 11:20:04 5.66085 68.571851 191.001724 1.007137
10/16/2023 11:20:11 5.667602 67.800497 190.971741 1.006887
10/16/2023 11:20:19 5.657798 68.025109 190.974121 1.007166
10/16/2023 11:20:26 5.667404 67.673919 191.035324 1.007091
10/16/2023 11:20:34 5.665759 66.856944 191.054398 1.006767
10/16/2023 11:20:42 5.720586 62.093884 190.988098 1.006887
10/16/2023 11:21:12 5.823763 57.060527 190.976517 1.006982
10/16/2023 11:21:19 5.87613 57.014224 190.976517 1.006982
10/16/2023 11:21:27 5.857697 56.590018 191.017044 1.007078
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 14:28:55 475.137075 478.943653 474.438742 190.984467 0.998356 10/16/2023 14:27:27 95.968989 190.971741 0.973833
10/16/2023 14:29:03 502.122072 507.588306 502.499833 190.984467 0.998773 10/16/2023 14:27:35 96.713408 190.971741 1.003514
10/16/2023 14:29:10 503.68969 509.514037 501.954306 190.984467 0.998796 10/16/2023 14:27:42 96.545206 190.962997 1.003464
10/16/2023 14:29:18 503.809061 509.416898 502.947781 190.984467 0.998974 10/16/2023 14:27:49 97.152355 190.985367 1.003592
10/16/2023 14:29:25 502.994495 509.074075 504.179234 190.984467 0.998733 10/16/2023 14:27:57 96.88578 190.998993 1.003764
10/16/2023 14:29:33 502.69893 508.568785 503.099698 190.984467 0.998782 10/16/2023 14:28:05 96.874012 190.98082 1.00383
10/16/2023 14:29:40 502.478 508.782378 504.825587 190.984467 0.998916 10/16/2023 14:28:12 96.628301 190.984467 1.003807
10/16/2023 14:29:48 502.875446 509.465455 504.592248 190.984467 0.998658 10/16/2023 14:28:20 96.808523 190.984467 1.003976
10/16/2023 14:29:55 505.340589 510.366661 507.142721 190.984467 0.99842 10/16/2023 14:28:27 96.785628 190.984467 1.004194
10/16/2023 14:30:03 503.319125 509.118738 504.363344 190.984467 0.998615 10/16/2023 14:28:35 96.815461 190.984467 1.004112
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 14:27:42 0.090286 -0.040207 0.423642 190.962997 1.003464 10/16/2023 14:30:45 0.104619 190.984467 1.004472
10/16/2023 14:27:49 -0.137303 -0.108016 -0.457491 190.985367 1.003592 10/16/2023 14:30:52 -0.104184 190.984467 1.004294
10/16/2023 14:27:57 -0.138357 -0.159491 -0.02038 190.998993 1.003764 10/16/2023 14:31:00 -0.691383 190.984467 1.004242
10/16/2023 14:28:05 -0.161589 -0.020022 0.276405 190.98082 1.00383 10/16/2023 14:31:07 -0.643087 190.984467 1.004131
10/16/2023 14:28:12 -0.08723 0.065847 -0.171012 190.984467 1.003807 10/16/2023 14:31:15 -0.0736 190.984467 1.00399
10/16/2023 14:28:20 -0.038005 0.007102 -0.523297 190.984467 1.003976 10/16/2023 14:31:22 -0.939172 190.984467 1.003876
10/16/2023 14:28:27 -0.092303 -0.204318 -0.48435 190.984467 1.004194 10/16/2023 14:31:30 -0.10848 190.984467 1.003537
10/16/2023 14:28:35 -0.117347 -0.093006 -0.247022 190.984467 1.004112 10/16/2023 14:31:37 -0.116093 190.984467 1.003285
SAMPLE SPIKE RECOVERY
POST SYSTEM CAL
POST SYSTEM ZERO
PRE TEST 1 508.7 6.4 29.7 5.7 62.1 0.099 70.0%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 514.9 509.3 -0.2 1.10 -0.03
CO 509.9 506.0 -0.1 0.77 -0.02
Propane 509.4 508.7 0.0 0.13 0.01
Ethylene 98.2 99.84 -0.3 -1.68 -0.29
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 512.5 509.3 0.0 0.63 0.01
CO 506.9 506.0 0.1 0.17 0.02
Propane 509.1 508.7 0.0 0.09 0.01
Ethylene*98.2 99.84 -0.1 -1.60 -0.09
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 509.1 509.3 -0.1 -0.04 -0.01 0.67 0.02
CO 503.3 506.0 -0.1 -0.53 -0.02 0.70 0.04
Propane 504.4 508.7 -0.1 -0.85 -0.03 0.94 0.03
Ethylene*97.2 99.84 -0.3 -2.69 -0.28 1.09 0.19
*CTS Scans are conducted with Ethylene through the sample line.
Lf
5.11
Lr Cr Tr Pr Lr/Lf
5.14 98.2 191.1 1.0 1.01
Ls Cs Ts Ps Ls/Lf
5.13 98.2 191.1 1.0 1.00
Pathlength
Stack Propane
Concentration
Stack + Spike CO2
Concentration
Stack + Propane
Concentration
DF
Calculated
POST SYSTEM CAL
PRE SYSTEM CAL
% Recovery
Propane
PRE DIRECT CAL
FTIR QA/QC SUMMARY
SAMPLE RECOVERY CALCULATIONS
Period Spike #Concentration of
Propane Cylinder
Stack CO2
Concentration
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 – Randlett CS
10-16-2023

Finley – Randlett CS
10-16-2023

Finley – 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\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000145.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\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000068.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000069.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000070.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000071.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000072.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000073.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000074.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 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 37.69 1.8 -0.18 0.25 2.45 2.45 -0.91 --0-2795 1.04 Good
NO2 191C 20.68 0.29 -0.02 0.02 0.31 0.31 -0.41 --0-488 1 Good
N2O 191C 0.15 0.21 0.19 0.02 0.02 0.24 0.24 0.23 0.23 0.04 0.06 0-200 -Close to DL
NH3 TE 191C -2.43 26.21 3.26 2.05 3.49 44.73 44.73 3.49 24.27 0.23 1.09 0-2995 -Close to DL
H2O% (HIGH) 191C9.93 0.21 -0.01 0.01 0.34 0.34 -0.2 --0-40 -Good
FORMALDEHYDE 191C2.44 0.77 1.94 0.13 0.15 0.87 0.87 2.18 2.18 0.24 0.65 0-69 -Close to DL
FORMIC ACID 191C TE1.51 9.98 1.22 0.7 0.82 11.69 11.69 1.38 9.26 0.17 0.41 0-466 -Close to DL
CH4 2900 CM-1 191C706.14 17.18 -0.84 1.22 33.12 33.12 -14.12 --0-3143 0.97 Good
PROPANE 191C27.86 1.2 -0.11 0.13 1.43 1.43 -0.61 --0-4976 0.96 Good
PROPYLENE 191C TE-5.23 9.83 2.07 0.78 0.93 11.63 11.63 2.3 8.9 0.24 0.69 0-194 -Close to DL
ETHANE 191C 55.91 2.73 -0.26 0.4 4.25 4.25 -1.38 --0-1004 -Good
ETHYLENE 191C TE4.1 16.28 4.58 1.01 1.24 20.09 20.09 5.08 15.17 0.49 1.53 0-900 -Close to DL
CO PPM 191C (1OF2)13.17 0.69 -0.15 0.33 1.28 1.28 -0.3 --0-5010 1.03 Good
CO2% 191C 6.01 0.14 -0.01 0.01 0.19 0.19 -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 191C-1.83 2.07 2.15 0.36 0.47 2.66 2.66 2.51 2.51 0.36 0.72 0-186 0.99 Close to DL
ACETYLENE 191C-0.06 2.23 0.57 0.36 0.48 2.94 2.94 0.71 1.88 0.14 0.19 0-1016 -Close to DL
SO2 191C 1.27 2.78 1.54 0.24 0.29 3.39 3.39 1.58 2.54 0.04 0.51 0-964 1.02 Close to DL
HEXANE 191C 2.34 0.82 2.17 0.06 0.09 1.1 1.1 2.41 2.41 0.24 0.72 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000205.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\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000068.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000069.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000070.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000071.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000072.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000073.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000074.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 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 35.48 1.75 -0.18 0.25 2.38 2.38 -0.88 --0-2795 1.04 Good
NO2 191C 19.11 0.29 -0.02 0.02 0.3 0.3 -0.38 --0-488 1 Good
N2O 191C 0.14 0.21 0.19 0.02 0.02 0.24 0.24 0.23 0.23 0.04 0.06 0-200 -Close to DL
NH3 TE 191C -2.04 26.03 3.26 2.05 3.49 44.42 44.42 3.49 24.1 0.23 1.09 0-2995 -Close to DL
H2O% (HIGH) 191C10.08 0.2 -0.01 0.01 0.33 0.33 -0.2 --0-40 -Good
FORMALDEHYDE 191C2.39 0.75 1.94 0.13 0.15 0.85 0.85 2.18 2.18 0.24 0.65 0-69 -Close to DL
FORMIC ACID 191C TE0.86 9.82 1.22 0.7 0.82 11.49 11.49 1.38 9.11 0.17 0.41 0-466 -Close to DL
CH4 2900 CM-1 191C702.28 16.69 -0.84 1.22 32.17 32.17 -14.05 --0-3143 0.97 Good
PROPANE 191C27.84 1.17 -0.11 0.13 1.41 1.41 -0.6 --0-4976 0.96 Good
PROPYLENE 191C TE-5.06 9.73 2.07 0.78 0.93 11.51 11.51 2.3 8.81 0.24 0.69 0-194 -Close to DL
ETHANE 191C 55.06 2.66 -0.26 0.4 4.15 4.15 -1.34 --0-1004 -Good
ETHYLENE 191C TE3.89 16.12 4.58 1.01 1.24 19.89 19.89 5.08 15.01 0.49 1.53 0-900 -Close to DL
CO PPM 191C (1OF2)12.84 0.67 -0.15 0.33 1.24 1.24 -0.29 --0-5010 1.03 Good
CO2% 191C 5.92 0.13 -0.01 0.01 0.18 0.18 -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 191C-1.27 2.03 2.15 0.36 0.47 2.61 2.61 2.51 2.51 0.36 0.72 0-186 0.99 Close to DL
ACETYLENE 191C-0.16 2.18 0.57 0.36 0.48 2.88 2.88 0.71 1.83 0.14 0.19 0-1016 -Close to DL
SO2 191C 1.18 2.91 1.54 0.24 0.29 3.55 3.55 1.58 2.67 0.04 0.51 0-964 1.02 Close to DL
HEXANE 191C 2.34 0.8 2.17 0.06 0.09 1.08 1.08 2.41 2.41 0.24 0.72 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000265.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\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000068.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000069.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000070.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000071.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000072.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000073.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 10-16-23_000074.LAB
C:\OLT\Data\Finley\Randlett CS U1 10-16-23\RANDLETT CS U1 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 35.44 1.58 -0.18 0.25 2.15 2.15 -0.79 --0-2795 1.04 Good
NO2 191C 20.16 0.3 -0.02 0.02 0.32 0.32 -0.4 --0-488 1 Good
N2O 191C 0.14 0.22 0.19 0.02 0.02 0.25 0.25 0.23 0.23 0.04 0.06 0-200 -Close to DL
NH3 TE 191C -4.27 27.55 3.26 2.05 3.49 47.01 47.01 3.49 25.55 0.23 1.09 0-2995 -Close to DL
H2O% (HIGH) 191C10.52 0.21 -0.01 0.01 0.34 0.34 -0.21 --0-40 -Good
FORMALDEHYDE 191C2.6 0.69 1.94 0.13 0.15 0.78 0.78 2.18 2.18 0.24 0.65 0-69 -Close to DL
FORMIC ACID 191C TE0.84 9.86 1.22 0.7 0.82 11.54 11.54 1.38 9.16 0.17 0.41 0-466 -Close to DL
CH4 2900 CM-1 191C702.49 16.57 -0.84 1.22 31.93 31.93 -14.05 --0-3143 0.97 Good
PROPANE 191C27.65 1.18 -0.11 0.13 1.42 1.42 -0.61 --0-4976 0.96 Good
PROPYLENE 191C TE-3.16 9.58 2.07 0.78 0.93 11.33 11.33 2.3 8.72 0.24 0.69 0-194 -Close to DL
ETHANE 191C 54.37 2.62 -0.26 0.4 4.08 4.08 -1.32 --0-1004 -Good
ETHYLENE 191C TE3.75 16.3 4.58 1.01 1.24 20.12 20.12 5.08 15.2 0.49 1.53 0-900 -Close to DL
CO PPM 191C (1OF2)12.67 0.62 -0.15 0.33 1.15 1.15 -0.27 --0-5010 1.03 Good
CO2% 191C 5.9 0.14 -0.01 0.01 0.19 0.19 -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 191C-1.25 1.92 2.15 0.36 0.47 2.47 2.47 2.51 2.51 0.36 0.72 0-186 0.99 Close to DL
ACETYLENE 191C-0.26 2.25 0.57 0.36 0.48 2.97 2.97 0.71 1.9 0.14 0.19 0-1016 -Close to DL
SO2 191C 1.85 2.88 1.54 0.24 0.29 3.51 3.51 1.58 2.63 0.04 0.51 0-964 1.02 Close to DL
HEXANE 191C 2.16 0.79 2.17 0.06 0.09 1.07 1.07 2.41 2.41 0.24 0.72 0-1000 -Close to DL

APPENDIX C

Test Run Load %Site Rated Load, bhp Load Approx., bhp
1 58 1380 800.4
2 58 1380 800.4
3 57 1380 786.6
Engine Load Approximation based on Panel Levels

APPENDIX D

Example Calculations: Uinta Wax Operating, LLC, Randlett Compressor Station, #1

The following is a step-by-step calculation for the first test run conducted on the Randlett
Compressor Station #1.

Test Parameters

• Stack Diameter = 16 inches
• Traverse Points = 16
• Ports = 2
• Barometric Pressure = 25.3 in Hg
• Average O2 = 9.8%
• Average CO2 = 6.5%
• Load Approximation = 800.4 bhp
• Moisture Content = 9.97%

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 = 6.5%
%O2 – Oxygen Content Of The Gas = 9.8%
%N2 – Nitrogen Content Of The Gas
%CO – Carbon Monoxide Content Of The Gas

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

= (100 – 9.8 – 6.5)

= 83.7% Dry

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

= (0.44 * 6.5) + (0.32 * 9.8) + (0.28 * 83.7)

= 29.43 lb/lbmol

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

Where:
MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 29.43 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 9.97%

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

= 29.43 * (1 – (9.97/ 100)) + (18 * (9.97/ 100))

= 28.29 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) = 0.562 in H2O
TS – Average stack temperature (R) = 962 R
PB – Barometric pressure (in Hg) = 25.3 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.1 in H2O
MA – Molecular weight of the wet gas (lb/lbmol) = 28.29 lb/lbmol

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

= 0.84 * (85.49) * 0.562 * ( 962 / (((0.1/ 13.6) + 25.3) * 28.29))

= 46.81 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 inches
BWS – Moisture content of the gas (%) = 9.97%
TSTD – Standard temperature (528R)
TS – Average stack temperature (R) = 962 R
PB – Barometric pressure (in Hg) = 25.3 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.1 in H2O
VS– Average Stack gas velocity (ft/sec) = 46.81 ft/sec

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

= 60 * (1 - (9.97/ 100)) * 46.81 *  * (((16 / 2) / 12))2) * 528 / 962 * (25.3 + (0.1 / 13.6))
/ 29.92

= 1639.09 dscfm

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

Where:
Q – Volumetric Flowrate = 1639.09 dscfm
2.83168*10 -2 – Conversion factor for cubic feet to cubic meter
60 – Minutes in an hour

= Q * 60 * 2.83168*10 -2

= 1639.09 *60 * 2.83168*10 -2

= 2784.83 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 = 65.36 ppm
1.92*10 -3 - Conversion constant for ppm to g/m3 NOx
Q – Volumetric Flowrate = 2784.83 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 800.4 Bhp

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

= (65.36 * 1.912*10 -3 * 2784.83 * 1) / 800.4

= 0.43 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.43 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 800.4 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.43 / 454 * 800.4

= 0.77 lbs/hr

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

Where:
Cd – Measured CO concentration in ppm = 14.46 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 CO
Q – Volumetric Flowrate = 2784.83 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 800.4 Bhp

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

= (14.46 * 1.164*10 -3 * 2784.83 * 1) / 800.4

= 0.06 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.06 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 800.4 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.06 / 454 * 800.4

= 0.10 lbs/hr

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

Where:
Cd – Measured VOC concentration in ppm = 38.35 ppm
1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – Volumetric Flowrate = 2784.83 m3/hr
T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 800.4 Bhp

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

= (38.35 * 1.833*10 -3 * 2784.83 * 1) / 800.4

= 0.24 g/Bhp-hr

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

Where:
g/Bhp-hr = 0.24 g/Bhp-hr
454 – Conversion factor for g to lbs
Bhp - Unit Brake Horsepower = 800.4 Bhp

= g/Bhp-hr / 454 * Bhp

= 0.24 / 454 * 800.4

= 0.43 lbs/hr

APPENDIX E

FTIR Engine Test Sheet

Company Name "::'-n / e y
Location / Unit 1.0. t: aYlI/I,C] -I-f-­(,.S (.J J
Type of Test Completed 3YJJ,.,r 11///1/
Jordan Nix
J(7h n G-(m.( v
IrilJ6/l-3
/I r~J, rrJ(/Y
Field Technician (5)
Client Rep and/or State Rep
Date
Stack Diagram Non-Resettable Run Time Hours l..-6"i?-z,
Engine Make I'Ff r
Engine Model rr3f]/~ T ..._--­
11/( W 06> I Z-.Enqine SIN c·····:····,·..·,,,····:·..··..· £-;~t!Port Distance A T
A""5{'Port Distance B \,; "":
1
t
B
~
I ~;;"Exhaust Diameter (inches) ::11
Cylinder # ConcentrationCalibration Gas 'rCC89245 509.3NO (ppm)
CC89245 506CO (ppm)
CC89245 508.7Propane (ppm
CC725232 148.6N02 (ppm) 1
EB0122984 99.84Ethvlene (ppm !f
CC89245 504.7Methane (ppm
SG9142412BAL 30.33Acetaldehvde 'ppm)
Test 1 Test 2 Test 3
Time of Reading
Atm Pressure (in Hg)
Atm Temp CF)
Engine RPM
" z.z:es .s»
6'2...
11_Jl
IZt. z-
2--5,z..q­
61) arz­
J"?Z2­
2:-?;?'Il)'
h9­
12-16
*Manifold Pres. Vae(") or Boostfpsi} or Boost (psia) t::-::,' Z­L 3,/ 2-3,z...­
Manifold Temp CF) /'F) 1/7­//<j
Psuction (psi) StaQe 1 , I( --­/11 I¥
Tsuction CF) Stage 1 -~.---.­,
Pdischarae (nsi) Staae 1
Psuction (psi) Stage 2
;r~ -. "7-'5
-'''''''"
.-rZ. -.
Tsuction CF) staae 2 --,~"-"' ,....-­--,,~
Pdlscharqe (osi) Staae 2 c::...2..'1 z. z:3 z.-zz........
Psuction (psi) Staqe 3 ."-~,.
...-..~._. o;-.....~'._ ..~,
Tsuction CF) Stage 3 -.... -­~..,,"
Pdischarae (psi) Staqe 3 -sz e: ~Z-.q ~ z, '-/
Psuction (psi) Stage 4
Tsuction ('F) Staqe 4
Pdischarge (psi) Staqe 4
Gas Throuqhput (mmet/d) or ( nnCi .<Se) -?tlel/~ Iblilf 7,,1 '1,,6 Z I:?­' Lf 2-.J~ 1'1
Pre Cat Temp CF) fLT lt7-r; 4-::r~ q1J/
Post Cat Temp ('F) (LT t:;O'l.-­J::7:; ~ ~~~
Cat Differential Pres. (" of H2O) ct· Z­ct, Z­4-Z--
Humiditv% 33 ~O "'Z..r":;­
02% Q--,4, q. ~ q.~
C02 % Dry
LOAD % (~r (Estimated) ~!rr
&.~
1S't!6
/',6
r;;-s:J
b/~
IJ~·
IQnition Timing CF)
AFR Setting mV (Left Bank) f)t?S tvo't..
'Lo·t(
60 p~m
...t> ..
AFR SettinQ mV (Riqht Bank) h~f... ?_q.{. ~
Rev 8
• Some units show boost in inches of Hg. In this situation please indicate if it is
positive (+) or negative(-). Eg: (+12") or (- 5")
9/17/2019
COMPANY NAME:Finley COMPANY LOCATION:Randlett CS U1 DATE:10/16/2023
STACK DIAMETER (inches):16 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:9.8 AVERAGE O2:9.8 AVERAGE O2:9.8
AVERAGE CO2:6.5 AVERAGE CO2:6.6 AVERAGE CO2:6.6
BARO PRESSURE:25.3 BARO PRESSURE:25.29 BARO PRESSURE:25.28
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 0.512 0.34 502 0.11 1 0.512 0.27 505 0.13 1 0.512 0.25 507 0.11
2 1.68 0.38 2 1.68 0.3 2 1.68 0.34
3 3.104 0.35 3 3.104 0.34 3 3.104 0.3
4 5.168 0.35 4 5.168 0.36 4 5.168 0.33
5 10.832 0.32 5 10.832 0.33 5 10.832 0.37
6 12.896 0.3 6 12.896 0.37 6 12.896 0.4
7 14.32 0.28 7 14.32 0.31 7 14.32 0.37
8 15.488 0.24 8 15.488 0.25 8 15.488 0.34
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 0.29 502 0.11 1 0.512 0.33 505 0.13 1 0.512 0.28 507 0.11
2 1.68 0.31 2 1.68 0.36 2 1.68 0.31
3 3.104 0.33 3 3.104 0.39 3 3.104 0.35
4 5.168 0.28 4 5.168 0.34 4 5.168 0.38
5 10.832 0.36 5 10.832 0.31 5 10.832 0.36
6 12.896 0.38 6 12.896 0.36 6 12.896 0.41
7 14.32 0.29 7 14.32 0.38 7 14.32 0.37
8 15.488 0.28 8 15.488 0.32 8 15.488 0.3
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:Randlett CS U1
Date:10/16/2023
PD:16
DD:36 YES Method 1 Criteria Met
UD:24 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 2.66 9.80
A 2 8.00 9.80
A 3 13.33 9.80
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 9.80
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)