DAQ-2025-000145

1

DAQC-022-25
Site ID 16169 (B4)

MEMORANDUM

TO: STACK TEST FILE – UINTA WAX OPERATING, LLC – Zager Booster Station –
Duchesne County

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

FROM: Kyle Greenberg, Environmental Scientist

DATE: January 9, 2024

SUBJECT: Sources: Caterpillar G3606LE; SN: 4ZS00902; Unit ID: E160518
Contact: Karen Pratt: 720-990-9927
Location: Remote location in Duchesne County, UT
Test Contractor: Oasis Emissions Consultants, Inc.
Permit/AO#: DAQE-AN161690003-24 dated July 26, 2024
Action Code: TR
Subject: Review of Stack Test Reports dated September 18, 2024
On September 26, 2024, Utah Division of Air Quality (DAQ) received a test report for the above listed
unit. Testing was performed on September 11, 2024, to demonstrate compliance with the emission limits
found in Condition II.B.4 of Approval Order DAQE-AN161690003-24 and 40 CFR Part 60 Subpart JJJJ.
The DAQ calculated test results are:

Source Test Date Test
Method
Pollutant Tester
Results
DAQ Results Limits
Caterpillar
G3606LE SN:
4ZS00902 Unit
ID: E160518
September
11, 2024
320 NOx 0.30 g/bhp-hr
1.12 lb/hr
0.304 g/bhp-hr
1.121 lb/hr
1.0 g/bhp-hr
2.09 lb/hr
320 CO 0.04 g/bhp-hr
0.13 lb/hr
0.036 g/bhp-hr
0.131 lb/hr
2.0 g/bhp-hr
2.09 lb/hr
320 VOC 0.57 g/bhp-hr
2.09 lb/hr
0.629 g/bhp-hr
2.088 lb/hr
0.7 g/bhp-hr
2.51 lb/hr

DEVIATIONS: None.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The emissions from the Caterpillar G3606LE compressor engine 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.

HPV: N/A

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

Emissions
Uinta Wax Operating, LLC
Zager Booster Station; Site ID: 16169
Duchesne County
Caterpillar G3606LE; SN: 4ZS00902; Unit ID: E160518
Test Date:9/11/2024
Run # 1 2 3 Average
Start Time 9:35 10:36 11:37
Stop Time 10:35 11:36 12:37
Sample Duration (minutes) 60 60 60
BHP Engine Load - Actual (bhp) 1686.3 1668.5 1668.5 1674.4
DS Stack Diameter (inches) 20.0 20.0 20.0 20.0
PAVG Average (Delta P)½ (" H2O)½0.828 0.859 0.850 0.846
CP Pitot Tube Constant (unitless) 0.84 0.84 0.84 0.84
TS Stack Temperature (°F) 795 797 795 796
Pbar Barometric Pressure (" Hg) 24.63 24.63 24.63 24.63
Ps Stack Pressure ('' H2O)0.33 0.36 0.35 0.35
O2%vd O2 (%vd)11.6 11.5 11.5 11.5
CO2%vd CO2 (%vd)5.6 5.6 5.6 5.6
N2%vd N2 (%vd)82.8 82.9 82.9 82.9
dry NOX (ppmvd)45.8 47.6 47.8 47.1
dry CO (ppmvd) 9.1 9.1 9.0 9.1
wet TVOC (ppmvw as C3H8)103.117 0.000 101.390 91.6
Run # 1 2 3 Average
Bws Measured Moisture Content (%/100) 0.102 0.100 0.101 0.101
Bws Saturated Moisture Content (%/100) 409.035 413.117 409.010 410.387
Bws Actual Moisture Content (%/100) 0.102 0.100 0.101 0.101
MD Molecular Weight Dry (lb/lb-mole) 29.36 29.36 29.36 29.36
MA Molecular Weight Wet (lb/lb-mole) 28.21 28.22 28.21 28.21
VS Gas Velocity (ft/sec) 79.9 82.9 82.0 81.6
FACFM Gas Flow (acfm) 10457 10854 10734 10682
FDSCFM Gas Flow (dscfm) 3254 3378 3343 3325
FWSCFM Gas Flow (wscfm) 3624 3756 3720 3700
FKWSCFH Gas Flow (kwscfh) 217 225 223 222
FKWSCFM Gas Flow (kwscfm) 4 4 4 4
lb/hr Gas Flow (lb/hr) 15919 16507 16344 16257
Fo Fo (unitless)1.661 1.679 1.679 1.673
wet O2 (%vw)10.4 10.4 10.3 10.4
wet CO2 (%vw)5.0 5.0 5.0 5.0
wet NOX (ppmvw)41.183 42.876 42.963 42.341
15 NOX (ppmvd @ 15% O2)29.081 29.902 29.996 29.660
lb/hr NOX (lb/hr)1.068 1.152 1.144 1.121 2.09
g/bhp-hr NOX (g/bhp-hr)0.287 0.313 0.311 0.304 2.0
wet CO (ppmvw) 8.211 8.190 8.055 8.152
15 CO (ppmvd @ 15% O2)5.798 5.712 5.624 5.711
lb/hr CO (lb/hr) 0.130 0.134 0.131 0.131 2.09
g/bhp-hr CO (g/bhp-hr) 0.035 0.036 0.035 0.036 4.0
dry NMEOC (ppmvd as C3H8)92.640 90.920 91.150 91.570
15 NMEOC (ppmvd as C3H8 @ 15% O2)58.772 57.067 57.211 57.679
lb/hr NMEOC (lb/hr as C3H8)2.068 2.107 2.090 2.088 2.51
g/bhp-hr NMEOC (g/bhp-hr as C3H8)0.556 0.573 0.568 0.566 1.0
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 1

Source Test Report
For
Uinta Wax Operating, LLC
Zager Booster Station
Duchesne County, Utah

Test Date: September 11, 2024
Report Date: September 18, 2024

UDEQ Permit: #DAQE-AN161690001-23 & ER #N161690003
Engine: Caterpillar G3606LE
SN: 4ZS00902
Unit ID: E160518

Prepared By:

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

September 18, 2024

Ms. Karen Pratt
Uinta Wax Operating, LLC

Dear Ms. Pratt:

Re: Engine Emission Testing For Uinta Wax Operating, LLC, Zager Booster Station,
Unit E160518, Permit #DAQE-AN161690001-23 & ER #N161690003.

An air emissions test program was conducted on a Caterpillar G3606LE engine, operated by
Uinta Wax Operating, LLC and designated as Unit E160518, located at the Zager Booster
Station in Duchesne County, Utah. The purpose of the testing was to demonstrate annual
compliance with the emissions limits contained in UDEQ Permit #DAQE-AN161690001-23
& ER #N161690003 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 September 11, 2024.

UDEQ Permit #DAQE-AN161690001-23 & ER #N161690003 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
lbs/hr 1.12 2.09 0.13 2.09 2.09 2.51
*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 0.30 2.0 0.04 4.0 0.57 1.0
*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)
726 0.8

Engine Load (Averaged Over 3 Test Runs)

Rated BHP Operating
BHP
% Load
1775 1674.4 94.3

Testing Protocol

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

Quality Assurance

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

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

Yours truly,
Oasis Emission Consultants, Inc.

_________________________ _______________________
Charles A. Chapman Crystal Leonard
Manager of Technical Services Senior EHS Specialist

_________________________

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

SOURCE EMISSION TEST REPORT

UDEQ Permit #DAQE-AN161690001-23 & ER #N161690003

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: Zager Booster Station
Duchesne County, Utah

Emission Source: Caterpillar G3606LE
Unit E160518

Date of Test: September 11, 2024

Date of Report: September 18, 2024

TABLE OF CONTENTS

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

List of Tables and Figures

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

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

APPENDIX A: NOx, CO and VOC Test Data

APPENDIX B: Quality Assurance/Calibration Data

APPENDIX C: Load Approximation

APPENDIX D: Example Calculations and Summary

APPENDIX E: Field Notes

1

1.1 Introduction

An air emissions test program was conducted on a Caterpillar G3606LE engine, operated by
Uinta Wax Operating, LLC and designated as Unit E160518, located at the Zager Booster
Station in Duchesne County, Utah. The purpose of the testing was to demonstrate annual
compliance with the emissions limits contained in UDEQ Permit #DAQE-AN161690001-23
& ER #N161690003 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 5.5 miles south of Myton, in Duchesne County, Utah.
Latitude: 40.115 Longitude: -110.0641

Three one hour test runs were performed on September 11, 2024 to analyze NOx, CO and
VOC emission levels. Test runs were performed according to methodologies outlined by EPA
40 CFR 60(A) Methods 1-3 & EPA 40 CFR 63(A), Method 320 as outlined in the submitted
Source Test Protocol dated May 17, 2024. Each one hour test run consisted of 60 readings
taken at one minute intervals.

Process parameters were recorded during each test run in order to determine the load.
Parameters include the engine panel load percent reading.

The following key personnel were present during testing:

David Martinez, OEC
John, Arch

2

2.1 Stack Sampling Location

The facility is located 5.5 miles south of Myton, in Duchesne County, Utah.
Latitude: 40.115 Longitude: -110.0641

Testing was conducted on the Caterpillar G3606LE engine. The sampling port for moisture,
NOx, CO and VOC measurements was approximately 7.2 pipe diameters (144”) downstream
from the nearest flow disturbance (Distance B) and 2.0 pipe diameters (40”) upstream from
the nearest disturbance (Distance A), as seen in Figure 1. The stack sampling location was
placed at approximately 50% insertion depth based on an O2 stratification check which
demonstrated a non-stratified flow regime. The stratification was conducted according to
EPA 40 CFR 75(A), §6.5.6.1 using 3 traverse points determined according to Table 1 below.

Figure 1 - Sample Port Location

20"
A
B

Oxidation
Catalyst
3

Table 1 - Insertion Depths of Traverse Points for Stratification Test

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

Table 2 - Location of Traverse Points in Circular Stacks

4

3.1 Discussion of NOx, CO and VOC Test Results

Three, one hour test runs were performed on September 11, 2024 to analyze exhaust NOx,
CO and VOC (NMNEHC C3) emission levels to demonstrate annual compliance with the
emissions limits contained in the WDEQ Permit #DAQE-AN161690001-23 & ER
#N161690003 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 G3606LE, NOx, CO and VOC

The first test was performed from 9:35 to 10:34 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1686.3 bhp, and the average NOx and CO levels were found to be 0.29 g/bhp-hr,
1.07 lbs/hr and 0.03 g/bhp-hr, 0.13 lbs/hr respectively, below limitations. The VOC
level tested at, 0.56 g/bhp-hr, 2.07 lbs/hr, which tested in compliance.

3.1.2 Source Test 2: Caterpillar G3606LE, NOx, CO and VOC

The second test was performed from 10:36 to 11:35 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1668.5 bhp, and the average NOx and CO levels were found to be 0.31 g/bhp-hr,
1.15 lbs/hr and 0.04 g/bhp-hr, 0.13 lbs/hr respectively, below limitations. The VOC
level tested at 0.57 g/bhp-hr, 2.11 lbs/hr, which tested in compliance.

3.1.3 Source Test 3: Caterpillar G3606LE, NOx, CO and VOC

The third test was performed from 11:37 to 12:36 for NOx, CO and VOC.

Based on operating parameters recorded during testing, the load was approximated at
1668.5 bhp, and the average NOx and CO levels were found to be 0.31 g/bhp-hr,
1.14 lbs/hr and 0.04 g/bhp-hr, 0.13 lbs/hr respectively, below limitations. The VOC
level tested at 0.57 g/bhp-hr 2.09 lbs/hr, which tested in compliance.

Test
Run
NOx
(ppmvd)
NOx
(g/bhp-
hr)
NOx
(lbs/hr)
CO
(ppmvd)
CO
(g/bhp-
hr)
CO
(lbs/hr)
VOC
(ppmvd)
VOC
(g/bhp-
hr)
VOC
(lbs/hr)
O2
(%)
1 45.84 0.29 1.07 9.14 0.03 0.13 92.64 0.56 2.07 11.6
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-
hr)
NOx
(lbs/hr)
CO
(ppmvd)
CO
(g/bhp-
hr)
CO
(lbs/hr)
VOC
(ppmvd)
VOC
(g/bhp-
hr)
VOC
(lbs/hr)
O2
(%)
2 47.64 0.31 1.15 9.10 0.04 0.13 90.92 0.57 2.11 11.5
Test
Run
NOx
(ppmvd)
NOx
(g/bhp-
hr)
NOx
(lbs/hr)
CO
ppmvd)
CO
(g/bhp-
hr)
CO
(lbs/hr)
VOC
(ppmvd)
VOC
(g/bhp-
hr)
VOC
(lbs/hr
O2
(%)
3 47.79 0.31 1.14 8.96 0.04 0.13 91.15 0.57 2.09 11.5
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). 31 August 2023. Web. 18 September 2024.
<https://www.epa.gov/emc/emc-promulgated-test-methods>.
ASTM International. “Standards & Publications.” All Environment Standards.
Web. 18 September 2024. <https://www.astm.org/Standards/D6348.htm>.

6

4.2 Equipment Utilization

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

• (1) MKS MultiGas 2030 FTIR Continuous Gas Analyzer (0.210 L/min sample flow, 0.014
atmosphere sample pressure, 1 atmosphere cell pressure, 191°C cell temperature)
• (1) Laptop Computer for the FTIR Analyzer using MKS MG2000 Software
• (1) 75ft or 100ft Heated Teflon Line w/ Heated Sample Probe and Spike Bypass Line
• S-Type Pitot Tube c/w 20 ft. Heated Sample Line (coefficient 0.84)
• (1) 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 99.4%, 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 17.730134 27.233854 44.963988 9.493763 93.783556 8.674241 9:35:22 09/11/2024
2 17.862924 27.376747 45.239671 9.314619 93.896413 8.383078 9:36:22 09/11/2024
3 18.501296 27.513336 46.014632 9.239253 93.036926 9.915867 9:37:22 09/11/2024
4 17.646257 26.918214 44.564471 9.307113 92.528367 12.092609 9:38:22 09/11/2024
5 18.615289 27.066577 45.681866 9.063254 92.979409 8.82499 9:39:22 09/11/2024
6 17.185282 27.492778 44.67806 9.215609 93.438572 8.383655 9:40:23 09/11/2024
7 19.33678 27.874283 47.211063 8.884418 92.924527 8.388179 9:41:23 09/11/2024
8 17.582024 27.405207 44.987231 9.305005 93.308854 12.747318 9:42:23 09/11/2024
9 18.94883 27.198904 46.147734 8.957462 92.804058 10.33235 9:43:23 09/11/2024
10 18.532712 27.8681 46.400812 9.073357 93.377305 9.73882 9:44:23 09/11/2024
11 17.349172 27.60279 44.951962 9.255693 93.612822 9.489854 9:45:23 09/11/2024
12 18.326185 27.583127 45.909312 9.060864 93.072186 8.831647 9:46:24 09/11/2024
13 18.460142 27.938211 46.398353 9.084125 92.624649 8.815924 9:47:24 09/11/2024
14 17.681848 27.450145 45.131993 9.156242 92.368415 10.745967 9:48:24 09/11/2024
15 18.291409 27.877849 46.169258 9.17596 92.168452 11.854341 9:49:24 09/11/2024
16 17.850297 27.80385 45.654147 9.080823 92.346172 10.284024 9:50:24 09/11/2024
17 17.454884 27.76847 45.223354 9.075141 92.991527 9.622947 9:51:24 09/11/2024
18 17.211633 27.75354 44.965173 9.122212 92.909399 9.941708 9:52:25 09/11/2024
19 17.402125 27.676466 45.078591 9.201799 92.626899 11.937696 9:53:25 09/11/2024
20 18.012901 27.510213 45.523114 9.175292 91.838406 10.89939 9:54:25 09/11/2024
21 18.04973 27.341383 45.391113 9.121964 91.968899 10.398864 9:55:25 09/11/2024
22 18.198136 27.947088 46.145224 9.173012 92.454854 10.429696 9:56:25 09/11/2024
23 19.596796 27.635941 47.232737 8.909688 91.810704 10.488752 9:57:25 09/11/2024
24 18.865196 27.607773 46.472969 9.021025 92.430671 10.400597 9:58:25 09/11/2024
25 16.459617 27.327972 43.787589 9.306972 93.552340 10.60225 9:59:26 09/11/2024
26 16.025664 27.20441 43.230074 9.313189 94.633933 10.211627 10:00:26 09/11/2024
27 18.718777 27.968469 46.687246 8.858601 92.842757 9.561139 10:01:26 09/11/2024
28 16.697316 27.780432 44.477748 9.197191 93.419234 10.20495 10:02:26 09/11/2024
29 16.342632 27.687095 44.029727 9.27581 93.319739 10.283373 10:03:26 09/11/2024
30 16.221769 27.485207 43.706976 9.308513 93.649033 12.046267 10:04:26 09/11/2024
31 17.716022 28.055148 45.77117 9.149342 93.335623 11.158903 10:05:27 09/11/2024
32 18.077038 27.921533 45.998571 8.934866 92.922164 9.551798 10:06:27 09/11/2024
33 16.957027 27.903686 44.860713 9.101196 93.632553 9.621535 10:07:27 09/11/2024
34 18.287161 27.953933 46.241094 8.985087 92.702849 10.028347 10:08:27 09/11/2024
35 17.58078 27.815668 45.396448 9.138523 93.075555 10.236574 10:09:27 09/11/2024
36 17.064199 28.435165 45.499364 9.093848 92.989374 10.129314 10:10:27 09/11/2024
37 17.010905 28.39124 45.402145 9.169052 93.297361 10.171458 10:11:27 09/11/2024
38 18.516743 28.486258 47.003001 8.882013 91.548135 11.086934 10:12:28 09/11/2024
39 17.560878 28.519532 46.08041 9.157013 92.891483 10.36941 10:13:28 09/11/2024
40 19.151635 28.285748 47.437383 8.831598 90.836345 11.584981 10:14:28 09/11/2024
41 18.16636 28.102818 46.269178 9.043468 92.506779 10.754211 10:15:28 09/11/2024
42 17.29313 28.171531 45.464661 9.237696 94.261952 9.82954 10:16:28 09/11/2024
43 16.993292 28.217125 45.210417 9.278687 92.465363 9.343065 10:17:28 09/11/2024
44 18.886753 28.444448 47.331201 9.070079 91.662957 10.502583 10:18:29 09/11/2024
45 17.990662 28.184347 46.175009 9.110561 91.401822 10.199651 10:19:29 09/11/2024
46 17.184534 28.305762 45.490296 9.265928 92.731946 9.623997 10:20:29 09/11/2024
47 18.604022 28.540933 47.144955 9.045043 91.931129 9.511151 10:21:29 09/11/2024
48 16.986697 28.073815 45.060512 9.293087 93.057102 9.116316 10:22:29 09/11/2024
49 17.647475 28.108697 45.756172 9.299208 92.812217 10.191715 10:23:29 09/11/2024
50 19.121212 28.055136 47.176348 9.053532 90.960507 9.406346 10:24:29 09/11/2024
51 18.82378 27.96729 46.79107 9.135618 91.677905 9.516383 10:25:30 09/11/2024
52 19.35844 27.824167 47.182607 9.050128 92.155733 10.212316 10:26:30 09/11/2024
53 18.514341 28.008681 46.523022 9.197559 92.192309 9.766698 10:27:30 09/11/2024
54 17.747274 27.91313 45.660404 9.297231 92.289320 9.607508 10:28:30 09/11/2024
55 19.568963 27.630705 47.199668 9.006441 91.347496 10.594799 10:29:30 09/11/2024
56 19.520281 27.716675 47.236956 9.221909 92.491334 10.320044 10:30:30 09/11/2024
57 18.751865 27.973037 46.724902 9.214824 91.797952 9.982423 10:31:31 09/11/2024
58 18.943255 27.673636 46.616891 9.163034 90.852520 11.384672 10:32:31 09/11/2024
59 18.416643 27.570743 45.987386 9.179497 90.545537 11.310225 10:33:31 09/11/2024
60 19.925122 27.820961 47.746083 9.109631 93.207206 9.804254 10:34:31 09/11/2024
AVG 18.03 0.00 45.84 9.14 92.64 10.16
ppm@15% O2 29.08 5.80 58.77
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.29 1.07 0.03 0.13 0.56 2.07
E160518
FTIR Measurements
Calculated Emission Levels
Uinta Wax Operating, LLC
Zager Booster Station
Run 1
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 20 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 0.64 0.62 1254 0.33 0.787
Average O2 11.6 (% dry)A 2 2.10 0.65 0.806
Average CO2 5.6 (% dry)A 3 3.88 0.69 0.831
Average N2 + CO 82.8 (% dry)A 4 6.46 0.73 0.854
Dry Molecular Weight 29.36 lb/lbmol A 5 13.54 0.71 0.843
Wet Molecular Weight 28.21 lb/lbmol A 6 16.12 0.68 0.825
EPA REFERENCE METHOD 320 A 7 17.90 0.66 0.812
Barometric Pressure 24.63 in Hg A 8 19.36 0.64 0.800
Moisture Content 10.16 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 45.84 ppm A 11
Calculated NOx Mass Output 1.07 lbs/hr A 12
Calculated NOx Output 0.29 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 9.14 ppm A 15
Calculated CO Mass Output 0.13 lbs/hr A 16
Calculated CO Output 0.03 g/bhp-hr B 1 0.64 0.63 1254 0.33 0.794
EPA REFERENCE METHOD 320 B 2 2.10 0.66 0.812
Average Analyzer NMNEHC Level 92.64 ppm B 3 3.88 0.70 0.837
Calculated NMNEHC Mass Output 2.07 lbs/hr B 4 6.46 0.74 0.860
Calculated NMNEHC Output 0.56 g/bhp-hr B 5 13.54 0.77 0.877
LOAD APPROXIMATION B 6 16.12 0.73 0.854
Estimated Engine Load 1686.3 BHP B 7 17.90 0.71 0.843
B 8 19.36 0.67 0.819
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.7 1254 0.3 0.828
Average Stack Gas Velocity 79.89 ft/sec
Average Dry Flowrate 3259.51 dscfm
TEST RUN # 1
NO Dry
(ppm)
NO2 Dry
(ppm)
NOx Dry
(ppm)
CO Dry
(ppm)
NMNEHC C3 Dry
(ppm)
H2O% (High)
191C
Time
1 20.153655 27.413951 47.567606 9.089101 90.905880 10.2147 10:36:31 09/11/2024
2 19.925032 27.107661 47.032693 9.162491 91.254984 10.378861 10:37:31 09/11/2024
3 19.224661 27.359236 46.583897 9.216085 91.022394 11.428231 10:38:32 09/11/2024
4 19.06111 27.641239 46.702349 9.213768 90.327447 10.543799 10:39:32 09/11/2024
5 17.773436 27.68501 45.458446 9.455305 92.176365 9.749885 10:40:32 09/11/2024
6 17.801743 27.372691 45.174434 9.50468 92.330144 9.838946 10:41:32 09/11/2024
7 19.979742 27.279488 47.25923 9.136294 91.028674 10.521988 10:42:32 09/11/2024
8 19.256937 27.451194 46.708131 9.243101 91.308239 9.756311 10:43:32 09/11/2024
9 18.523214 27.32359 45.846804 9.420058 92.820285 9.992326 10:44:33 09/11/2024
10 20.264327 27.76735 48.031677 9.151085 91.064073 9.804085 10:45:33 09/11/2024
11 20.072997 27.6132 47.686197 9.101734 90.518466 9.63264 10:46:33 09/11/2024
12 19.285021 27.853545 47.138566 9.249706 91.051369 8.8413 10:47:33 09/11/2024
13 20.341754 27.991725 48.333479 9.128161 89.880771 10.341585 10:48:33 09/11/2024
14 20.554035 28.157605 48.71164 9.043511 90.420147 9.244039 10:49:33 09/11/2024
15 20.737449 27.742457 48.479906 8.954179 89.180241 9.327239 10:50:34 09/11/2024
16 18.038744 27.672551 45.711295 9.361907 90.135413 9.264239 10:51:34 09/11/2024
17 20.030089 27.575773 47.605862 8.989991 90.020466 9.319854 10:52:34 09/11/2024
18 19.284821 28.106685 47.391506 9.12977 90.241403 10.422246 10:53:34 09/11/2024
19 20.338335 27.742399 48.080734 8.989899 89.858213 10.486115 10:54:34 09/11/2024
20 20.446635 27.474316 47.920951 8.975103 90.335783 10.083072 10:55:34 09/11/2024
21 21.147703 27.001731 48.149434 8.97012 89.730650 13.191282 10:56:34 09/11/2024
22 23.207867 26.758196 49.966063 8.612566 89.978188 10.444076 10:57:35 09/11/2024
23 21.035765 27.587498 48.623263 8.905616 90.302047 10.113813 10:58:35 09/11/2024
24 21.992208 27.262143 49.254351 8.729981 89.012320 9.002177 10:59:35 09/11/2024
25 21.516037 27.296158 48.812195 8.901997 89.593990 9.405123 11:00:35 09/11/2024
26 19.301389 27.680885 46.982274 9.365418 89.914574 10.674253 11:01:35 09/11/2024
27 20.113161 27.408942 47.522103 9.212601 89.863729 10.142645 11:02:35 09/11/2024
28 20.514357 27.618793 48.13315 9.04873 90.037880 9.858823 11:03:36 09/11/2024
29 21.147369 27.336399 48.483768 8.934139 89.737370 10.473032 11:04:36 09/11/2024
30 20.816322 27.633727 48.450049 9.047194 89.112276 10.589835 11:05:36 09/11/2024
31 22.280927 27.134807 49.415734 8.8119 88.494455 11.003235 11:06:36 09/11/2024
32 20.014295 27.675583 47.689878 9.082369 88.913999 11.573921 11:07:36 09/11/2024
33 20.316681 27.689036 48.005717 8.949915 88.798679 10.729863 11:08:36 09/11/2024
34 21.399321 27.498538 48.897859 8.785486 90.013272 10.035014 11:09:36 09/11/2024
35 21.543116 27.300912 48.844028 8.759624 90.597772 9.597093 11:10:37 09/11/2024
36 21.614829 27.239865 48.854694 8.794924 89.573787 9.730775 11:11:37 09/11/2024
37 19.993976 27.528308 47.522284 9.089239 90.451826 9.825211 11:12:37 09/11/2024
38 20.391536 27.574895 47.966431 9.009632 90.761961 9.833765 11:13:37 09/11/2024
39 23.033031 26.927991 49.961022 8.637155 90.589650 10.360005 11:14:37 09/11/2024
40 20.533361 27.859118 48.392479 9.035719 90.125465 11.125806 11:15:37 09/11/2024
41 19.170466 27.93496 47.105426 9.207701 91.208023 10.618833 11:16:38 09/11/2024
42 19.349011 27.788659 47.13767 9.186411 92.270777 9.904912 11:17:38 09/11/2024
43 18.244784 28.162905 46.407689 9.298774 92.934560 9.633671 11:18:38 09/11/2024
44 18.141403 28.522943 46.664346 9.389865 91.954893 9.122885 11:19:38 09/11/2024
45 18.746093 28.421804 47.167897 9.292321 91.977769 9.362185 11:20:38 09/11/2024
46 20.005731 28.452188 48.457919 8.99546 92.132877 9.346151 11:21:38 09/11/2024
47 17.885769 28.768231 46.654 9.334174 92.456599 9.139597 11:22:38 09/11/2024
48 19.077493 28.695887 47.77338 9.160493 92.223740 9.423749 11:23:39 09/11/2024
49 19.75525 28.50046 48.25571 8.992309 91.896426 10.506703 11:24:39 09/11/2024
50 18.376255 28.10415 46.480405 9.296722 91.894646 11.344752 11:25:39 09/11/2024
51 18.242791 28.339031 46.581822 9.387759 92.470843 10.26878 11:26:39 09/11/2024
52 18.762573 28.29107 47.053643 9.202869 92.314341 9.384134 11:27:39 09/11/2024
53 18.099007 28.992617 47.091624 9.217018 91.653189 8.501831 11:28:39 09/11/2024
54 17.297376 28.875956 46.173332 9.339249 92.178288 8.361717 11:29:39 09/11/2024
55 19.668653 29.030017 48.69867 8.898239 91.892848 9.060566 11:30:40 09/11/2024
56 18.872907 29.19192 48.064827 9.0659 92.071651 9.896895 11:31:40 09/11/2024
57 17.623375 28.72258 46.345955 9.267803 92.658347 9.859929 11:32:40 09/11/2024
58 18.662751 29.349648 48.012399 9.17705 94.078809 9.449735 11:33:40 09/11/2024
59 18.732417 28.971355 47.703772 9.100095 91.944047 10.124328 11:34:40 09/11/2024
60 17.835067 29.160248 46.995315 9.221549 91.752875 9.87139 11:35:40 09/11/2024
AVG 19.76 27.88 47.64 9.10 90.92 10.00
ppm@15% O2 29.90 5.71 57.07
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.31 1.15 0.04 0.13 0.57 2.11
Calculated Emission Levels
Record Date
Uinta Wax Operating, LLC
Zager Booster Station
Run 2
E160518
FTIR Measurements
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 20 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 0.64 0.69 1256 0.36 0.831
Average O2 11.5 (% dry)A 2 2.10 0.72 0.849
Average CO2 5.6 (% dry)A 3 3.88 0.75 0.866
Average N2 + CO 82.9 (% dry)A 4 6.46 0.79 0.889
Dry Molecular Weight 29.36 lb/lbmol A 5 13.54 0.78 0.883
Wet Molecular Weight 28.22 lb/lbmol A 6 16.12 0.74 0.860
EPA REFERENCE METHOD 320 A 7 17.90 0.72 0.849
Barometric Pressure 24.63 in Hg A 8 19.36 0.71 0.843
Moisture Content 10.00 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 47.64 ppm A 11
Calculated NOx Mass Output 1.15 lbs/hr A 12
Calculated NOx Output 0.31 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 9.10 ppm A 15
Calculated CO Mass Output 0.13 lbs/hr A 16
Calculated CO Output 0.04 g/bhp-hr B 1 0.64 0.68 1256 0.36 0.825
EPA REFERENCE METHOD 320 B 2 2.10 0.73 0.854
Average Analyzer NMNEHC Level 90.92 ppm B 3 3.88 0.77 0.877
Calculated NMNEHC Mass Output 2.11 lbs/hr B 4 6.46 0.80 0.894
Calculated NMNEHC Output 0.57 g/bhp-hr B 5 13.54 0.78 0.883
LOAD APPROXIMATION B 6 16.12 0.75 0.866
Estimated Engine Load 1668.5 BHP B 7 17.90 0.72 0.849
B 8 19.36 0.69 0.831
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.7 1256 0.4 0.859
Average Stack Gas Velocity 82.90 ft/sec
Average Dry Flowrate 3383.36 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 18.382397 29.011419 47.393816 9.136544 91.602731 9.722966 11:37:41 09/11/2024
2 17.721185 29.332394 47.053579 9.239084 91.349596 9.295211 11:38:41 09/11/2024
3 18.326333 29.306213 47.632546 9.206774 91.084566 9.860204 11:39:41 09/11/2024
4 18.233252 29.011754 47.245006 9.031677 91.330212 9.478768 11:40:41 09/11/2024
5 17.495226 29.091952 46.587178 9.28772 91.292437 10.125332 11:41:41 09/11/2024
6 19.680554 29.005514 48.686068 8.947613 91.195334 10.164337 11:42:41 09/11/2024
7 20.297351 28.734791 49.032142 8.889665 91.730088 9.734649 11:43:42 09/11/2024
8 18.359268 28.931828 47.291096 9.120302 91.444002 10.80836 11:44:42 09/11/2024
9 17.076528 29.097028 46.173556 9.31479 91.632068 9.816705 11:45:42 09/11/2024
10 17.633503 28.747329 46.380832 9.159944 91.037191 11.504189 11:46:42 09/11/2024
11 17.960257 28.669294 46.629551 9.162861 91.885366 12.039561 11:47:42 09/11/2024
12 17.72177 29.2231 46.94487 9.223203 91.878373 11.212191 11:48:42 09/11/2024
13 18.374738 29.026804 47.401542 9.095606 90.892713 10.833537 11:49:43 09/11/2024
14 19.830407 28.655209 48.485616 8.870659 91.037395 10.577669 11:50:43 09/11/2024
15 18.99225 28.888542 47.880792 8.994642 90.741806 9.723277 11:51:43 09/11/2024
16 17.761278 28.946578 46.707856 9.211534 91.802406 9.730843 11:52:43 09/11/2024
17 17.801273 28.849913 46.651186 9.160453 91.378006 9.472927 11:53:43 09/11/2024
18 18.853268 28.886504 47.739772 9.0041 91.744613 9.559274 11:54:43 09/11/2024
19 18.664494 28.790517 47.455011 9.116042 90.939876 9.68862 11:55:43 09/11/2024
20 19.106723 28.834253 47.940976 8.997443 91.260138 9.347024 11:56:44 09/11/2024
21 17.289977 29.199065 46.489042 9.258254 91.428069 9.271439 11:57:44 09/11/2024
22 19.261076 29.039676 48.300752 8.952125 91.157102 9.552769 11:58:44 09/11/2024
23 19.073323 28.87338 47.946703 8.887989 91.161526 9.711229 11:59:44 09/11/2024
24 19.139368 28.596761 47.736129 8.942434 91.042196 9.740868 12:00:44 09/11/2024
25 20.938275 28.239823 49.178098 8.590529 89.956945 9.82264 12:01:44 09/11/2024
26 20.038064 28.802483 48.840547 8.819155 90.634788 10.019251 12:02:45 09/11/2024
27 20.770359 28.507742 49.278101 8.653204 90.377827 10.385452 12:03:45 09/11/2024
28 19.819211 28.897065 48.716276 8.835002 90.778086 10.051391 12:04:45 09/11/2024
29 20.197452 28.769329 48.966781 8.783727 91.219699 9.778166 12:05:45 09/11/2024
30 19.754255 28.71127 48.465525 8.774322 90.760234 10.468135 12:06:45 09/11/2024
31 19.781011 28.734264 48.515275 8.812416 89.736956 10.604562 12:07:45 09/11/2024
32 19.001064 29.1281 48.129164 8.960922 91.470393 10.297533 12:08:45 09/11/2024
33 19.795909 28.886434 48.682343 8.76174 91.795972 10.182683 12:09:46 09/11/2024
34 22.618165 27.975251 50.593416 8.421988 92.135237 9.550975 12:10:46 09/11/2024
35 21.685048 28.314481 49.999529 8.430728 90.770771 9.509624 12:11:46 09/11/2024
36 21.84096 28.106763 49.947723 8.445971 90.222546 10.11098 12:12:46 09/11/2024
37 20.33823 28.207375 48.545605 8.759661 89.689308 11.534681 12:13:46 09/11/2024
38 18.16978 29.299857 47.469637 9.06668 89.999668 10.575873 12:14:46 09/11/2024
39 18.436814 29.228646 47.66546 9.057625 91.030557 9.91664 12:15:46 09/11/2024
40 20.258857 28.607634 48.866491 8.745967 90.255666 9.774708 12:16:47 09/11/2024
41 20.328905 28.797697 49.126602 8.692352 90.540143 9.773838 12:17:47 09/11/2024
42 19.54424 28.806494 48.350734 8.819769 91.012008 9.362691 12:18:47 09/11/2024
43 17.457583 29.545956 47.003539 9.177145 91.632044 9.596436 12:19:47 09/11/2024
44 19.821736 29.103039 48.924775 8.712008 90.455244 9.4628 12:20:47 09/11/2024
45 21.404576 28.608682 50.013258 8.518447 90.060042 9.755343 12:21:47 09/11/2024
46 18.976808 29.233803 48.210611 8.853602 90.675587 9.903074 12:22:48 09/11/2024
47 19.66286 29.116748 48.779608 8.833377 90.975102 10.054693 12:23:48 09/11/2024
48 19.433631 28.978336 48.411967 8.878694 89.765712 10.860335 12:24:48 09/11/2024
49 18.097403 29.208962 47.306365 9.075362 89.877334 11.022936 12:25:48 09/11/2024
50 18.637303 29.186837 47.82414 8.960179 90.717645 10.454753 12:26:48 09/11/2024
51 17.841682 29.271388 47.11307 8.973527 91.760712 9.725821 12:27:48 09/11/2024
52 17.473215 29.304615 46.77783 9.076718 91.237413 9.93472 12:28:48 09/11/2024
53 17.215594 28.989824 46.205418 9.064057 91.764978 10.467446 12:29:49 09/11/2024
54 16.809836 29.00572 45.815556 9.267928 92.083724 11.41573 12:30:49 09/11/2024
55 17.165601 29.258351 46.423952 9.136598 91.359469 10.713804 12:31:49 09/11/2024
56 17.9848 28.890795 46.875595 9.015568 91.850826 10.006818 12:32:49 09/11/2024
57 17.481754 28.979554 46.461308 9.069072 91.754022 10.009957 12:33:49 09/11/2024
58 16.270993 29.264315 45.535308 9.296826 92.951437 10.065832 12:34:49 09/11/2024
59 16.009797 29.100277 45.110074 9.31266 92.955875 9.897468 12:35:50 09/11/2024
60 18.071736 29.51515 47.586886 8.994999 92.724475 9.771389 12:36:50 09/11/2024
AVG 18.87 28.92 47.79 8.96 91.15 10.10
ppm@15% O2 30.00 5.63 57.21
NOx
(g/bhp-hr)
NOx
(lbs/hr)
CO
(g/bhp-hr)
CO
(lbs/hr)
NMNEHC C3
(g/bhp-hr)
NMNEHC C3
(lbs/hr)
0.31 1.14 0.04 0.13 0.57 2.09
FTIR Measurements
E160518
Calculated Emission Levels
Uinta Wax Operating, LLC
Zager Booster Station
Run 3
Record Date
EPA REFERENCE METHOD 1 EPA REFERENCE METHOD 2
Stack Diameter 20 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 0.64 0.66 1254 0.35 0.812
Average O2 11.5 (% dry)A 2 2.10 0.69 0.831
Average CO2 5.6 (% dry)A 3 3.88 0.73 0.854
Average N2 + CO 82.9 (% dry)A 4 6.46 0.77 0.877
Dry Molecular Weight 29.36 lb/lbmol A 5 13.54 0.75 0.866
Wet Molecular Weight 28.21 lb/lbmol A 6 16.12 0.73 0.854
EPA REFERENCE METHOD 320 A 7 17.90 0.71 0.843
Barometric Pressure 24.63 in Hg A 8 19.36 0.68 0.825
Moisture Content 10.10 %A 9
EPA REFERENCE METHOD 320 A 10
Average Analyzer NOx Level 47.79 ppm A 11
Calculated NOx Mass Output 1.14 lbs/hr A 12
Calculated NOx Output 0.31 g/bhp-hr A 13
EPA REFERENCE METHOD 320 A 14
Average Analyzer CO Level 8.96 ppm A 15
Calculated CO Mass Output 0.13 lbs/hr A 16
Calculated CO Output 0.04 g/bhp-hr B 1 0.64 0.67 1254 0.35 0.819
EPA REFERENCE METHOD 320 B 2 2.10 0.70 0.837
Average Analyzer NMNEHC Level 91.15 ppm B 3 3.88 0.74 0.860
Calculated NMNEHC Mass Output 2.09 lbs/hr B 4 6.46 0.79 0.889
Calculated NMNEHC Output 0.57 g/bhp-hr B 5 13.54 0.77 0.877
LOAD APPROXIMATION B 6 16.12 0.74 0.860
Estimated Engine Load 1668.5 BHP B 7 17.90 0.71 0.843
B 8 19.36 0.72 0.849
B 9
B 10
B 11
B 12
B 13
B 14
B 15
B 16
Averages 0.7 1254 0.4 0.850
Average Stack Gas Velocity 81.94 ft/sec
Average Dry Flowrate 3345.62 dscfm
TEST RUN # 3

APPENDIX B

Date Time NO 191C span NO2 191C span H2O% (high) 191C Formaldehyde 191C Ethylene 191C TE span Propane 191C span Acetaldehyde 191C span CO ppm 191C (1of2) spanCO ppm Dry CO2% 191C NOx Wet NOx Dry NM NE HC C3 Temp ( C )Pressure (atm)9/11/2024 8:57:21 -0.13493 -0.039598 0.007781 -0.023594 0.399466 0.156227 -0.384025 0.009372 0.009373 -0.002086 -0.174529 -0.174542 0.00181 191.009888 1.0207389/11/2024 8:57:29 -0.057803 -0.000395 0.004987 0.030714 -0.173899 0.074846 0.032508 -0.006784 -0.006784 -0.002959 -0.058198 -0.0582 -0.00731 191.009888 1.0074489/11/2024 8:57:36 -0.097593 0.013582 0.002725 0.046513 -0.096533 0.059137 -0.137183 0.08174 0.081742 0.000604 -0.08401 -0.084013 -0.004384 191.009888 1.002609
9/11/2024 8:57:44 -0.059823 -0.007112 0.003017 -0.028071 -0.239402 -0.081223 0.119963 -0.118085 -0.118089 -0.000768 -0.066935 -0.066937 -0.007059 190.919296 1.0020099/11/2024 8:58:21 0 0 0 0 0 0 0 0 0 0 0 0 0 190.967438 1.002105
9/11/2024 8:58:34 -0.041106 0.030377 -0.000438 0.01832 0.258432 0.068527 -0.489379 0.027977 0.027977 -0.006988 -0.010729 -0.010729 0.004356 190.990814 1.0021599/11/2024 8:58:41 0.037315 -0.016928 -0.002168 -0.022521 -0.339562 0.254742 -0.327586 0.018056 0.018056 -0.002096 0.020387 0.020387 0.00195 190.990814 1.0022259/11/2024 8:58:49 0.112282 0.042665 -0.000992 0.02773 -0.016796 0.144423 0.207228 -0.01056 -0.01056 -0.004018 0.154947 0.154945 0.003523 190.990814 1.0022399/11/2024 8:58:56 0.126802 0.012224 -0.002266 -0.005291 0.133493 -0.158428 -0.132138 0.052338 0.052337 -0.00771 0.139026 0.139023 0.012837 190.990814 1.0022739/11/2024 8:59:04 0.162282 0.037348 -0.001363 -0.022078 0.002204 0.155108 0.006503 0.039324 0.039323 0.00203 0.19963 0.199627 0.003125 190.990814 1.0024389/11/2024 8:59:11 -0.088146 0.00316 -0.003971 -0.046645 0.038139 0.139734 0.079597 0.166158 0.166152 0.001829 -0.084986 -0.084983 0.007676 190.990814 1.0024889/11/2024 8:59:19 -0.008978 0.034921 -0.002118 -0.045394 -0.274889 0.120899 0.145112 -0.120308 -0.120306 0.001492 0.025942 0.025942 0.007368 190.990814 1.00248
9/11/2024 8:59:26 -0.058562 0.015468 -0.004624 -0.076863 -0.361763 0.190435 0.107261 0.034421 0.034419 -0.007327 -0.043095 -0.043093 0.001682 190.990814 1.0025379/11/2024 8:59:34 0.020344 -0.027571 -0.003141 -0.033701 0.153471 0.293783 -0.099911 0.084114 0.084111 0.000332 -0.007228 -0.007227 0.015466 190.990814 1.002604
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)9/11/2024 9:00:17 500.917663 515.329485 507.192125 191.051743 1.001678 9/11/2024 9:05:09 98.558878 191.054398 1.0088579/11/2024 9:00:25 500.201243 515.561798 507.217391 191.054398 1.001909 9/11/2024 9:05:17 99.195837 191.031693 1.008956
9/11/2024 9:00:32 500.512966 515.135418 507.693183 191.059845 1.002001 9/11/2024 9:05:24 98.887953 190.995361 1.0089689/11/2024 9:00:40 499.24131 514.217742 506.980233 191.06076 1.001951 9/11/2024 9:05:32 99.02547 190.984467 1.0090919/11/2024 9:00:47 498.544581 513.389309 503.911818 191.06076 1.001964 9/11/2024 9:05:39 98.792763 190.984467 1.0093659/11/2024 9:00:55 498.091753 513.819355 502.611671 191.06076 1.002084 9/11/2024 9:05:47 99.257149 190.984467 1.0093699/11/2024 9:01:02 497.980827 513.51404 504.723586 191.040894 1.002089 9/11/2024 9:05:54 99.17962 190.984467 1.0094789/11/2024 9:01:10 498.593515 514.199774 504.910659 191.001724 1.002139 9/11/2024 9:06:02 99.287261 190.984467 1.0095719/11/2024 9:01:17 498.717898 514.583346 504.833057 190.997177 1.002348 9/11/2024 9:06:09 98.942383 190.984467 1.009679
9/11/2024 9:01:25 498.803688 514.697694 504.714834 190.997177 1.002391 9/11/2024 9:06:17 99.12128 190.984467 1.009797
Date Time NO2 191C span Temp ( C )Pressure (atm)9/11/2024 9:03:34 144.419252 190.978104 1.004229/11/2024 9:03:42 144.571637 190.978104 1.0042689/11/2024 9:03:49 144.741784 190.978104 1.004324
9/11/2024 9:03:57 144.754174 190.981735 1.0044999/11/2024 9:04:04 144.807139 191.00354 1.0045469/11/2024 9:04:12 144.649614 191.052582 1.0046319/11/2024 9:04:19 144.68836 191.054398 1.0047319/11/2024 9:04:27 144.70018 191.054398 1.0047599/11/2024 9:04:34 144.528126 191.054398 1.0047699/11/2024 9:04:42 144.874739 191.054398 1.004886
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)9/11/2024 9:06:47 116.942577 150.771683 131.040779 190.984467 0.988925 9/11/2024 9:09:01 32.264704 190.965393 0.9896349/11/2024 9:06:54 311.265202 336.909326 337.079355 190.984467 0.989518 9/11/2024 9:09:09 87.701001 190.965393 0.9893819/11/2024 9:07:02 313.552456 336.824856 331.836012 190.984467 0.994727 9/11/2024 9:09:16 93.559535 190.982651 0.9893329/11/2024 9:07:09 472.882014 488.609942 473.648281 190.984467 1.008627 9/11/2024 9:09:24 95.54742 191.027374 0.989214
9/11/2024 9:07:17 500.67594 515.40044 502.880121 190.982071 1.006039 9/11/2024 9:09:31 95.278171 191.041687 1.0103229/11/2024 9:07:24 501.811135 516.038891 505.318699 190.978104 1.005836 9/11/2024 9:09:39 99.488903 191.041687 1.016589
9/11/2024 9:07:32 502.094709 516.499188 506.05321 190.920883 1.005913 9/11/2024 9:09:46 99.439469 191.041687 1.0134389/11/2024 9:07:39 502.069131 516.698516 505.584016 190.889084 1.005934 9/11/2024 9:09:54 99.251251 191.041687 1.0130879/11/2024 9:07:47 502.161492 516.816217 505.924874 190.889084 1.006059 9/11/2024 9:10:01 99.720303 191.041687 1.0132539/11/2024 9:07:55 503.284307 517.459385 506.987496 190.889084 1.006045 9/11/2024 9:10:09 99.418143 191.041687 1.013264
Date Time CO ppm 191C (1of2) span NOx Wet Propane 191C span Ethylene 191C TE Temp ( C )Pressure (atm)9/11/2024 9:10:32 0.23679 0.174483 0.302841 0.267128 191.041687 1.0082539/11/2024 9:10:39 0.167372 0.140708 -0.037074 0.098668 191.041687 1.0083639/11/2024 9:10:47 0.112829 0.141706 0.181446 0.330743 191.041687 1.00859/11/2024 9:10:54 0.179125 0.24244 -0.00174 0.175841 191.041687 1.0085389/11/2024 9:11:02 0.135563 -0.036474 0.406216 -0.234633 191.041687 1.008697
9/11/2024 9:11:09 0.028484 0.134526 0.261275 0.214082 191.041687 1.0087189/11/2024 9:11:17 0.04328 0.157212 -0.079429 0.102383 191.041687 1.008807
9/11/2024 9:11:24 0.074878 0.016085 0.163083 -0.08285 191.041687 1.00889
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)
9/11/2024 9:30:43 5.17961 64.759417 191.022614 1.0005539/11/2024 9:30:51 5.170699 64.92222 191.008987 1.0014369/11/2024 9:30:58 5.133231 64.21158 190.996262 0.9998769/11/2024 9:31:06 4.968344 63.075064 190.962997 0.9925429/11/2024 9:31:13 4.98259 62.854398 190.952667 0.9930699/11/2024 9:31:51 5.104331 64.589199 190.952667 0.9973379/11/2024 9:31:58 3.946785 144.486387 190.952667 1.004115
9/11/2024 9:32:06 3.032628 227.796601 190.952667 1.0031219/11/2024 9:32:13 3.860085 159.206189 190.952667 1.000949/11/2024 9:32:21 4.723472 96.123955 190.952667 1.0004269/11/2024 9:32:28 4.614944 104.794453 190.952667 1.0013679/11/2024 9:32:36 4.169605 140.482595 190.96698 1.0019999/11/2024 9:32:43 4.177622 139.525009 191.015335 1.0021629/11/2024 9:32:51 4.48484 116.32046 191.028961 1.001542
9/11/2024 9:32:58 4.51238 114.397841 191.028961 1.0023259/11/2024 9:33:44 4.565154 107.931374 191.026123 1.001899
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)9/11/2024 12:53:00 496.532534 511.362468 499.468515 191.016251 1.005939 9/11/2024 12:51:22 97.683927 191.015198 1.0066999/11/2024 12:53:08 498.892174 514.30288 502.855826 191.016251 1.006114 9/11/2024 12:51:29 98.960301 191.007172 1.007215
9/11/2024 12:53:15 500.388577 515.815085 505.445987 191.016251 1.006209 9/11/2024 12:51:37 98.812448 190.997177 1.007399/11/2024 12:53:23 501.358798 516.156588 504.084859 191.016251 1.00608 9/11/2024 12:51:44 99.069828 190.988998 1.007769/11/2024 12:53:30 500.852024 516.074008 502.770718 191.016251 1.006212 9/11/2024 12:51:52 98.682941 190.975723 1.0078749/11/2024 12:53:38 501.11187 516.270919 504.044783 191.016251 1.00632 9/11/2024 12:51:59 98.778185 190.957214 1.0079189/11/2024 12:53:45 500.561577 515.747326 504.068304 191.016251 1.006174 9/11/2024 12:52:07 98.937903 190.952667 1.0080139/11/2024 12:53:53 500.66707 515.800548 503.098818 191.016251 1.006396 9/11/2024 12:52:14 99.20031 190.955856 1.008089/11/2024 12:54:00 500.088869 515.27905 503.71191 191.016251 1.006326 9/11/2024 12:52:22 99.242614 190.95903 1.008185
9/11/2024 12:54:19 500.377598 515.583105 506.089908 191.016251 1.00631 9/11/2024 12:52:30 98.612632 190.962662 1.008202
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)9/11/2024 12:51:37 0.03965 0.228583 0.026715 190.997177 1.00739 9/11/2024 12:55:06 -0.299882 190.94632 1.0090149/11/2024 12:51:44 0.102293 0.020761 -0.359711 190.988998 1.00776 9/11/2024 12:55:14 -0.767321 190.94632 1.0098479/11/2024 12:51:52 -0.030305 0.107772 -0.088836 190.975723 1.007874 9/11/2024 12:55:22 -0.454696 190.993546 1.009745
9/11/2024 12:51:59 0.042541 0.10602 -0.110416 190.957214 1.007918 9/11/2024 12:55:29 -0.152005 191.035324 1.0097719/11/2024 12:52:07 0.065998 0.137144 -0.019134 190.952667 1.008013 9/11/2024 12:55:37 -0.154039 191.035324 1.0098049/11/2024 12:52:14 -0.08857 0.126747 -0.139277 190.955856 1.00808 9/11/2024 12:55:44 -0.445701 191.035324 1.0097859/11/2024 12:52:22 0.044271 0.171226 -0.130421 190.95903 1.008185 9/11/2024 12:55:52 -0.77228 191.035324 1.0099229/11/2024 12:52:30 0.065335 0.27509 0.107441 190.962662 1.008202 9/11/2024 12:55:59 -0.363228 191.035324 1.009955
SAMPLE SPIKE RECOVERY
POST SYSTEM CAL
POST SYSTEM ZERO
PRE TEST 1 497.5 5.0 62.9 4.5 114.4 0.094 99.4%
Sensor Analyzer Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Error (%)Error (%)
NOx 514.7 514.5 0.1 0.04 0.01
CO 498.8 501.8 0.0 -0.60 0.01
Propane 504.7 497.5 0.1 1.45 0.02
Ethylene 99.1 99.76 -0.1 -0.64 -0.07
Sensor System Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)
NOx 517.5 514.5 0.1 0.58 0.03
CO 503.3 501.8 0.1 0.30 0.03
Propane 507.0 497.5 0.1 1.91 0.03
Ethylene*99.4 99.76 0.1 -0.34 0.14
Sensor System Cal Zero Cal Zero Cal Zero
Response (ppm)Level (ppm)Response (ppm)Recovery (%)Error (%)Drift Error (%)Drift Error (%)
NOx 515.6 514.5 0.1 0.21 0.02 0.36 0.00
CO 500.4 501.8 0.0 -0.28 0.01 0.58 0.02
Propane 506.1 497.5 -0.1 1.73 -0.02 0.18 0.05
Ethylene*98.6 99.76 -0.4 -1.15 -0.37 0.81 0.50
*CTS Scans are conducted with Ethylene through the sample line.
Lf
5.11
Lr Cr Tr Pr Lr/Lf
5.09 99.1 191.0 1.0 1.00
Ls Cs Ts Ps Ls/Lf
5.06 99.4 191.0 1.0 0.99
% 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
Uinta Was Operating – Zager
9-11-2024

Uinta Was Operating – Zager
9-11-2024

Uinta Was Operating – Zager
9-11-2024

Spectral Fit

Run 1

Spectral Fit

Run 2

Spectral Fit

Run 3

Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000142.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000068.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000069.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000070.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000071.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000072.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000073.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000074.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 16.95 1.44 -0.24 0.32 1.96 1.96 -0.79 --0-2795 1.03 Good
NO2 191C 25.17 0.34 -0.03 0.03 0.36 0.36 -0.5 --0-488 0.99 Good
N2O 191C 0.21 0.14 0.23 0.03 0.03 0.16 0.16 0.25 0.25 0.02 0.08 0-200 -Close to DL
NH3 TE 191C -4.37 25.1 3.32 4.14 7.06 42.84 42.84 4.45 21.05 1.13 1.11 0-2995 -Close to DL
H2O% (HIGH) 191C10.21 0.2 -0.02 0.03 0.32 0.32 -0.2 --0-40 -Good
FORMALDEHYDE 191C13.31 0.86 -0.24 0.27 0.99 0.99 -0.35 --0-69 -Good
FORMIC ACID 191C TE1.56 16.85 1.15 1.56 1.83 19.72 19.72 1.34 15.3 0.19 0.38 0-466 -Close to DL
CH4 2900 CM-1 191C995.86 21.85 -1.63 2.37 40.41 40.41 -19.92 --0-3143 0.97 Good
PROPANE 191C63.14 2.09 -0.22 0.27 2.51 2.51 -1.26 --0-4976 0.95 Good
PROPYLENE 191C TE3.11 15.91 3.09 1.57 1.86 18.82 18.82 3.41 14.27 0.32 1.03 0-194 -Close to DL
ETHANE 191C 116.3 4.49 -0.55 0.85 6.99 6.99 -2.37 --0-1004 -Good
ETHYLENE 191C TE6.94 23.9 7.36 2.07 2.55 29.48 29.48 8.31 21.69 0.95 2.45 0-900 -Close to DL
CO PPM 191C (1OF2)8.17 0.62 -0.25 0.55 1.15 1.15 -0.21 --0-5010 1.01 Good
CO2% 191C 5.08 0.09 -0.01 0.02 0.12 0.12 -0.1 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C2.95 2.09 2.38 0.64 0.82 2.68 2.68 2.65 2.65 0.27 0.79 0-186 1 Close to DL
ACETYLENE 191C0.27 2.21 0.4 0.79 1.05 2.92 2.92 0.44 1.45 0.04 0.13 0-1016 -Close to DL
SO2 191C 1.11 2.61 0.67 0.26 0.32 3.19 3.19 0.81 2.36 0.14 0.22 0-964 1.02 Close to DL
HEXANE 191C 6.07 1.32 6.31 0.13 0.18 1.79 1.79 7.06 7.06 0.75 2.1 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000203.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000068.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000069.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000070.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000071.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000072.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000073.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000074.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 16.61 1.37 -0.24 0.32 1.88 1.88 -0.75 --0-2795 1.03 Good
NO2 191C 25.82 0.34 -0.03 0.03 0.36 0.36 -0.52 --0-488 0.99 Good
N2O 191C 0.21 0.14 0.23 0.03 0.03 0.16 0.16 0.25 0.25 0.02 0.08 0-200 -Close to DL
NH3 TE 191C -5.8 23.7 3.32 4.14 7.06 40.46 40.46 4.45 19.62 1.13 1.11 0-2995 -Close to DL
H2O% (HIGH) 191C9.38 0.18 -0.02 0.03 0.3 0.3 -0.19 --0-40 -Good
FORMALDEHYDE 191C15.45 0.9 -0.24 0.27 1.03 1.03 -0.36 --0-69 -Good
FORMIC ACID 191C TE1.53 17.03 1.15 1.56 1.83 19.94 19.94 1.34 15.48 0.19 0.38 0-466 -Close to DL
CH4 2900 CM-1 191C993.95 21.71 -1.63 2.37 40.16 40.16 -19.88 --0-3143 0.97 Good
PROPANE 191C63.48 2.11 -0.22 0.27 2.54 2.54 -1.27 --0-4976 0.95 Good
PROPYLENE 191C TE3.52 15.99 3.09 1.57 1.86 18.91 18.91 3.41 14.34 0.32 1.03 0-194 -Close to DL
ETHANE 191C116.06 4.53 -0.55 0.85 7.05 7.05 -2.38 --0-1004 -Good
ETHYLENE 191C TE6.96 23.73 7.36 2.07 2.55 29.26 29.26 8.31 21.51 0.95 2.45 0-900 -Close to DL
CO PPM 191C (1OF2)8.38 0.58 -0.25 0.55 1.08 1.08 -0.19 --0-5010 1.01 Good
CO2% 191C 5.1 0.09 -0.01 0.02 0.12 0.12 -0.1 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C2.43 2.08 2.38 0.64 0.82 2.67 2.67 2.65 2.65 0.27 0.79 0-186 1 Close to DL
ACETYLENE 191C0.16 2.12 0.4 0.79 1.05 2.8 2.8 0.44 1.37 0.04 0.13 0-1016 -Close to DL
SO2 191C 0.57 2.48 0.67 0.26 0.32 3.02 3.02 0.81 2.24 0.14 0.22 0-964 1.02 Close to DL
HEXANE 191C 6.15 1.34 6.31 0.13 0.18 1.81 1.81 7.06 7.06 0.75 2.1 0-1000 -Close to DL
Analysis Validation Report
Sample Filename: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000264.LAB
Filename for noise: C:\OLT\Data\Golden Spectrum 10-31-23\GOLDEN SPECTRUM 10-31-23_000004.LAB
Interferences Filenames: C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000068.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000069.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000070.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000071.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000072.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000073.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000074.LAB
C:\OLT\Data\Finley Resources\Zager BS E1 9-11-24\UWO ZAGER BS E1 9-11-24_000075.LAB
Recipe path: C:\OLT\RECIPES\STEPHEN PYER TEST.MGRCP
Gas calibration NameConc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL ~ CL ~ Bias Sigma Range Span Comment
NO 191C 15.34 1.39 -0.24 0.32 1.89 1.89 -0.78 --0-2795 1.03 Good
NO2 191C 26.57 0.35 -0.03 0.03 0.37 0.37 -0.53 --0-488 0.99 Good
N2O 191C 0.2 0.15 0.23 0.03 0.03 0.17 0.17 0.25 0.25 0.02 0.08 0-200 -Close to DL
NH3 TE 191C -5.73 24.76 3.32 4.14 7.06 42.26 42.26 4.45 20.67 1.13 1.11 0-2995 -Close to DL
H2O% (HIGH) 191C9.93 0.2 -0.02 0.03 0.32 0.32 -0.2 --0-40 -Good
FORMALDEHYDE 191C12.87 0.66 -0.24 0.27 0.76 0.76 -0.26 --0-69 -Good
FORMIC ACID 191C TE1.59 16.78 1.15 1.56 1.83 19.65 19.65 1.34 15.23 0.19 0.38 0-466 -Close to DL
CH4 2900 CM-1 191C981.16 22.38 -1.63 2.37 41.4 41.4 -19.62 --0-3143 0.97 Good
PROPANE 191C62.79 2.09 -0.22 0.27 2.51 2.51 -1.26 --0-4976 0.95 Good
PROPYLENE 191C TE3.28 15.85 3.09 1.57 1.86 18.75 18.75 3.41 14.21 0.32 1.03 0-194 -Close to DL
ETHANE 191C116.47 4.47 -0.55 0.85 6.96 6.96 -2.37 --0-1004 -Good
ETHYLENE 191C TE6.9 23.82 7.36 2.07 2.55 29.38 29.38 8.31 21.61 0.95 2.45 0-900 -Close to DL
CO PPM 191C (1OF2)8.22 0.56 -0.25 0.55 1.03 1.03 -0.18 --0-5010 1.01 Good
CO2% 191C 5.04 0.09 -0.01 0.02 0.12 0.12 -0.1 --0-23 -Good
CO% 191C (2OF2)0 0 0 0 0 0 0 0 0 0 0 0-8 -Close to DL
ACETALDEHYDE 191C2.53 2.11 2.38 0.64 0.82 2.71 2.71 2.65 2.65 0.27 0.79 0-186 1 Close to DL
ACETYLENE 191C0.16 2.2 0.4 0.79 1.05 2.91 2.91 0.44 1.45 0.04 0.13 0-1016 -Close to DL
SO2 191C 0.96 2.58 0.67 0.26 0.32 3.14 3.14 0.81 2.33 0.14 0.22 0-964 1.02 Close to DL
HEXANE 191C 5.98 1.32 6.31 0.13 0.18 1.79 1.79 7.06 7.06 0.75 2.1 0-1000 -Close to DL

APPENDIX C

Test Run Load %Site Rated Load, bhp Load Approx., bhp
1 95 1775 1686.3
2 94 1775 1668.5
3 94 1775 1668.5
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 3259.51 1686.3 11.6 45.84 0.29 1.07 9.14 0.03 0.13 92.64 0.56 2.07 10.16
2 3383.36 1668.5 11.5 47.64 0.31 1.15 9.10 0.04 0.13 90.92 0.57 2.11 10.00
3 3345.62 1668.5 11.5 47.79 0.31 1.14 8.96 0.04 0.13 91.15 0.57 2.09 10.10
1674.4 11.5 47.09 0.30 1.12 9.07 0.04 0.13 91.57 0.57 2.09 10.09
Summary
Average Levels
Example Calculations: Uinta Wax Operating, LLC, Zager Booster Station, E160518

The following is a step-by-step calculation for the first test run conducted on the Zager Booster
Station E160518.

Test Parameters • Stack Diameter = 20 inches • Traverse Points = 16 • Ports = 2 • Barometric Pressure = 24.63 in Hg • Average O2 = 11.6% • Average CO2 = 5.6% • Load Approximation = 1686.3 bhp • Moisture Content = 10.16%

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 = 5.6%
%O2 – Oxygen Content Of The Gas = 11.6% %N2 – Nitrogen Content Of The Gas %CO – Carbon Monoxide Content Of The Gas
(%N2 +%CO) = (100 - %O2 - %CO2)
= (100 – 11.6 – 5.6)
= 82.8% Dry

= (0.44 * %CO2) + (0.32 * %O2) + ((0.28 * (%N2 + %CO))
= (0.44 * 5.6) + (0.32 * 11.6) + (0.28 * 82.8) = 29.36 lb/lbmol

Wet Molecular Weight (lb/lbmol)
= MD * (1-BWS) + (18) * BWS
Where:
MD – Molecular Weight Of The Dry Gas (lb/lbmol) = 29.36 lb/lbmol
BWS – Moisture Content Of The Gas (%/100) = 10.16%
= MD * (1-BWS) + (18) * BWS
= 29.36 * (1 – (10.16/ 100)) + (18 * (10.16/ 100))

= 28.21 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) = 0.828 in H2O
TS – Average stack temperature (R) = 1254 R PB – Barometric pressure (in Hg) = 24.63 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.3 in H2O MA – Molecular weight of the wet gas (lb/lbmol) = 28.21 lb/lbmol

= Cp * (85.49) * ∆PAVG * (TS / (((PS / 13.6) + PB) * MA))
= 0.84 * (85.49) * 0.828 * ( 1254 / (((0.3/ 13.6) + 24.63) * 28.21))
= 79.89 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) = 20 inches BWS – Moisture content of the gas (%) = 10.16%
TSTD – Standard temperature (528R)
TS – Average stack temperature (R) = 1254 R
PB – Barometric pressure (in Hg) = 24.63 in Hg
PS – Stack pressure relative to barometric pressure (inches water) = 0.3 in H2O
VS– Average Stack gas velocity (ft/sec) = 79.89 ft/sec

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

= 60 * (1 - (10.16/ 100)) * 79.89 *  * (((20 / 2) / 12))2) * 528 / 1254 * (24.63 + (0.3 /
13.6)) / 29.92

= 3259.51 dscfm

Conversion of Dry Flowrate to m3/hr
= Q * 60 * 2.83168*10 -2 Where:
Q – Volumetric Flowrate = 3259.51 dscfm 2.83168*10 -2 – Conversion factor for cubic feet to cubic meter
60 – Minutes in an hour
= Q * 60 * 2.83168*10 -2

= 3259.51 *60 * 2.83168*10 -2 = 5537.94 m3/hr

ASTM D 6348-03: Determination of NOx, CO and VOC Emissions From Stationary Sources NOx Emission Rate (g/Bhp-hr)
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
Where:
Cd – Measured NOx concentration in ppm = 45.84 ppm 1.92*10 -3 - Conversion constant for ppm to g/m3 NOx
Q – Volumetric Flowrate = 5537.94 m3/hr
T – Time in Hours of Test Run = 1 hr HP-hr – Unit Brake Horsepower = 1686.3 Bhp
= (Cd * 1.912*10 -3 * Q * T) / HP-hr
= (45.84 * 1.912*10 -3 * 5537.94 * 1) / 1686.3
= 0.29 g/Bhp-hr

NOx Emission Rate (lbs/hr) = g/Bhp-hr / 454 * Bhp
Where: g/Bhp-hr = 0.29 g/Bhp-hr
454 – Conversion factor for g to lbs Bhp - Unit Brake Horsepower = 1686.3 Bhp

= g/Bhp-hr / 454 * Bhp = 0.29 / 454 * 1686.3
= 1.07 lbs/hr
CO Emission Rate (g/Bhp-hr)
= (Cd * 1.164*10 -3 * Q * T) / HP-hr
Where: Cd – Measured CO concentration in ppm = 9.14 ppm
1.164*10 -3 - Conversion constant for ppm to g/m3 CO
Q – Volumetric Flowrate = 5537.94 m3/hr T – Time in Hours of Test Run = 1 hr
HP-hr – Unit Brake Horsepower = 1686.3 Bhp = (Cd * 1.164*10 -3 * Q * T) / HP-hr
= (9.14 * 1.164*10 -3 * 5537.94 * 1) / 1686.3

= 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 = 1686.3 Bhp = g/Bhp-hr / 454 * Bhp
= 0.03 / 454 * 1686.3
= 0.13 lbs/hr
VOC Emission Rate (g/Bhp-hr) = (Cd * 1.833*10 -3 * Q * T) / HP-hr
Where: Cd – Measured VOC concentration in ppm = 92.64 ppm
1.833*10 -3 - Conversion constant for ppm to g/m3 VOC
Q – Volumetric Flowrate = 5537.94 m3/hr T – Time in Hours of Test Run = 1 hr HP-hr – Unit Brake Horsepower = 1686.3 Bhp
= (Cd * 1.833*10 -3 * Q * T) / HP-hr
= (92.64 * 1.833*10 -3 * 5537.94 * 1) / 1686.3 = 0.56 g/Bhp-hr
VOC Emission Rate (lbs/hr)
= g/Bhp-hr / 454 * Bhp Where:
g/Bhp-hr = 0.56 g/Bhp-hr 454 – Conversion factor for g to lbs Bhp - Unit Brake Horsepower = 1686.3 Bhp
= g/Bhp-hr / 454 * Bhp
= 0.56 / 454 * 1686.3 = 2.07 lbs/hr

APPENDIX E

FTIR Engine Test Sheet

Company Name f);l1ta L./~,~
Location / Unit I.D. 1:-e.,q~ t" Ri Fl..
Type of Test Completed 3x1hr Nt.V
Field Technician (5) David Martinez
Client Rep and/or State Rep .:soh", .... /Jr" h
Date q-U~'"
Non-Resettable Run Time Hours ~6~t)~ Stack Diagram
Engine Make C.AT
Engine Model I, ~,j;b' l, £ .. "'-""""'''''''''-''''''''." """""'-"""";"'~"'''''-
Engine SIN '( tS.bO"O~ r~"-·"·_· ........•..._--"".", TPort Distance A '10 ~'"Port Distance 8 '~I..\ A·'
Exhaust Diameter (inches) '~.l\l7 tCalibration Gas Cylinder # Concentration ( ~.
NO (ppm CC745222 514.5
CO (ppm CC450607 501.8
Propane (ppm ND46380 497.5
N02 (ppm) CC510760 144 t B
.." f 1Ethylene (ppm CC127876 99.97 j
Methane (ppm CC471136 494.5 "Gas'_·.j
Acetaldehyde 'ppm) XC0155878 199.1 :...­
Test 1 Test 2 Test 3
Time of Reading c1,3S W:36 11:3,
Atm Pressure (in Hg) -a1.1, {.,J.. (1'J ,/'3 1'1,(3
Atm Temp CF) c 6 ~ tq
Engine RPM ------------­lf~o q< l qC/
*Manifold Pres. Vae(") OJ' Boost(psi})or Boost (psia) ~'"i ~l 'SCJ Manifold Temo ('F) <; ~ \o.-b ") 13/
Psuction psi) Stage 1 S~., S,() S6~
Tsuction CF) Stage 1 ----
Pdischarqe (psi) Staae 1 I p., I fJ..\!. y;1t-l 1....,~D fl"/6 /'1~'1 f!:(;>!/7So
Psuction psi) Stage 2 \
Tsuction CF) Stage 2
Pdischarr e (psi) Stage 2
Psuction psi) Stage 3
Tsuction OF) Stage 3
Pdischarae (psi) Staae 3
Psuction (psi) Stage 4
Tsuction CF) Stage 4 I
Pdischarge (psi) Stage 4 A I
Gas Throughput (mmef/d) or ( SL~"' ) \b 1
Pre Cat Temp CF) ., ~"l ., l~ 7:l.5
Post Cat Temp CF) 14(,\ It " ~rt{
Cat Differential Pres. (" of H2O) n.~ O.~ 0,f<
Humidity % ---02% lU. I\, !i. 1/.5C02 % Dry S.b .'\ ~ S,
LOAD % (l'"anel) or (Estimated) CiS <fL./ '1't Ignition TimingT F ".\ \1.1 n.)
AFR Setting mV r. ",ft R<>nl<\ J...~tJ d.>., 1.3.)
AFR SettinQ mV Dc::<, Af­-1).,:~.~ fl<.~ dS. &­
Rev 8 • Some units show boost in inches of Hg. In this situation please indicate if it is
positive (+) or negative(-), Eg: (+12") or (- 5'')
9/17/2019
Worksheet: O2 Stratification
Client:Uinta Wax Operating
Location:Zager Booster Station
Date:9/11/2024
PD:20
DD:144 YES Method 1 Criteria Met
UD:38 YES Method 1 Criteria Met
Port Point Insertion Depth Reading
(inches)(%)
A 1 3.32 11.60
A 2 10.00 11.50
A 3 16.66 11.50
A 4
A 5
A 6
A 7
A 8
A 9
A 10
A 11
A 12
Average 11.53
Notes: To demonstrate non-stratified flow and utilize one sampling location
O2 may not deviate by more than +/- 0.3% of the average O2 concentration.
EPA REFERENCE METHOD 3A (Determination Of Stratification)
COMPANY NAME:Uinta Wax Operating COMPANY LOCATION:Zager Booster Station DATE:9/11/2024
STACK DIAMETER (inches):20 TRAVERSE POINTS:16 2
TEST RUN #1 TEST RUN #2 TEST RUN #3
AVERAGE O2:11.6 AVERAGE O2:11.5 AVERAGE O2:11.5
AVERAGE CO2:5.6 AVERAGE CO2:5.6 AVERAGE CO2:5.6
BARO PRESSURE:24.63 BARO PRESSURE:24.63 BARO PRESSURE:24.63
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 0.64 0.62 794 0.33 1 0.64 0.69 796 0.36 1 0.64 0.66 794 0.35
2 2.1 0.65 2 2.1 0.72 2 2.1 0.69
3 3.88 0.69 3 3.88 0.75 3 3.88 0.73
4 6.46 0.73 4 6.46 0.79 4 6.46 0.77
5 13.54 0.71 5 13.54 0.78 5 13.54 0.75
6 16.12 0.68 6 16.12 0.74 6 16.12 0.73
7 17.9 0.66 7 17.9 0.72 7 17.9 0.71
8 19.36 0.64 8 19.36 0.71 8 19.36 0.68
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 0.64 0.63 794 0.33 1 0.64 0.68 796 0.36 1 0.64 0.67 794 0.35
2 2.1 0.66 2 2.1 0.73 2 2.1 0.7
3 3.88 0.7 3 3.88 0.77 3 3.88 0.74
4 6.46 0.74 4 6.46 0.8 4 6.46 0.79
5 13.54 0.77 5 13.54 0.78 5 13.54 0.77
6 16.12 0.73 6 16.12 0.75 6 16.12 0.74
7 17.9 0.71 7 17.9 0.72 7 17.9 0.71
8 19.36 0.67 8 19.36 0.69 8 19.36 0.72
9 9 9
10 10 10
11 11 11
12 12 12
13 13 13
14 14 14
15 15 15
16 16 16