DAQ-2024-010880

1

DAQC-1012-24
Site ID 15971 (B4)

MEMORANDUM

TO: STACK TEST FILE – RAMSEY HILL EXPLORATION, LLC – RHEx Vernal
Sand Mine – Uintah County

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

FROM: Kyle Greenberg, Environmental Scientist

DATE: October 3, 2024

SUBJECT: Source: Sand Dryer #3 and Crusher #2
Contact: Mike Cina: 715-821-1866 Ext. 6
Location: 1015 East 12600 North, Cove, UT 84320
Test Contractor: Western Environmental Services and Testing, Inc.
Permit/AO#: DAQE-AN159710004-23, dated July 31, 2023
Action Code: TR
Subject: Review of Stack Test Report dated July 23, 2024
On July 23, 2024, the Utah Division of Air Quality (DAQ) received a test report for the Sand Dryer #3
and Crusher #2 at the RHEx Vernal Sand Mine in Uintah County, Utah. Testing was performed on May
29, 2024, to demonstrate compliance with the emission limits found in in Conditions II.B.2.a and II.B.4.e
of Approval Order DAQE-AN159710004-23, 40 CFR Part 60 Subpart OOO, and 40 CFR Part 60 Subpart
UUU. The DAQ-calculated test results are:

Source Test Date Test
Methods Pollutants Tester Results DAQ Results Limits
Sand Dryer #3 May 29,
2024
M5 PM 0.262 lb/hr
0.00235 gr/dscf
0.2777 lb/hr
0.0025 gr/dscf
0.61 lb/hr
0.01 gr/dscf
9 VEO 0.14 % N/A 10%
7E NOx
1.56 lb/hr

77.88 ppm
@3%O2
1.562 lb/hr

78.161 ppm
@3%O2
2.9 lb/hr

96 ppm
@3%O2
Crusher #2 May 29,
2024 9 VEO 0 % N/A 10%

DEVIATIONS: None.

CONCLUSION: The stack test appears to be acceptable.

RECOMMENDATION: The Sand Dryer #3 was operating at an average of 184 tons per hour of
throughput during the time of testing. It is recommended the Sand Dryer
#3 and Crusher #2 be considered as in compliance with their VEO and
PM emission limits, during the time of testing.

2

HPV: None.

ATTACHMENTS: Ramsey Hill Exploration’s Stack Test Report, DAQ excel worksheets
Ramsey Hill Exploration, LLC
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT
Sand Dryer #3
Test Date: 5/29/2024
EPA Methods 5 & 202: Determination of Particulate and Condensible Particulate Emissions
from Stationary Sources
Run # 1 2 3 Average
date 5/29/2024 5/29/2024 5/29/2024
start time 11:45 15:50 9:33
stop time 15:19 9:10 11:03
sampling time (minutes) 120.0 120.0 120.0 60.0
DS stack diameter (inches) 41.13 41.13 41.13 41.13
PAVG average (delta P)½ (" H2O)½0.6002 0.5965 0.5922 0.5963
CP pitot tube constant (unitless) 0.837 0.837 0.837 0.84
TS stack temp. (°F) 187.0 190.0 187.0 188.0
Pbar barometric pressure (" Hg) 24.22 24.22 24.22 24.22
Ps stack pressure (" H2O)0.54 0.54 0.54 0.54
Yd meter box Yd (unitless)0.9780 0.9780 0.9780 0.978
Tm meter temp. (°F) 74.00 79.00 82.00 78.33
Vm sample volume (ft3)89.107 90.090 89.250 89.482
H orifice setting delta H (" H2O)1.350 1.350 1.310 1.3
Vlc moisture (g) 289.8 277.9 277.8 281.8
O2%vd oxygen (%vd) 17.0 17.0 17.1 17.0
CO2%vd carbon dioxide (%vd) 2.6 2.7 2.7 2.7
DN nozzle diameter (inches) 0.2790 0.2780 0.2790 0.2787
Run # 1 2 3 Average
grams mass particulate front half (g) 0.0075 0.0067 0.0033 0.00583
grams mass particulate filter (g) 0.0026 0.0069 0.0069 0.00547
Run # 1 2 3 Average
Vmstd sample volume (dscf) 69.994 70.110 69.063 69.722
sample volume (dscm) 1.982 1.985 1.956 1.974
Vwstd moisture volume (dscf) 13.667 13.106 13.101 13.291
Bws measured moisture content (%/100) 0.163 0.157 0.159 0.160
saturated moisture content (%/100) 0.735 0.784 0.735 0.751
actual moisture content (%/100) 0.163 0.157 0.159 0.160
MD molecular weight (dry) 29.10 29.1136 29.11 29.11
MA molecular weight (actual) 27.29 27.37 27.34 27.33
VS gas velocity (ft/sec) 42.4 42.2 41.8 42.2
FACFM gas flow (acfm) 23,494 23,369 23,156 23,340
FDSCFM gas flow (dscfm) 13,012 12,974 12,885 12,957
lb/hr gas flow (lb/hr) 66,033 65,570 65,223 65,609
% % isokinetic 97.5 98.6 97.1 97.7 Permit
Limits
lb/hr F½ PM (lb/hr) 0.248 0.333 0.252 0.278
gr/dscf F½ PM (gr/dscf) 0.002 0.003 0.002 0.002
lb/hr Total PM (lb/hr) 0.2484 0.3330 0.2518 0.2777 0.61
gr/dscf Total PM (gr/dscf) 0.002 0.003 0.002 0.0025 0.01
Field Reference Method Data
Laboratory Data
Reference Method Calculations
Page 1 of 3
Ramsey Hill Exploration, LLC
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT
Sand Dryer #3
Test Date: 5/29/2024
EPA Methods 5 & 202: Determination of Particulate and Condensible Particulate Emissions
from Stationary Sources
Run 1 - Intermediate Isokinetic values
Point Dwell Time DGM ∆P √∆P ∆H Stack %
Temp ⁰F Inlet Outlet Isokinetics
1 5 150.476 0.38 0.6164 1.3 186 72 72 91.39
2 5 154.04 0.4 0.6325 1.4 187 72 72 93.33
3 5 157.77 0.43 0.6557 1.6 188 72 72 95.94
4 5 161.74 0.45 0.6708 1.7 189 72 72 97.66
5 5 165.87 0.48 0.6928 1.8 189 72 72 97.34
6 5 170.12 0.5 0.7071 1.9 190 72 72 98.17
7 5 174.49 0.38 0.6164 1.4 191 72 72 100.94
8 5 178.41 0.38 0.6164 1.4 191 73 73 98.95
9 5 182.26 0.31 0.5568 1.2 191 73 73 102.38
10 5 185.86 0.28 0.5292 1 190 73 73 97.42
11 5 189.12 0.25 0.5000 0.9 188 73 73 100.06
12 5 192.29 0.2 0.4472 0.75 180 73 73 101.00
13 5 195.171 0.3 0.5477 1.1 181 74 74 97.86
14 5 198.59 0.3 0.5477 1.1 188 74 74 93.24
15 5 201.83 0.34 0.5831 1.3 188 74 74 97.92
16 5 205.45 0.38 0.6164 1.4 187 74 74 96.67
17 5 209.23 0.4 0.6325 1.5 187 74 74 97.74
18 5 213.15 0.45 0.6708 1.7 186 74 74 97.78
19 5 217.31 0.48 0.6928 1.8 187 75 75 97.55
20 5 221.6 0.43 0.6557 1.6 186 75 75 98.61
21 5 225.71 0.38 0.6164 1.4 186 75 75 99.22
22 5 229.6 0.35 0.5916 1.3 185 76 76 100.17
23 5 233.38 0.28 0.5292 1 182 76 76 96.57
24 5 236.65 0.23 0.4796 0.9 175 76 76 100.17
239.742
Run 2 - Intermediate Isokinetic values
Point Dwell Time DGM ∆P √∆P ∆H Stack %
Temp ⁰F Inlet Outlet Isokinetics
1 5 239.905 0.28 0.5292 1.05 189 77 77 95.16
2 5 243.11 0.31 0.5568 1.2 189 77 77 99.37
3 5 246.63 0.34 0.5831 1.3 190 77 77 98.22
4 5 250.27 0.34 0.5831 1.3 190 77 77 99.30
5 5 253.95 0.4 0.6325 1.5 190 78 78 97.65
6 5 257.88 0.45 0.6708 1.7 189 78 78 97.20
7 5 262.03 0.48 0.6928 1.8 189 78 78 97.77
8 5 266.34 0.43 0.6557 1.6 189 78 78 99.65
9 5 270.5 0.4 0.6325 1.5 188 78 78 100.48
10 5 274.55 0.35 0.5916 1.3 188 79 79 99.21
11 5 278.3 0.3 0.5477 1.1 187 79 79 103.02
12 5 281.91 0.25 0.5000 0.9 179 79 79 101.74
13 5 285.187 0.4 0.6325 1.5 190 79 79 96.55
14 5 289.08 0.38 0.6164 1.4 189 79 79 97.35
15 5 292.91 0.4 0.6325 1.5 190 79 79 97.47
16 5 296.84 0.43 0.6557 1.6 192 79 79 95.14
17 5 300.81 0.45 0.6708 1.7 192 79 79 102.40
18 5 305.18 0.48 0.6928 1.8 193 79 79 95.62
19 5 309.39 0.38 0.6164 1.4 194 79 79 101.04
20 5 313.35 0.35 0.5916 1.3 194 80 80 99.22
21 5 317.09 0.33 0.5745 1.2 195 80 80 99.77
22 5 320.74 0.28 0.5292 1 194 80 80 96.90
23 5 324.01 0.23 0.4796 0.9 193 80 80 101.58
DGM Meter Temp ⁰F
DGM Meter Temp ⁰F
Page 2 of 3
24 5 327.12 0.2 0.4472 0.75 190 81 81 103.31
330.083
Run 3 - Intermediate Isokinetic values
Point Dwell Time DGM ∆P √∆P ∆H Stack %
Temp ⁰F Inlet Outlet Isokinetics
1 5 330.104 0.3 0.5477 1.1 189 81 81 97.61
2 5 333.55 0.34 0.5831 1.3 188 80 80 94.62
3 5 337.1 0.34 0.5831 1.3 189 80 80 104.03
4 5 341 0.43 0.6557 1.6 189 81 81 92.65
5 5 344.91 0.45 0.6708 1.7 189 81 81 97.78
6 5 349.13 0.48 0.6928 1.8 188 81 81 97.10
7 5 353.46 0.38 0.6164 1.4 189 81 81 100.26
8 5 357.44 0.32 0.5657 1.2 187 81 81 101.35
9 5 361.14 0.28 0.5292 1 184 81 81 96.06
10 5 364.43 0.28 0.5292 1 183 81 81 95.70
11 5 367.71 0.28 0.5292 1 183 82 82 94.94
12 5 370.97 0.28 0.5292 1 184 82 82 100.00
13 5 374.401 0.3 0.5477 1.1 188 82 82 94.62
14 5 377.75 0.3 0.5477 1.1 188 82 82 96.62
15 5 381.17 0.32 0.5657 1.2 188 82 82 96.87
16 5 384.71 0.35 0.5916 1.3 190 82 82 95.94
17 5 388.37 0.38 0.6164 1.4 190 82 82 96.88
18 5 392.22 0.4 0.6325 1.5 190 82 82 97.65
19 5 396.2 0.43 0.6557 1.6 189 82 82 97.45
20 5 400.32 0.4 0.6325 1.5 187 82 82 98.16
21 5 404.33 0.38 0.6164 1.4 187 82 82 97.91
22 5 408.23 0.35 0.5916 1.3 186 82 82 100.87
23 5 412.09 0.35 0.5916 1.3 184 82 82 95.49
24 5 415.75 0.35 0.5916 1.3 186 82 82 98.54
419.521
DGM Meter Temp ⁰F
Page 3 of 3
Emissions
Ramsey Hill Exploration, LLC
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT
Sand Dryer #3
Test Date: 5/29/2024
Run # 1 2 3 Average
Start Time 8:25 10:52 13:13
Stop Time 10:30 12:58 15:18
Sample Duration (minutes) 120 120 120
DS Stack Diameter (inches) 41.1 41.1 41.1 41.1PAVG Average (Delta P)½ (" H2O)½0.6002 0.5965 0.5922 0.5963
CP Pitot Tube Constant (unitless) 0.84 0.84 0.84 0.84
TS Stack Temperature (°F) 187 190 187 188
Pbar Barometric Pressure (" Hg) 24.22 24.22 24.22 24.22
Ps Stack Pressure ('' H2O)0.54 0.54 0.54 0.54
Yd Meter Y Factor (unitless) 0.9780 0.9780 0.9780 0.9780
Tm Meter Temperature (°F) 74 79 82 78
Vm Sample Volume (ft3)89.107 90.090 89.250 89.482
H Orifice Pressure Delta H (" H2O)1.4 1.4 1.3 1.3
Vlc Moisture (g) 289.8 277.9 277.8 281.8
O2%vd O2 (%vd)17.0 17.0 17.1 17.0
CO2%vd CO2 (%vd)2.6 2.7 2.7 2.7
N2%vd N2 (%vd)80.4 80.3 80.2 80.3
dry NOX (ppmvd)16.4 17.2 17.0 16.9
Run # 1 2 3 Average
Vmstd Sample Volume (dscf) 69.994 70.110 69.063 69.722
Vwstd Moisture Volume (scf) 13.67 13.11 13.10 13.29
Bws Measured Moisture Content (%/100) 0.163 0.157 0.159 0.160
Bws Saturated Moisture Content (%/100) 0.735 0.784 0.735 0.751
Bws Actual Moisture Content (%/100) 0.163 0.157 0.159 0.160
MD Molecular Weight Dry (lb/lb-mole) 29.10 29.11 29.11 29.11
MA Molecular Weight Wet (lb/lb-mole) 27.29 27.37 27.34 27.33
VS Gas Velocity (ft/sec) 42.5 42.2 41.8 42.2
FACFM Gas Flow (acfm) 23506 23381 23168 23351
FDSCFM Gas Flow (dscfm) 13004 12966 12877 12949
FWSCFM Gas Flow (wscfm) 15553 15399 15329 15427
FKWSCFH Gas Flow (kwscfh) 933 924 920 926
FKWSCFM Gas Flow (kwscfm) 16 15 15 15
lb/hr Gas Flow (lb/hr) 66086 65623 65275 65661
Fo Fo (unitless)1.503 1.430 1.418 1.450
wet O2 (%vw)14.2 14.4 14.4 14.3
wet CO2 (%vw)2.2 2.3 2.3 2.2
wet NOX (ppmvw)13.7 14.5 14.3 14.2
3 NOX (ppmvd @ 3% O2)75.076 79.611 79.797 78.161 96.0
lb/hr NOX (lb/hr)1.526 1.593 1.567 1.562 2.90
Permit Limits
Field Reference Method Data
Reference Method Calculations
Page 1 of 5
Linearity
Ramsey Hill Exploration, LLC
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT
Sand Dryer #3
Test Date: 5/29/2024
O2 NOX
20.4 20.2
10.20 10.1
0.0 0.0
10.2 10.1
Linearity Bias (Zero) 0.0 0.0
Linearity Bias (Span) 10.2 10.1
% (ppm)
0.00 0.0
10.20 10.1
20.40 20.2
0.0 0.0
10.2 10.1
20.4 20.2
0.0 0.0
0.0 0.0
0.0 0.0
0.0 0.0
0.20% 0.20%
0.15% 0.05%
0.10% 0.05%
Gas Concentration
1
2
3
Linearity Information
Gas
Span Gas Value/Range
Bias Gas Value
4
Difference
1
4
Response
1
2
Span Bias
Max Calibration Error
Bias Check (Zero)
Bias Check (Span)
2
3
4
Results
3
Zero Bias
Page 2 of 5
Run 1
Ramsey Hill Exploration, LLC Run 1
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT Start Time 8:25
Sand Dryer #3 Run Length 120
Test Date: 5/29/2024 Stop Time 10:30
O2 CO2 NOX
20.4 0.0 20
10.20 0.00 10.1
0.0 0.0 0.0
10.2 0.0 10.1
0.0 0.1
10.2 10.1
0.1% #DIV/0! 0.5%
0.2% #DIV/0! 0.2%
0.0% #DIV/0! 0.3%
0.0% #DIV/0! 0.1%
Corrected O2 % Corrected CO2 % Corrected NOX ppm
17.0 #N/A 16.4
Run Length
(Minutes) Time Uncorrected O2 % Uncorrected CO2 % Uncorrected NOX ppm
17.0 #N/A 16.4
Zero%
Span%
Absolute Bias (Zero)
Absolute Bias (Span)
Absolute Drift (Zero)
Absolute Drift (Span)
Results
Post Test Calibration
Calibration Information
Instrument Range
Span Gas Value
Gas
Calibration
Pretest Calibration
Zero%
Span%
Page 3 of 5
Run 2
Ramsey Hill Exploration, LLC Run 2
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT Start Time 10:52
Sand Dryer #3 Run Length 120
Test Date: 5/29/2024 Stop Time 12:58
O2 CO2 NOX
20.4 0.0 20
10.20 0.00 10.1
0.0 0.0 0.1
10.2 0.0 10.1
0.0 0.1
10.1 10.1
0.0% #DIV/0! 0.5%
0.2% #DIV/0! 0.1%
0.1% #DIV/0! 0.0%
0.4% #DIV/0! 0.3%
Corrected O2 % Corrected CO2 % Corrected NOX ppm
17.0 #N/A 17.2
Run Length
(Minutes) Time Uncorrected O2 % Uncorrected CO2 % Uncorrected NOX ppm
17.0 #N/A 17.1
Gas
Instrument Range
Post Test Calibration
Zero%
Span Gas Value
Calibration
Pretest Calibration
Zero%
Calibration Information
Results
Absolute Bias (Zero)
Absolute Bias (Span)
Absolute Drift (Zero)
Absolute Drift (Span)
Span%
Span%
Page 4 of 5
Run 3
Ramsey Hill Exploration, LLC Run 3
RHEx Vernal Sand Mine (Site ID: 15971)
Uintah County, UT Start Time 13:13
Sand Dryer #3 Run Length 120
Test Date: 5/29/2024 Stop Time 15:18
O2 CO2 NOX
20.4 0.0 20
10.20 0.00 10.1
0.0 0.0 0.1
10.1 0.0 10.1
0.0 0.1
10.2 10.1
0.1% #DIV/0! 0.5%
0.2% #DIV/0! 0.1%
0.0% #DIV/0! 0.0%
0.4% #DIV/0! 0.2%
Corrected O2 % Corrected CO2 % Corrected NOX ppm
17.1 #N/A 17.0
Run Length
(Minutes) Time Uncorrected O2 % Uncorrected CO2 % Uncorrected NOX ppm
17.1 #N/A 16.9
Post Test Calibration
Instrument Range
Zero%
Results
Absolute Bias (Zero)
Span%
Span%
Zero%
Absolute Bias (Span)
Absolute Drift (Zero)
Absolute Drift (Span)
Calibration Information
Span Gas Value
Calibration
Pretest Calibration
Gas
Page 5 of 5

AIR REGULATIONS CONSULTING, LLC•5455 RED ROCK LN, STE 13, LINCOLN, NE 68516•402.817.7887•AIRREGCONSULTING.COM

July 23, 2024

Attn: Mr. Chad Gilgen
Minor Source Compliance, Division of Air Quality
P.O. Box 144820
Salt Lake City, UT 84114-4820

[Submitted via https://utahgov.co1.qualtrics.com/jfe/form/SV_3dSxf7JSzy4jwGh & email to [e-mail].]

RE: Dryer #3 & Crusher #2 Stack Test Report, Filterable PM, Opacity, & NOx
Ramsey Hill Exploration, LLC – RHEx Vernal Mine
DAQE-AN159710004-23

Mr. Gilgen,

On behalf of Ramsey Hill Exploration, LLC (RHEx), Air Regulations Consulting, LLC (ARC) is providing
this copy of the Compliance Source Emissions Test Report to the Utah Department of Environmental
Quality, Division of Air Quality (DAQ), as required by Utah Administrative Code R307-165-3 and
Section II.B.4.f.3 of RHEx’s Approval Order, DAQE-AN159710004-23, which allowed RHEx to add a
third sand dryer (Dryer #3) and a second crusher (Crusher #2) at the Vernal Mine. The test was
conducted on May 29, 2024, and sampled filterable particulate matter (PM), opacity, and oxides of
nitrogen (NOx). The results demonstrate compliance with 40 CFR 60 Subpart UUU, 40 CFR 60 Subpart
OOO, UAC R307-165-2, and II.B.4.f of RHEx’s Approval Order. This report fulfills the requirements in
UAC R307-165-3 and Section II.B.4.g.3 of Approval Order DAQE-AN159710004-23 in being submitted
to the DAQ within 60 days of testing.

The testing report was prepared by Western Environmental Services and Testing, Inc and is attached
for review. If you have any questions regarding the enclosed information, please do not hesitate to
call me, Eric Sturm, with ARC at 402.817.7887, or email at [e-mail].

Sincerely,

Eric Sturm
ARC Owner, Lead Consultant

Enclosures

Cc: Mike Cina, RHEx
Sand Dryer #3
Roll Mill Crusher #2 Inlet
Roll Mill Crusher #2 Outlet
Ramsey Hill Exploration, LLC
Vernal, Utah
Table 3
Results Summary
Filterable 0.00235 gr/dscf 0.01 gr/dscf
Particulate 0.262 lb/hr 0.61 lb/hr
NOx
Opacity
Opacity
Opacity
77.88 ppm@3% 02
1.56 lb/hr
0.14%
0%
0%
96ppm@3%O2
4.35 lb/hr
10%
10%
10%
4
Western Environmental Services and Testing, Inc. 24-1043
Ramsey Hill Exploration, LLC
Vernal, Utah
Table 4
Sand Dryer #3
Particulate Emissions Results
Run Number: 1 g ~ Average
Start Date/Time 5/29/2024 8:25 5/29/2024 10 :52 5/29/202413:13
Stop Date/Time 5/29/2024 10 :30 5/29/2024 12:58 5/29/2024 15:18
Test Parameters Units
Pbar (Barometric Pressure, absolute) In. Hg 24.22 24.22 24.22 24.22
Y (Dry Gas Meter Calibration Factor) dimensionless 0.978 0.978 0.978 0.978
Cp (Pilot tube Coefficient) dimensionless 0.837 0.842 0.837 0.839
Dn (DiameterofNozzle) Inches 0.279 0.278 0.279 0.279 e (Total Sampling Time ofTest) minutes 120.00 120.00 120.00 120.00
,1H (Orifice Pressure Drop) in. H20 1.35 1.35 1.31 1.34
V m (Volume of Dry Gas Sampled -as measured) ft3 (dry) 89.107 90.090 89.250 89.482
Tm (Gas Meter Temperature, avg.) •F 74 79 82 78
V10 (Condensate -Impinge rs and silica gel) mlorg 289.8 277.9 277.8 281.83
Location/Process Parameters
As (Cross-sectional Area of Stack) ln2 1,328.32 1,328.32 1,328.32 1,328.32
P9 (Static Pressure of Stack Gas) 0.54 0.54 0.54 0.54
Ts (Temperature of Stack Gas) •F 187 190 187 188
✓ ,1p (Sq. root of velocity head of gas) ✓in. H20 0.6002 0.5965 0.5922 0.5963
CO2 (Carbon Dioxide) % 2.60 2.70 2.69 2.66
02 (Oxygen) % 16.99 17.04 17.09 17.04
N2 (Nitrogen) % 80.41 80.26 80.22 80.30
Calculations
V n-std (Gas Sampled, standard conditions (std)) ft3 70.093 70.190 69.170 69.818
Vwstd (Water Vapor In Gas Sampled, std) ft3 13.641 13.081 13.076 13.266
Bws (Water Vapor In Gas, Proportion by Vol.) ,
% 16.29 15.71 15.90 15.97
Gd (Proportion of Dry Gas in stack) % 83.71 84.29 84.10 84.03
EA (Excess Air) % 401 411 418 410
Md (Molecular Weight ofD ry Stack Gas) lb/lb-mole 29.10 29.11 29.11 29.11
Ms (Molecular Weight of Wet Stack Gas) lb/lb-mole 27.29 27.37 27.35 27.33
P, (Pressure of Stack Gas, Absolute) In. Hg 24.26 24.26 24.26 24.26
lso (Percent of lsokinetlc Sampling) % 97.5 98.1 97.2 97.6
Flow Results
v. (Average Stack Gas Velocity) ft/m(fpm) 2,547 2,549 2,511 2,536
Ostd (Dry Volumetric Flow Rate, std.) ft3/m (dscfm) 13,015 13,047 12,881 12,981
Q. (Measured Volumetric Flow Rate, Actual) ft3/m (cfm) 23,492 23,514 23,167 23,391
Particulate Results
Mass of Particulate collected, FIiter mg 2.60 6.90 5.00 4.83
Mass of Particulate collected, Probe -Acetone rinse mg 7.50 6.70 3.30 5.83
Total Mass of Particulate collected mg 10.10 13.60 8.30 10.67
Particulate Concentrations
Particulate Concentrations, Filter gr/dscf 0.000572 0.00152 0.00112 0.00107
Particulate Concentrations, Probe -Acetone rinse gr/dscf 0.00165 0.00147 0.000736 0.00129
Particulate Concentrations, FIiterabie Total gr/dscf 0.00222 0.00299 0.00185 0.00235
Particulate Emission Rates
Particulate Emission Rate, FIiter lb/hr 0.0639 0.170 0.123 0.119
Particulate Emission Rate, Probe -Acetone rinse lb/hr 0.184 0.165 0.0813 0.143
Particulate Emission Rate, FIiterabie Total lb/hr 0.248 0.334 0.204 0.262
Standard Conditions= 68° F, 29.92" Hg
5
Western Environmental Services and Testing, Inc. 24-1043
Ramsey Hill Exploration, LLC
Vernal, Utah
02 (Oxygen)
Flow Results
v. (Average Stack Gas Velocity)
Q,1d (Dry Volumetric Flow Rate, std.)
Q, (Measured Volumetric Flow Rate, Actual)
N0x Emissions
NO, Concentration-dry
NO, Concentration-dry
NO, Emission Rate
Table 5
Sand Dryer #3
NOx Emissions Results
Run Number: 1
Start Date/Time 5/29/2024 8:25
Stop Date/Time 5/29/2024 10:30
% 16.99
ft/m (fpm) 2,547
ft3/m (dscfm) 13,015
ft3/m (cfm) 23,492
ppm 16.37
ppm@3%O2 74.94
lb/hr 1.53
5. SAMPLING AND ANALYTICAL PROCEDURES
g i Average
5/29/2024 10:52 5/29/2024 13:13
5/29/2024 12:58 5/29/2024 15:18
17.04 17.09 17.04
2,549 2,511 2,536
13,047 12,881 12,981
23,514 23,167 23,391
17.09 16.91 16.79
79.25 79.45 77.88
1.60 1.56 1.56
The point source characterizations include the above listed source and the associated test
parameters. A summary of the source test methods follows. Because standard EPA
methodology was followed, only a brief description of each method is provided. Detailed US
Environmental Protection Agency (EPA) Methods are available in Title 40 of the CFR (40CFR).
Part 60, Appendix A
Method 1 "Sample and Velocity Traverses for Stationary Sources"
Method 2 "Determination of Stack Gas Velocity and Volumetric Flow Rate"
Method 3A "Determination of Oxygen and Carbon Dioxide Concentration in Emissions
Method 4
Method 5
Method 7E
Method 9
from Stationary Sources"
"Determination of Moisture Content in Stack Gas"
"Determination of Particulate Matter Emissions from Stationary Sources"
"Determination of Nitrogen Oxides Emissions from Stationary Sources"
"Visual Determination of the Opacity of Emissions from Stationary Sources"
Sampling Point Determination (EPA Method 1)
The location of velocity sampling points was determined in accordance with the procedures
outlined in EPA Method 1. Stack sampling points are based on the stack diameter or equivalent
diameter and the distance from the sampling ports to flow disturbances. Stack dimensions and
traverse point locations for each source are presented in Appendix A.
Velocity and Flow Rate Determination (EPA Method 2)
Stack gas velocity and volumetric flow rates were determined in accordance with the procedures
outlined in EPA Method 2. Velocity and temperature were measured at the points determined by
6
Western Environmental Services and Testing, Inc. 24-1043
Ramsey Hill Exploration, LLC
Vernal, Utah
Method 1 during the testing. Wind tunnel calibrated pitot tubes were used to measure velocity
head. Type K thermocouples with digital pyrometers were used to measure temperature.
Carbon Dioxide, Oxygen, and Dry Molecular Weight Determination (EPA Method 3)
Oxygen (02) concentrations, carbon dioxide (CO2) concentrations and dry molecular weight
were determined in accordance with the procedures outlined in BP A Method 3. An integrated
sample from each traverse point was collected in Tedlar bags from the dry gas leaving the dry
gas meter during each BP A Method 4 test. Analysis of CO2 and 02 were performed with a
Burrell Corporation Orsat Gas Analyzer. Dry molecular weight was calculated from CO2, 02,
and N2 (by difference) concentrations.
Moisture Content Determination (Method 4)
Flue gas moisture content was determined in accordance with the procedures outlined in BP A
Method 4. Water entrained in the stack gas was condensed in chilled impingers in conjunction
with the isokinetic sampling. The volume of gas sampled was measured with a dry gas meter.
Moisture content was calculated from the measured gas and condensed liquid volumes.
Particulate Emissions Determination (EPA Method 5)
Particulate emissions were determined in accordance with the procedures outlined in BP A
Method 5. Sampling nozzles were constructed of stainless steel. All other sampling train
components (probe liner, filter holders, impingers, etc.) were constructed of borosilicate glass.
All glassware was thoroughly decontaminated prior to testing in accordance with Method 5
requirements. The impingers used in the train are as follows:
* Impinger 1: Modified Greenburg-Smith impinger containing 100 ml of DI H2O
* Impinger 2: Greenburg-Smith impinger containing 100 ml of DI H2O
* Impinger 3: Modified Greenburg-Smith impinger, dry
* Impinger 4: Modified Greenburg-Smith impinger containing silica gel
Samples were collected isokinetically for a minimum of 120 minutes with a minimum sample
volume of 1.70 dry standard cubic meters (60 dry standard cubic feet). The sampling runs were
performed to meet the conditions specified in EPA Method 5. A schematic of the Method 5
sampling train is shown in Figure 1.
W estem Environmental Services and Testing, Inc. 24-1043
7
Ramsey Hill Exploration, LLC
Vernal, Utah
Nozzle t..,
' Types
pitot Tube
.....
/f
Manometer
Temperature
Sensor
' Heated )t. Probe
~ !
Manometer
/f
Temperature
Sensor
JI '
Figure 1
D.I.
Vacuum
Gauge ♦
ce ath
t . vacuum Line
Method 5 Particulate Sampling Train Schematic
Upon successful completion of a test run, all exposed front-half sampling surfaces; nozzle,
probe, connecting glassware, and front half of the filter holder were rinsed and brushed a
minimum of three times with acetone for particulate recovery and collected in polypropylene
sample containers. The front half filter was carefully recovered and transferred to a container for
transport. The front half samples were analyzed gravimetrically for particulate matter.
After the mass of the impingers were recorded for moisture content determination, any liquid
collected in the impingers were discarded. Blanks of all reagents used were also collected and
analyzed with the samples.
Gaseous Emissions (Methods 3A and 7E)
Oxygen (02), carbon dioxide (CO2), and nitrogen oxides (NOx) were measured in accordance
with the procedures outlined in EPA Methods 3A and 7E, respectively, using extractive
continuous emission monitors (CEMS). This package is comprised of four basic subsystems:
• sample acquisition and conditioning system
• calibration gas system
8
Western Environmental Services and Testing, Inc. 24-1043
Ramsey Hill Exploration, LLC
Vernal, Utah
• analyzers
• data acquisition system
The sample acquisition and conditioning system contains components to extract a sample of gas
from the stack, transport the sample to the analyzers, and remove particulate from the sample. A
sample is extracted continuously from the stack through a heated probe and heated sample line.
The gas passes through a moisture removal system before being delivered to the 02, CO, and
NOx analyzers. 02, CO2, and NOx were measured on a dry basis.
The calibration system includes protocol gases, a gas dilution system, and a method for
introducing the desired gas concentrations into the sample acquisition system as close to the
probe as possible. The gas dilution system is calibrated annually by the manufacturer. A zero
gas, a mid-range gas concentration, and a high range gas concentrations were used to calibrate
and check the linearity of each analyzer. The zero and mid-range gas concentrations were also
used to check each analyzer before and after each run for bias and drift. The analyzers used,
along with a brief description of their principles of operation, are listed in Table 6.
I< S2ecies··· I
Oxygen
Carbon Dioxide
Nitrogen Oxides
Table 6
CEMS Analyzers
Test Method ·• ... Atialytei-.
3A CAIZRE
3A CAIZRE
7E API 200AH
.. , I· Princi2Ie QfO2eratiop. I
Fuel Cell
NDIR
Chemiluminescent
The data acquisition system operates on a computer platform. Instrument outputs follow a 16-bit
ADC and are polled once every second and compiled as minute averages. All CEMS and the
data acquisition system are rack mounted in a temperature controlled mobile laboratory. A
schematic of the CEMS sampling equipment is shown in Figure 2.
9
Western Environmental Services and Testing, Inc. 24-1043
Probe
!
+ Data Acquizition Cable
+ Heated Teflon Sample Line
Pressure + Regulators
Teflon Bias Line
Dilution
Control Cable
l
Figure 2
CEMS Sampling System Schematic
Visual Determination of the Opacity of Emissions -EPA Method 9
Ramsey Hill Exploration, LLC
Vernal, Utah
Sixty-minute opacity observations were performed in accordance with the procedures outlined in
EPA Method 9. Opacity observations were performed by a certified observer. Opacity
observations was made at the point of greatest opacity and will be recorded to the nearest 5
percent at 15-second intervals on an observational record sheet. The observer stood at a distance
sufficient to provide a clear view of the emissions with the sun oriented in the 140° sector to his
back.
The observer recorded the name of the plant, emission location, type of facility, observer's name,
and affiliation, a sketch of the observer's position in relation to the source, and the date on a field
data sheet. The time, estimated distance to the emission location, approximate wind direction,
estimated wind speed, description of the sky conditions (presence and color of clouds), and
plume background was recorded on the data sheet at the time opacity readings are initiated and
completed. The opacity was determined as an average of the observations recorded at 15-second
intervals during each run.
10
Western Environmental Services and Testing, Inc. 24-1043
Ramsey Hill Exploration, LLC
Vernal, Utah
6.0 SOURCE EMISSION CALCULATIONS
The values in the sample calculations shown below are from Run 1. Computer generated
numbers were used to eliminate rounding error.
1. Volume of water collected, standard conditions
(wscf):
V w(std) = K(V1c)
= 0.04707(289.8)
= 13.641 Vwstd
2. Volume of gas metered, standard conditions ( dscf)
till (K)(Vm)(Pbar + 13 6 )(Y)
Vm(std) = •
(460 + Tm)
0.54 (17.647)(89.107)(24.22 + 11:o )(0.978)
(460 + 74)
= 70.093 dscf
3. Moisture content, %
Vw(std) Bws = xl00%
Vm(std) + V w(std)
13 .641 ------x100% 70.093+13.641
= 16.29%
4. Dry Gas,%
Gd= 100-Bws
= 100-(16.29)
= 83.71%
Western Environmental Services and Testing, Inc.
Vw(std) = Volume (ft3) of water collected at standard
conditions
Vic = Volume of liquid collected in impingers
K = 0.04707 = Conversion factor (ft3/ml)
Vm (std) = Volume (ft3) of gas through the dry gas meter, at
standard conditions
Vm = Volume (ft3) of gas sample through the dry gas meter,
ambient conditions
Pbar = Barometric pressure (inches of Hg)
,1H = Average pressure drop across meter orifice (in.H2O)
Y = Dry gas meter conversion factor
Tm= Average dry gas meter temperature (°F)
K = 17.647 = Conversion factor (0R/inch Hg)
13. 6 = Conversion factor (inch H2Olinch Hg)
460 = Conversion constant (°F to 0R)
Bws = Percent by volume of water vapor in the gas stream
Vw(std) = Volume (ft3) of water collected, at standard
conditions
V,n(std) = Volume (ft3) of gas through the dry gas meter, at
standard conditions
Gd = Percent of dry gas by volume in the gas stream
Bws = Percent by volume of water vapor in the gas stream
24-1043
11
5. Molecular weight of dry gas stream (lb/lb•mole)
Ramsey Hill Exploration, LLC
Vernal, Utah
Md= Meo, (%COz) + Mo, (%Oz)+ (Mcoo,MN,) (%CO+ %Nz)
(100) (100) (100)
Md = Dry molecular weight of sample gas (lb/lb mole)
Mc02 = Molecular weight of carbon dioxide (lb/lb mole)
M02 = Molecular weight of oxygen (lb/lb mole) = 44,0 (2,60) + 32.0 (16.99) + 28.0 (80.41)
(100) (100) (100)
= 29. 10 lb/lb mole
6. Molecular weight of sample gas (lb/lb•mole)
Ms= (Md)(Gctll00)+(MH2o)(BwsllO0)
= (29.10)(83,71/100)+(18)(16.29/100)
= 27 .29 lb/lb mole
7. Sample gas pressure (inches of Hg)
P, = (Pbar)+ (Pg)
(13.6)
( 0,54)
= ( 24.22) + ( ) 13.6
= 24.26 in. Hg
8. Velocity of sample gas (ft/min)
v, +p) ( °") ( 60 )( !AP) ( i~; ;::n
= ( 85.49 )( 0.837) ( 60 )( 0,6002)
=2,547:fpm
187 +460
27.29x24.26
Western Environmental Services and Testing, Inc.
Meo orN2 = Molecular weight of CO or N2 (lb/lb mole)
(Same)
Ms02 = Molecular weight of sulfur dioxide (lb/lb mole)
CO2 = Percent by volume of CO2 in the gas stream
02 = Percent by volume of oxygen in the gas stream
CO+N2 = Percent by volume of CO and N2 in the gas
stream
SO2 = Percent by volume of sulfur dioxide in the gas stream
100 = Conversion from percent to decimal fraction
M, = Molecular weight of sample gas, wet (lb/lb mole)
Md = Dry molecular weight of sample gas (lb/lb mole)
Gd = Percent of dry gas by volume in the gas stream
Bw, = Percent by volume of water vapor in the gas stream
MH20 = Molecular weight of water (lb/lb mole)
P, = Absolute sample gas pressure (inches of Hg)
Pbar = Barometric pressure (inches of Hg)
Pg = Sample gas static pressure (inches of H20)
13. 6 = Conversion factor (inches H2Olinches of Hg)
Cp = Pitot tube constant
Kp = Velocity pressure coefficient (dimensionless)
60 = Conversion factor (sec/min)
M, = Molecular weight of sample gas, wet (lb/lb•mole)
P, = Absolute sample gas pressure (inches of Hg)
T, = Average sample gas temperature (°F)
V, = Sample gas velocity (ft/min)
,J7;p = Average square roots of velocity heads of stack gas (in
I-hO)
460 = Conversion constant (°F to 0R)
12
24-1043
9. Total flow of sample gas, actual conditions (acfm)
Qa = (As/144)(Vs)
= (l,328.32/144)(2,547)
= 23,492 cfm
10. Total flow of sample gas, standard conditions
(dscfm)
(Qa)(P,)(17.641{ l~~)
Q,td = ---------(T,+460)
(23,492)(24.26)(17.647)( 83•71 )
100
(187+460)
= 13,015 dscfm
11. Concentration of Particulate
C,= (K)(mn)
Vm(std)
(15.43)(0,01010)
70.093
= 0.00222 gr I dscf
12. Particulate emissions (lb/hr), Total
(Cs)(Qstd)(60)
Elb/hr = ------
=
7,000
(0.00222)(13,015)(60)
7,000
= 0.248 lb/hr
Western Environmental Services and Testing, Inc.
Ramsey Hill Exploration, LLC
Vernal, Utah
Qa = Volumetric flow rate at actual conditions (acfm)
As = Cross sectional area of sampling location (in2)
144 = Conversion Factor, inches to feet
Vs = Sample gas velocity (ft/min)
Qs1d = Volumetric flow rate at standard conditions, dry
basis (dscfm)
Qa = Volumetric flow rate at actual conditions (acfm)
Ps = Absolute sample gas pressure (inches of Hg)
Gd = Percent of dry gas by volume in the gas stream
Ts= Average sample gas temperature (°F)
17.647 = Conversion factor (0R/inch Hg)
460 = Conversion constant (°F to 0R)
Cs = Total concentration of particulate in stack gas, grldscf
mn = Total mass of particulate collected, grams
Vin(stdJ = Volume (ft3) of gas through the dry gas meter at
standard conditions
K = 15. 43 = conversion factor (grains/gram)
Etb!ltr = Emission rate (lb/hr)
Cs = Measured concentration in the gas stream (gr/dscf)
Qstd = Volumetric flow rate at standard conditions, dry
basis ( dscfm)
60 = Conversion factor (min/hr)
7,000 = Conversion factor (gr/lb)
24-1043
13
13. Continuous emissions monitoring for Nitrogen
Oxides (ppmdv)
Cgas =(C-Co) (Cma)
(Cm-Co)
=16.33-[0.03+(-0.04)J[ 25.00
2 (25.00;24.89) [ 0.03+~-0.04) J
=16.37 ppm
14. Emissions Nitrogen Oxides (lb/hr)
Elb/hr (Cgas)(MNOx)(Qstd)(60)
(385.3)(106)
(16.37)( 46.0I)(13,015)(60)
(385.3)(106)
=1.53 lb/hr
Western Environmental Services and Testing, Inc.
Ramsey Hill Exploration, LLC
Vernal, Utah
Cgas = Effluent gas concentration indicated by analyzer, dry
basis, (ppmdv)
C = Average gas concentration indicated by analyzer in
the gas stream, dry basis (ppmdv)
Co = Average of initial and final system calibration bias
check response for the zero gas (ppm)
Cm = Average of initial and final system calibration bias
check response for the upscale calibration gas (ppm)
Cma= Actual concentration of the upscale cal. gas (ppm)
E1blhr = Emission rate (lb/hr)
Cgas = Effluent gas concentration, drift corrected, dry basis,
(ppmdv)
MNox = Molecular weight of nitrogen oxides (lb/lb•mole)
Qstd = Volumetric flow rate at standard conditions, dry
basis (dscfm)
60 = Conversion factor (min/hr)
385.3 = Conversion factor (ft3/lb mole)
106 = Conversion/actor (ppm)
24-1043
14
APPENDICES
A. Sampling Locations
B. Field Testing Data
C. Computer Data Entry
D. Analytical Data
E. Chain of Custody
F. Calibration of Equipment
G. Resumes of Test Personnel
H. Process Data
APPENDIX A
Sampling Locations
Stack Dimensions
Sand Dryer#3
Stack Diameter, inches 41 1/s
Port and Wall, inches 2 3/4
Downstream Diameters 5.8 from Flow Disturbance (240 inches) to Ports
Upstream Diameters
0.7 from Flow Disturbance
to Ports (27 inches)
Traverse Points
Sand Dryer #3
Inside Stack Diameter= 41 1/8 inches
Port and Wall Thickness = 2 ¾ inches
Sample %of Inches from
Point No. Diameter Wall
1 2.1 1*
2 6.7 2¾
3 11.8 4 7/s
4 17.7 7 1/4
5 25.0 10 1/4
6 35.6 14 5/s
7 64.4 26 1/i
8 75.0 30 7/s
9 82.3 33 7/s
10 88.2 36 1/4
11 93.3 383/s
12 97.9 40 1/s*
* Adjusted to 1 inch from stack wall
APPENDIXB
Field Testing Data
Cyclonic Flow Determination
Client: /ll:\E~
Location: V O>r_S,,,\
Operator: /~
Western Environmental Services and Testing, Inc.
Preliminary Velocity Data
Inches Downstream from flow distubance to ports: fJl/0 It
117 f/ Inches Upstream from flow disturbance to ports:_~"'---
Ds:,--"-5_. 1~-
Ds:_~o~.1_,___
Date: 5' -:z.i ,. 2 4
Job No.: o2L\ -\OL\:')-Source Identification _~;;.;w.C::~'\~\Q..~,---~------------
Port B Port C Port D Average Port A
Port & Inside Dia.: L\~+/'6' Ll 3,%
Port & Inside Wall Thick : ;2 3/~ :) \
Inside Stack Dia. L\\ ')f'
I
: '-/I~ \7~
PORT A PORT B
TIME:
Point Dist.from Ref. Dist. lrom Ref.
No. % Dia. point, 0.01" Point, 1/16" 6P / Temp I Cycl. 6P / Temp I Cycl.
2
3
4
5
6
7
8
9
10
11
12
Average: I I I ,
Pitot No. % Moisture Velocity (fpm) ,,
Cp Gd· ' Time of Test
Box# CO2 Assumed SCFM
Pb 02 Assumed Vmstd
Ps co Dn
Avg. t1P N2 SCFM(sample)
Avg. ✓tlP MWd llH
Avq.Ts MW K Factor
Ava.Cyclonic 'I" Vmstd
Area of Stack: lsokinetic
ACFM ______ _ SCFM _____ _
SEE BACK FOR DRAWING AND FURTHER INFORMATION
*Standard, 528 R, 29.92 "Hg, (20 C., 760 mm Hg)
POAT C
6P / Temp I Cycl.
I I
I I
I
I
I
I
I I
I I
I I
I
I I
I
I
PORTO
6P / Temp I Cycl.
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
I
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roe .C,
6<;~.o
S1-IS
911,3
Particulate Run Sheets
Western Environmental Services and Testing, Inc.
Facility 111-tE)C \/errul Job No:24-/0~ Schematic of Stack Cross Section K Factor -J 3 .5
Run No. l Date: 5/2q /202-4
Source/ I.D.No. Dv;~« #-3
Stack:Areain2 {A5)1!2 .3Z Dia{in) '-1 1 '1?
·operators p. Robi.s:on
Meter Box# I 2. Calib. Factor(Y) o.q 7'8 g
\...l '2-Delta H @ I. 7 I 3
Nozzle #_•Af~~~_Diameter (On)~-,c,0.271 IJ ~ or Up
Pitot 1.0. A q Calib.Factor(Cp) O· 8'1 I
-----'-Yn.,__,__5.__ ___ Field Data
Clock Dry Gas ~p (Pitot) ~H (Orifice) "H2O
Point Time Meter (W) "H2O Desired Actual
A-12. 0&2.S I SO.&/70 0-~8 1.3~ 1.30
l J 03~ 15l-f. 04 0. lf(} 1.LtO 1.lfo
JO Gg~5 }S17-=f-O.l-/~ ~,., ~~ Jt.
oq o'640 IC: 1.7'1 o. LfS 1.~8 l-7O
08 0 ic.,~ IC.5.~?-o.4~ t. jo 1. 80
CY+ og50 110.J Z o,SO 1.ir i.qo
OCo 0~55 )74.L.fq o.~S? l.'12 I. 40
05 oGJoo I 7f. 'l l 0-~7? i.42-J.4O
OY nCio5 l f<Z. 2.f> 0:2~1 uro I. 2(J
G3 oq,o I ~ S. -x 6 0. z..i '-O~ 1.0
02. oq IS I S? q.1 2 n.zs o.C13 o.qC)
of 692.0 Jqz.2.q 0-ZG 0.75 0.15
furl oqz5 I q 5. D 12.
1312 GC\~ I q,s /7/ o.a,o 1. 12.. 1.10
1 l oq;c; Jq'Z. t:;q 0 .~() I. 12. I. JO
10 0(\40 1.n I. 'i< :> 0. ?i-1 1.~1 J.&)
()q oq45 2..05.l/S G.~i I .'12. 1.40
Pump
Vac. "Hg
7-. 0
'1.0
4.0
s.o
'5,C)
1::).0
6.0
5.0
4.0
4,0
LJ_o
t./.0
Y.o
Y.0
4.o
4.0
Uncorrected V mFC/, / 0 7 ft3
Corrected V rn f ? , / L/ 7 ft3
%CO2 2. <Ad %CO -G--
l b// 9 %O2 J +-6.l %N,:::8'o,~b,
g>o,¾11
Barometric Pressure (Pb) 24. 2 2. ' Pe
Amb. °F 7 2 Assumed Moisture % -J-9-!-20
Static Stack Pressure ;,H20 Gt-) a.SL/
Probe Length / Material '-/ I ~J(i!SS u Before Middle After
Pitot Tube Leak Check _L_ ✓ --
Gas Flow Out / In Initial Leak @ J(J • OCJO "Hg= 0-000 ft3/min
Final Leak @ 1 o. 0 o 6 "Hg =o,Qoo> ft3/min
Temperature °F %
Probe T5 (stack) Tmln Tm Out Filter Exit Cold Filter lsokinetic
Zl/6 180 12. ----7-S'-I (ht./ -
243 l 8,.-72---2.$5' £5 '-1 --
l.l/6 IRR 7Z -i.4R sz -K~ ~-7~
7152.. I ??Cf 72 · -z,sz. <53 -
1'57 19Q 7'2. -'zt1Cf 54 -
ZC3lf Jqo 7'2. -ZS'j 5G -
252. l Cf I 12... -253 sg -
2,'-1q l{,f J 73 --. 2.03 07---'
?,$} I q J 7g -2.ljf ,s <f -
2.l/6 I GJO 7~ -2'-15 0tf -
2..5ii igg 73 -2.0.1 53 -
·1.}Jq 15?0 7~ -z4q vj z_ -
2.54 18 J 74 ---iWh 68 -
2'5Z. ,22 7'1 -20"0 "5} --
7.,54 182 74 -2.SO 50 -
Z'BO 1~1 74 -z4q ~, -
Sample Purge: Initial .-Final ___ ..,,._
Volume Collected V,c~f 1. f ml Sample Time, e I zo min.
Western Environmental Services and Testing, lnc.
Job No: Z lJ ..... /043 ---'-VY)""---'--5 ___ Field Data Page~of '2...
Run No.~_ Date: $ / 2Cf I 2CJZ4 Facility ~J.1-E.t \/etntA:l Source/ I.D. No. l)r~ e,r-¾3
Clock Dry Gas .6.P (Pitot) .6.H (Orifice) "H20 Pump Temperature °F %
Point Time Meter (ft'') "H20 Desired Actual Vac. "Hg Probe T 8 (stack) Tmln Tm Out Filter Exit Cold Filter lsokinetic
O'R ~60 2.0ll. '2.~ o.4o 1.-SO LSD 6.0 2.'GZ. 181 7CJ -250 '52. -
01 oqss '2-13. lS o.4c, t.Gi 1.76 0~0 Jt62.. lf6 74 -2'-1-1-62--
O(o /000 ?_ 17-:g.) 0-l-f~ 1.80 I. &'O 6,0 2'-Jq l&'r 75 -2'-IG 58 -
GS 1005 22.1-60 o.4~ 1.61 J.60 ?-0 il/G 18G 75 ..a.. 21./6 54 -
DY 1010 '2.-2~11 o.i1 l.L-/2 1.40 '5.o 2.l-J~ ISG 7S -'2.5 2. '55 -
0~ 1015 1..-z.<t~O 0. ?)15' 1.i1 I. 30 '5.0 1'fJO I }ZS 70 -• 2.? I S6 -
02 l'O 2.0 -z.,;~.; .g 0.28 l.O<o'" t.o 6.o zss 18 2.. 70 -2~2. 56 -
01 102.s 2-gc; G'S" o.2~ o,gG o.qo 6.0 2,4q 17$" 7G -1-5) 58 -
fu1 1050 Z.3 c1_ "7 '-( 2.
;
l1ti!.i ~1&
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~J
Western Environmental Services and Testing, Inc
Job Number: r2L\ -\ 6':::\~
Field Data: (Y)S:
Source ID: ~~ec ~'3>
lmpinger # 1
ContentsNol. \ Cc)M \
Tip Style
Final Wt.
Initial Wt.
Difference
lmpinger# 5
ContentsNol.
Tip Style
Final Wt.
Initial Wt.
Difference
(rota!, grams 1-~g,y_g \
2
6
. 3
7
Run#: ___ ~:;;z..~-'~---
Filter #: __ ___.x~,c._-_1:...._,_$"i,_.,.l...,,o'------
Balance Check (500 g):
4 tiH=
IIP=
sq. root i'.P
T = m
T.=
Vms1d=
VWgas=
% Moisture=
8 Gd=
Mwd=
Mw=
Vs (ft/min)=
ACFM=
SCFM=
¾E.A.=
Silica Gel {%Spent): ¾lsokinelic=
Date: Time: Analyst Initials: _____ _ ------
(Check one) Grab Sample: __
Integrated Single Point: __
Integrated Muti Point: __
Replicate Original Aliquot CO2 Volume
Measurement (mis) (i) (mis) (2)
1 100
2 100
3 100
Mean 100
Mwd= 0.44*(%CO2)+0.32*(%O2)+0.28*(%CO+¾N2)
COMMENTS:
------
Initial Leak Check:
Final Leak Check:
Leak check must not change level by more than 0.2 mis in 4 minutes
ORSAT Analysis
0 2 Reading 0 2 Volume N2/CO by Difference Dry Molecular
(mis) (3) (mis) (4)=(3-2) (mis) (S)=(i-3) WeighlMwd
(Mwd must agree within +/-0.3 gig-mole from their mean for any 3 analyses)
Western Environmental Services and Testing, Inc.
Facility KB Ex Vevn-od Job No: 2,4 -10'13 Schematic of Stack Cross Section K Factor ·3. 7 :5
Run No. 2. Date: srzq IZ02/·-I
Source/ LO.No. Dr.g-w :1:l:-3
Stack: Area in2 (As) l ,?28.32 Dia (in) 41 '18
·operators P. fiob,so11
Meter Box # I 2 Calib. Factor(Y) o. Cl 7 '8
..:,/:e-V-.2. Delta H@ l-715
Nozzle# ·:g..J.4-~ Diameter (On) <'-~1~~n~ J ~ or Up
Pitot I.D. ~Lgj'f Calib.Factor(Cp)'__::§t:~~~o.9'1i,
rns Field Data
Clock Dry Gas L'i.P (Pitot) L'i.H (Orifice) "H2O
Point Time Meter (W) "H2O Desired Actual
AIZ /0&;2.. z'.:sq_qos o. 21? ~ ..J·(,.e_JI
v=
11 /0'57 1.,4~ l 1 0~3J 1.16 l.20
10 1102 2'16.G3 o.i4 L2~ \.30
aq IJ()7 "2so.~. r o.34 '· ,z--:r I.~
O~ t I 12.. ?,~:3. q s o.lfJ I.SO 1.60
07 ll J 7 2'77. 88 0.4S l.tn ~ 1.70
Oh 1122. 2.02-03 o.48 I. fO l. ]iO
OS 112.9-Z-GG>-sl.f o.<-1~ I.GI I.ho
04 1r.;2-Z-70-~0 oHO I . t";o I . Cf)
CJ3 / I ~7 2 7•-f.~S 0-35' L~I 1-~0
oz. [Jt.f 2. Z78.50 0.50 /.12. I.JO
Ol I I '-fr 28 I .Cf/ o.zs OA~ o.qo
Clv1rii llt:iZ.. z gs.oqq
~12 115& 2 ~5. I f=t-O.LfO I .SO I .S-0
I l 12.03 2iN.G8 0.~8 J .42. 1.lJO
lO /'2.0'6 2 q 2. q:J o.4o J. 50 1.~0
oq 1Zl3 zq6.8'i-f o.t-13 /.6 I L0cJ
Pump
Vac. "Hg
~-0
'-/.0
4.o
!1.0
r.-/.0
5.o-
5.0
'5 .. 0
6-0
0.0
5.0
'5.0
t;.o
,s,o
e:,_o·
6.0
Uncorrected V rn C/t),D'f L> ft3
Corrected v m E/ f. I O,? ft3
%CO2 :J_ IQ %CO -tY
%02 /7-o~, %N2 80-lk
Barometric Pressure (Pb) 2 t{. ZZ '
Amb. °F 7 7 Assumed Moisture % ...J:;. l-=72-
Static Stack Pressure ;,H20 e1-) o.54
Probe Length / Material 4' 3 i a S.S
. Before Middle After
Pitot Tube Leak Check _Jf_ __ ./
Gas Flow Out/ In Initial Leak @ i (), ooCY "Hg = 0-0/'J(!J ft3/min
Final Leak@ /0,(JOO "Hg = O,OO(J) ft3/min
Temperature °F %
Probe Ts (stack) Tmln Tm Out Filter Exit Cold Filter lsokinetic
1,4q l??q 77 ---2€5 G3 -
250 19CJ 77 -2.46 6q -
252 1qa 17 -2Y=t-SI -
2/16 lqo 77 -zs3 £/ff -
zlJq 1qo 78 -2<-/6 4q -
Z<SZ. 1fq 77? --z4q 4g -
l4q I gq 7g -248 4q -
2'-16 I %I 78 -251 50 -ILC .-, ~l!:'
; _.,v...,
zqq rzi 7?? -il/6 c; I -
251 JJ8 7q -Z.4S '52.. -
2l/q 191-7q -Z55 03 -
2% 11q ttf -llf6 Slf -
2~, llfO 7q -2s4 G3 -
291 1iq 7q ·-153 51 -
Z.Sl /q_o 7q -2'53 l-J ?--
Z5S l q 2. 7q -2,':53 i/9 -
Sample Purge: Initial .-Final -
Volume Collected Vied 17. '/ ml Sample Time, e 120 min.
Run No. 2.
Clock Ory Gas L'.P (Pitot)
Point Time Meter (ft"') "H2O
0-s? )21"8 .3 oo.-&' l 0.115,.~
01-12Z.§ gos-. J-R O.l-/f?
(Jh )·2-'2.'3 3gq_ ◊CJ o.;~
D5 i2g3 ~ ,~. 3-S-o.~5
f\4 12. 3~ 3 J 7. oq 0. ~3
03 1243 Z..2,0.74 0.?~
02. 12l-f2 3?4.0l 0-2~
Of 1203 2..27.JZ. Q.?~
4tnd 125~ b'30,G~3
m
'""
~
~
!~
I !;
Date: ?f'2U'i/ZOW
___ YYJ~G __ Field Data
Facility B » E 1, V e,vn~I
L'.H (Orifice) "H20 Pump
Desired Actual Vac. "Hg Probe Ts (stack)
1.68 l.70~' t5.&·" • -2 Slf 1a2
1.'80 1.~(5 t;;,O 2.152. 1q3
l.42 1.l,/o 6,0 2SS l W-1
l.31 l..sO '1.0 zyq 1q4
1.2~ l.ZO ~.O 29-1 )q5
1.0~ LO t;,{) 7-SC:, /qt-{
o.Q~ 9~0 5.0 2.0~ 103 -
0.75' ()¥7~ 4.0 '.2.~ I ctO
. .,,. -·
...
.i,ti·,!';
Western Environmental SeNices and Testing, Inc.
Page_b__of~
Source/ I.D. No. P1::,w:#:-3
Temperature °F %
Tmln Tm Out Filter Exit Cold Filter lsokinetic
7q -265 t..Jq -
7q -2--50 60 -
7q -z,sl 51 -
)<(') -2.~3 5/ -
RO -250 SJ -
RO -260 51 -
5?0 -24q S3 -
81 -ZSJ 55 -
t
,$'-
r~
.£.tf:' ni.,,~-
·o;,i$ ...
~.C"
¢"i·t
'..
',,)\~!',~!
Western Environmental Services and Testing, Inc
Job Number: Run #: ____ --<f,---"""-'~=--'------
Field Data: Filter#: __ XT~_,___ .... _7:_,_..S~S.~----
Source ID: Balance Check (500 g): v::::
lmpinger# 1 2 3 4 l!H=
tiP=
· ContentsNol. ~ sq. root l!P
Tip Style T = m
Final Wt. .7.., T= s
Initial Wt. Vm,td=
Difference Vw9,.=
% Moisture=
lmpinger # 5 6 7 8 Gd=
ContentsNol. Mwd=
Mw=
Tip Style Vs (fUmin)=
Final Wt. ACFM=
Initial Wt. SCFM=
Difference % E.A.=
lrotal, grams I ~ I Silica Gel (%Spent): %\sokinetic=
Date: d. 7 7' 9
(Check one) Grab Sample: __
Integrated Single Point: __
Integrated Muti Point: __
Time:
Replicate Original Aliquot CO2 Volume
Measurement (mis) (1) (mis) (2)
1 100
2. 100
3. 100
Mean 100
COMMENTS:
-------Analyst Initials: _____ _
Initial Leak Check:
Final Leak Check:
Leak check must not change level by more than 0.2 mis in 4 minutes
ORSAT Analysis
0 2 Reading 0 2 Volume N2/CO by Difference Dry Molecular
(mis} (3) (mis) (4)=(3-2) (mis) (5)=(1-3) WeightMwd
!
(Mwd "l.ust agree within +/-0.3 gig-mole from their mean for any 3 analyses)
Western Environmental Services and Testing, Inc.
Facility ~ tt E;,<;. Vevo0 I Job No: 24-/O"l:3 Schematic of Stack Cross Section K Fa ctor 3.7~
Run No. ?> Date: S/2f)I, rzozy
Source/ 1.0.No. Drjv J±-_g
Stack: Area in2 (A5) l'!.Zli'. 52 Dia (in) 4 I 'I'S
Operators ~-Robi,SOV\-2
Meter Box# IZ. Calib. Factor(Y) G.CJ7&'
Delta H @ I. 713
Nozzle# • \J-2 Diameter (On) O. zzq
Pitot 1.0. A -9 Calib. Factor(Cp) 0. '?J½ I
yY) S Field Data
Clock Ory Gas t.P (Pilot)
Point Time Meter (W) "H20
A-I7-J3~~ 330./04 0 .~0
\ I I ~<Jg 2,~t;G' o.34
10 ,~,~ ~37. 10 0 .:2>Lf
09 i ;21' ?-,Lj I. 00 (i.l-/~
05? 13~ Ill' ?}ilf. q I 0.1../~
o:,-. 1530 s 4 Ci!. I 3 o.4~
00 ,3 y3 ;s3_ l/ 6 [1.~1?
0 c; 13 l/'9, 1-i51. 44 o.5Z
0'-1 ,;~j 36 I.I '-I 0.28
OS /353 3 ~ 4. Lf 3 o. z ~
02.. 1403 ~h 7. 7 / n. 2~
01 1<--10~ 310. q 1--r?.2'8
&-irl ll-/1 ~ ~7Lf . 23'-I
tJ, I Z I '11 ~ 31'-IJ./0 I o.~
11 I 1../2.5 377. 7S 0 .30
/0 /£/21. '2,R l .lr o.32
09 JY3 3 ~%/ 7 1 0 .35
Hor Up
t.H (Orifice) "H 20 Pump
Desired Actual Vac. "Hg
I. 12.. 1./ 0 Y.o
I. 29"" 1.80 L-f.O
1.29' 1-30 6.0
I. 6 J l.fD '3.o
/.iflff ).7CJ G.O
1-30 I .fO s .o
l .'-12.. 1.40 e:s .o
I. zo 1.20 5.o
I. OS I.O 6 .n
I. 05 t.0 Ci. 0
I .Ot:; /.0 ~-0
I .Or;' I.O s.o
1.12 I. 1cJ Y.o
I, J Z. I_. I 0 4,0
I. 20 ,. 2 0 ~.D
I .3 J I . ?,0 5.. C)
%CO 2 2 (/i ¾CO -e-
%0 2 / 7. o <} %N2 <lo. l ~
Barometric Pressure (Pb) 2 , .. Lz::;i. '
Amb. °F ?O Assumed Moisture % I "'-1--
Static Stack Pressure .-,H20 (3,'-) Q.S4
Probe Length / Material L/ '!!) lass
Be/ Middle
Pitot Tube Leak Check __ -=-
Gas Flow Out / In Initial Lea k @ /0. O O CJ "Hg = o .oQ.CLJt~/min
Final Leak @ to _ do o "Hg =~o o ft3/min
Temperature °F %
Probe T5 (s tack) Tmln Tm Out Filter Exit Cold Filter lsokinetic
ZCSG l?Cf i1 --2~~ 00 -
ZS / ,gi xO -265°' rrio --
246 1iq 5?0 ----zc:, } t;,.'.s -
zso 1x1q RI -2S9i 51 -
253 I ??Cf 81 ~ 2.~3 S2 -
2SS I ~8 '61 -2.. i.f 5? ~3 -
2-5_3 18q 8) -254 Ci6 -
25 / 18} ~} -253 S5 --;
2 51 l[?Y Rl -250 54 -
2S4 I f3 x i -2.5"0 65' -
7..t.-/6 183 xz -2so 56 -
1Cj'7 l??'i RZ -25/ 50 -
zyq 188 ?iZ -2'18 h3 -
z.'-IG )t2 82 -2..51 0 6 -
2 v) -:;.., 189 82 --Zl18 S6 ___,
Z51 100 8l -2-S3 Sr -
Sample Purge: Initial -Final __ _
Volume Collected V1r1~ 7 7 ,8'" ml Sample Time, 0 / 2 o min.
RunNo.~2-
Clock Dry Gas b.P (Pitot)
Point Time Meter (ft'') "H20
08 ILJ8i ?:,8R g-::;-0-~~~~
09' ll-J49> 3q z. 2. 2.. o.40
00 )i/48 ;qG. 2 o O.lf~
OS tuf03 y 00.~ 2. 0,40
olf llf 6S L-JaY.3~ 0.38
03 tSD3 ~O~. 2~ n.~5"'
02 IS03 l-j 12. 09 0.3S
DJ l t:J I .3 4 I<;. 7 S-n.g,s-
llnrA IS 18 L-(1. q,. s z l
w ..
l~
Hiil! .,,
d.l
I,,Lt
b.H (Orifice) "H20
Desired Actual
__ -rrJ_,_0.<---_ Field Data
Facility ~rt E.x Vt,fh/11\
Pump
Vac. "Hg Probe T5 (stack)
1.L-/2. I .40_,_ •• c:;_r!j·< ·~24q I Cf-0
1.'30 I.SO 6.0 260 1qo
1.01 !. Go tr\.~ 7_,sy 1~q
I. 50 I.SO ~.G 2lfG l&r
1.42. 1.40 G:i.O 25/ l 81--
'-~' 1.;0 0. () 25 I !i?6
l .3 / l. 30 6.,0 265 l8Y
I. g f 1.30 5.0 2so 186
., . ...
~
),.~-
Western Environmental Services and Testing, Inc.
Page~of-1:_
Source/ I.D. No. Dg-ec #-3
Temperature °F
Tmln Tm Out Filter Exit
fs2.. -248 cs-::;-
iz -? 4fo sY
8L -2'50 55'
82.. -2.5 J 56
'X 2. -25) S8
??2--z4q CjCJ
f?z_ -251 5q
82 -25'1 sq
',
,,.~~ .. ·~-;. ,., .,.
%
Cold Filter lsokinetic
-
-----
-
-
-
I
:~--
"
..:.;,,.
,;:;•
/;t~·.~1
Western Environmental Services and Testing, Inc
Job Number:
Field Data:
Source ID: Balance Check (500 g):
lmpinger# 1 2 3 4 nH=
LIP=
ContentsNol.
sq. root L'lP
Tip Style Tm=
Final Wt. T= s
Initial Wt. Vmstd=
Difference VWgas=
% Moisture=
lmpinger# 5 6 7 a, Gd=
··,,
ContentsNol. Mwd=
"Mw=
Tip Styie Vs (ft/min)=
"'•~·~
Finai Wt. ACFM=
'
Initial Wt SCFM=
Difference % E.A.=
' 21~.-r ..
' smb Gel (%Spent); Total, grams %\sokinetic=
Date: ------
• (Check one) Gra·b Sample: __ •
Integrated Single Point: __
Integrated Muti Poin't: __ .
-•
Time:
Replicate Original Aliquot CO2 Volume
Measurement (mis) (1) '(tnis) (2)
1 100
2 100
.3 100 . , ,,
.,
. fop ·Mean
' !
COMMENTS:
.....,_ _____ _ Analyst Initials: _____ _
Initial Leak Check:
Final Leak Check:
_ Leak check must not change level by more than 0.2 mis in 4 minutes
OR.SAT Analysis
0 2 Re.ading 0 2 Volume Nif,CO.by Difference Dry Molecular
.(mis) (3) (mis) (4)=(3-2) (ml$) (5)=(1-3) Weight Mwd .. .
..
(Mwd must agree w1thIn +/-0.3 gig-mole from their mean for any 3 analyses)
Opacity
\
• Western Environmental Services and Testing, Inc.
Source Name fJ,-u,r,,,,.-#'·J Observati~fc 7, ~r/ Start Time f! '2f Stop Time~ ~::2$"
Address Rf./fl?'i vt,rn Q./{ ~ 0 15 30 45 ~ 0 15 30 45 ,Im l
I Q, 0 0 0 31 n ~ 0 §)
City .Vi-,-no.,I State ur Zip 2 0 a, (); 0 32 0 q n t<'l
Phone Source ID Number 3 0, Q /} 0 33 0 r'I 11 .,,..
Process Equipment Or ':f.wf,/"' Operating Mode ~,h, 4 Q, ll (J .ll' 34 n 0 ~ 0
Control Equipment « .. ,tlll .. YJ
Operating Mode R.,. f/0
-0 0. ,.vv,,.,ft, -5 (}I (J (J 0 35 0 0
Describe Emission Point~ 0 6 ('} (J /) (l 36 (') 0 ,1, /}
Height Above Ground Levelj~(f Height Relative to Observer Q. $" f'.+-7 n (}, 0 n, 37 n Ci) ,> 0
Distance From Observer !uitt Direction From Observer .fLJ -(} 8 0 Q;. (J 38 0 ,.., 0 0
Describe Emissions 9 0 (\ () 0 39 l'.l. /1 /7 0 ~ L":9 /,l-1,.J;/4 ~/g:rop
.
Start 10 a () 0 n 40 a /1 0 ,(7 ,,
Plume Type -Conti;1uous -Emission Color 11 C), 0 Q () 41 0 0 /"l /'7
Start iJ /1;,r k wL.J.~ 1=
· Stop Ful!itivc; -Intermittent 12 6) 0 a t') 42 /1.. /I /l 0. c.,,
Water Droplets Present If Water Droplet Plume 13 (J (] 0 () 43 r} () 0 r'.'>
No i,l ;
Yes D Attached D Detached D 14 a 0 0 0 44 (] 0 5'' (l
Point in the Plume at which opacity was determined 15 0 0 Q (fJ 45 Q 0 ./':Y {li
} ·a -Start C,-(/)1 Stop 0-10 16 0 0 Q D 46 () l'1 a
Describe Background 17 Q 0 a 0 47 (,) i'J (;) (}
Start £/., _ . Ill t,i(, J' #.~ __. Stop <a,...,...-e.. 18 ,,., a Q 0 48 CJ) I) 11 /,l,
V
() Background Color Sky Conditions 19 n 0, Q 0 49 Q l'.'ll r\
Start 1(/ ... Stop 13/w; Start l.k,,,;,,.. Stop /j,d/ 20 0 0 j 0 50 -s {) 11 fi
Wind Speed, mph Wind Direction, degrees 21 r, CJ 0 0 51 '5 ~ a ~ -
Start t§'o Stop 5 Start NIA Stop J"Jn 22 Q., Q 0 Q 52 0 (,) I'.) /)
Ambient Temp., °F Wet Bulb Temp., °F R.H percent 23 r.} 0 n 0 53 Q 0 I') 0
Start ii!l"' Stop /;1-'3'1 24 r"".J IJ r, G 54 (J 5 0 0
Source Layout Sketch Draw North Arrow G 25 0 rJ (1 0 55 0 (J /') 0
26 (') ('y a 56 CJ 0 (;) '.5" I"\, ..,, -27 . I\ (\ 0, 0, 57 0 (';) 0 0
X Emission Point 28 () () (J 5" 58 0 0 0 0 f 29 (), 1 () () 59 0 a 0 0 .
Sun -6-Wind ...... 30 5' D a Q 60 0 0 0 0
I Observers Position Average Opacity For 1s: Number of Readings Above Pl11mea11d a: Highest Period (.) • ~ % Were / J Stack ~~~ Range of Opacity Readings
S~cation Line Minimum Cl Maximum '75
I Observers Name (Print) 13r1',, ... rlG ~ Comments Q:fv" J. ,,,6 ,A • /lt} ____
Observer's Signatu~~/~ .f'/,;;i,,/~
I have received a copy of these Opacity Observations
Organization: Western Environmental, Casper, Wyoming
,
Signature Certified By5,' akrc s;~ 1/1. 0~ Aok.
Date 'tff)'l/"olf-' J .,;;:I/ .;.J-;,._I~ 1' .. ~
loate
Verified By V Date
Title
I
Western Environmental Services ancl Testing, Inc.
Source Name
Address
City
Phone
Process Equipment
Control Equipment
Describe Emission P
Distance From Observer
Describe Emissions
Start /Y'o
Emission Color
Water Droplets Present
Yes D No
State llf,1 Zip
Source ID Number
Operating Mode
Operating Mode
Height Relative to Observer 2,1{,J!f
Direction From Observer
Stop
Plume Type -Continuous
"itiv -itennittent
If Water Droplet Plume
Attached D Ddached □
Point in the Plume at which opacity was cletcnnincd
Start o -o'
Describe Background
Start £,/,e~,-'8 'wl, JK,
Background Color
Start
Wind Speed, mph
Start &
Stop
Sto)
Ambient Temp., °F
• () ;,;()
Start f Stop 7lJ
Source Layout Sketch
Sun-()-Wind ....._
I
Plumeand ~
Stack v_
Comments
Stop .. lD 1
r Stop
Wind Direction, degrees
Start /7"-Stop
Wet Bulb Temp., °F RH percent
3
Draw North Arrow (!)
X Emission Point
Observers Position
I have received a copy of these Opacity Observations
Signature
Title Date
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
25
26
27
28
29
Average Opacity For
Highest Period 0•t./..J
Range of Opacity Readings
Minimum Q
Organization:
Stop Time /:}/()
Number of Readings Above
% Were 9
Maximum5"'
4
Western Envirnnmcntal Services and Testing, Inc.
Source Name
Address
City
Phone
Process Equipment
Control Equipment
Describe Emission Po·
Distance From Observer
Describe Emissions
Emission· .olor
Start ulk Stop
Water Droplets Present
Yes D No
~
vu;w.J
State l,/ Zip
Source ID Number
Operating Mode
Operating Mode
Direction From Observer
Fugitive -lntennittent
If Water Droplet Plume
Attached D Detached D
Point in the Plume at which opacity was detennined
Start O • l O I Stop , -I 0
Describe Background
Start c/-tov,,-
Background Color
Start 'D.
Wind Speed, mph
Start '-Stop
Ambient Temp., °F
Start i I Stop g3
Source Layout Sketch
Sun -0 Wind ..._
I
Plume and r::-
Stack v_
Stop
Wind Direction, degrees
Start J 10 Sto ~ Q 0
Wet Bulb Temp., °F RH percent
Draw North Arrow ~
X Emission Point
Observers Position
Sun Location Line
Comments
I have received a copy of these Opacity Observations
Signature
Title Date
Stop Time fl
15 30
2
3
4
5
6
7
8
9
12
13
14
15
16
17
18
22
23
24
25
26
27
28
29 0
30 0
Average Opacity For Number of Readings Above
Highest Period (J , 'l f Ci,., ~IJH (}lo Were ·2
Range of Opacity Readings
Minimum CiJ
Observers Name (Print)
Observer's Signature
Verified y
Maximum)
Date
45
CEMS
Date Time NOx [ppm] 02 [%] CO2[%]
5/28/2024 15:03:58 35.82 20.44 20.24
5/28/2024 15:04:58 35.24 20.41 20.2
5/28/2024 15:05:58 71.931 20.431 20.19
5/28/2024 15:06:58 0.78 20.42 20.18
5/28/2024 15:07:58 1.69 15.45 14.27
5/28/2024 15:08:58 1.75 9.86 10
5/28/2024 15:09:58 1.73 10.15 10.08
5/28/2024 15:10:58 1.571 10.181 10.08
5/28/2024 15:11:58 1.51 10.18 10.08
5/28/2024 15:12:58 1.35 10.17 10.04
5/28/2024 15:13:58 1.281 10.11 10
5/28/2024 15:14:58 1.15 10.12 10
5/28/2024 15:15:58 1.05 10.13 9.99
5/28/2024 15:16:58 0.96 10.13 9.98
5/28/2024 15:17:58 0.81 10.14 9.97
5/28/2024 15:18:58 0.74 10.13 9.96
5/28/2024 15:19:58 0.59 10.15 9.97
5/28/2024 15:20:58 0.53 10.15 9.97
5/28/2024 15:21:58 0.38 10.16 9.96
5/28/2024 15:22:58 0.33 10.15 9.94
5/28/2024 15:23:58 0.22 17.99 17.11
5/28/2024 15:24:58 0.18 21.09 20.33
5/28/2024 15:25:58 0.01 20.44 20.22
5/28/2024 15:26:58 -0.011 20.441 20.12
I 5/28/2024 15:27:58 0.05 20.44 20.01
5/28/2024 15:28:58 0.1 20.45 19.92
5/28/2024 15:29:58 0.1 20.46 19.83
5/28/2024 15:30:58 0.11 15.06 13.78
5/28/2024 15:31:58 0.04 9.89 9.98
5/28/2024 15:32:58 -0.02 10.08 9.94
5/28/2024 15:33:58 -0.011 10.181 9.92
5/28/2024 15:34:58 -0.01 10.18 9.92
5/28/2024 15:35:58 -0.01 10.19 9.92
5/28/2024 15:36:58 -0.01 10.2 9.77
5/28/2024 15:37:58 -0.021 10.111 9.84
5/28/2024 15:38:58 -0.01 10.1 9.83
5/28/2024 15:39:58 -0.01 11.15 11.53
5/28/2024 15:40:58 -0.01 21.22 20.1
5/28/2024 15:41:58 -0.02 21.41 20.14
5/28/2024 15:42:58 -0.02 21.16 20.15
5/28/2024 15:43:58 -0.021 20.411 20.16
5/28/2024 15:44:58 -0.01 14.99 13.94
5/28/2024 15:45:58 -0.02 10.16 9.97
5/28/2024 15:46:58 -0.021 10.191 9.95
5/28/2024 15:47:58 -0.01 10.17 9.93
5/28/2024 15:48:58 0.06 10.13 9.87
5/28/2024 15:49:58 0.161 10.141 9.86
5/28/2024 15:50:58 0.1 12.83 6.69
5/28/2024 15:51:58 8.93 18.27 0.43
5/28/2024 15:52:58 95.6 0.03 0.15
5/29/2024 5:55:58 0.24 -0.05 -0.01
5/29/2024 5:56:58 0.21 -0.06 -0.01
5/29/2024 5:57:58 0.16 -0.07 -0.01
5/29/2024 5:58:58 0.15 -0.03 0
5/29/2024 5:59:581 0.121 -0.02 -0.01
5/29/2024 6:00:58 1.33 -0.04 -0.01
5/29/2024 6:01:58 46.73 -0.05 0
5/29/2024 6:02:58 49.63 -0.04 0
5/29/2024 6:03:58 49.74 -0.07 -0.01
5/29/2024 6:04:581 50.021 -0.03 0
5/29/2024 6:05:58 38.75 -0.02 0
5/29/2024 6:06:58 24.73 -0.03 0
5/29/2024 6:07:58 25 -0.01 -0.02
5/29/2024 6:08:581 25.031 -0.011 -0.011
5/29/2024 6:09:58 30.88 14.27 0
5/29/2024 6:10:58 34.88 20.94 0
5/29/2024 6:11:58 34.97 20.96 0
5/29/2024 6:12:58 35.08 20.99 0
5/29/2024 6:13:58 35.07 21 -0.01
5/29/2024 6:14:58 35.09 20.98 0
5/29/2024 6:15:58 35.09 20.96 0
5/29/2024 6:16:58 35.14 20.98 0
5/29/2024 6:17:58 35.2 20.98 0
5/29/2024 6:18:58 35.18 20.96 0
5/29/2024 6:19:58 13.72 20.85 6.22
5/29/2024 6:20:58 0.39 20.66 22.18
5/29/2024 6:21:58 0.11 20.87 22.36
5/29/2024 6:22:58 0.01 20.46 20.27
5/29/2024 6:23:58 -0.08 20.42 20.22
5/29/2024 6:24:58 0.021 20.391 20.21
5/29/2024 6:25:58 0.02 13.54 12.04
5/29/2024 6:26:58 -0.04 10.14 10.06
5/29/2024 6:27:58 -0.06 10.15 10.08
5/29/2024 6:28:58 0.021 10.181 10.091
5/29/2024 6:29:58 -0.03 12.89 6.68
5/29/2024 6:30:58 -0.02 11.21 8.84
5/29/2024 6:31:58 -0.04 10.2 10.11
5/29/2024 6:32:58 0.051 10.211 10.11
5/29/2024 6:33:581 8.47 6.37 0.03
5/29/2024 6:34:58 16.31 0.46 1.49
5/29/2024 6:35:58 24.83 0.05 0.04
5/29/2024 6:36:58 24.85 0.04 0.04
5/29/2024 6:37:581 251 0.03 0.041
5/29/2024 6:38:58 17.46 13.64 0.89
5/29/2024 6:39:58 14.25 17.42 2.5
5/29/2024 6:40:58 14.35 17.43 2.5
5/29/2024 6:41:58 14.38 17.42 2.5
5/29/2024 6:42:58 14.47 17.42 2.51
5/29/2024 6:43:58 14.56 17.42 2.5
5/29/2024 6:44:58 14.67 17.42 2.51
5/29/2024 6:45:58 14.69 17.41 2.51
5/29/2024 6:46:58 14.78 17.4 2.51
5/29/2024 6:47:58 14.77 17.39 2.52
5/29/2024 6:48:58 14.8 17.39 2.51
5/29/2024 6:49:58 14.78 17.39 2.51
5/29/2024 6:50:58 12.39 18.08 1.91
5/29/2024 6:51:58 13.97 17.63 2.48
5/29/2024 6:52:58 14.96 17.37 2.52
5/29/2024 6:53:58 15.09 17.35 2.53
5/29/2024 6:54:58 15.26 17.34 2.53
5/29/2024 6:55:58 15.26 17.34 2.53
5/29/2024 6:56:58 15.31 17.33 2.53
5/29/2024 6:57:58 15.39 17.33 2.54
5/29/2024 6:58:58 15.44 17.32 2.54
5/29/2024 6:59:58 15.5 17.31 2.55
5/29/2024 7:00:58 15.4 17.3 2.56
5/29/2024 7:01:58 15.46 17.28 2.56
5/29/2024 7:02:58 15.57 17.27 2.57
5/29/2024 7:03:58 15.6 17.27 2.57
5/29/2024 7:04:58 15.58 17.27 2.57
5/29/2024 7:05:58 15.64 17.27 2.57
5/29/2024 7:06:58 15.62 17.26 2.58
5/29/2024 7:07:58 15.65 17.24 2.59
5/29/2024 7:08:58 15.73 17.24 2.6
5/29/2024 7:09:58 15.74 17.23 2.6
5/29/2024 7:10:58 15.68 17.23 2.6
5/29/2024 7:11:58 15.52 17.29 2.56
5/29/2024 7:12:58 15.55 17.18 2.64
5/29/2024 7:13:58 16.04 17.17 2.64
5/29/2024 7:14:58 16.04 17.19 2.63
5/29/2024 7:15:58 15.97 17.2 2.62
5/29/2024 7:16:58 16.14 17.21 2.62
5/29/2024 7:17:58 16.18 17.22 2.61
5/29/2024 7:18:58 16.1 17.2 2.62
5/29/2024 7:19:58 16.14 17.21 2.62
5/29/2024 7:20:58 16.02 17.21 2.62
5/29/2024 7:21:58 15.81 17.2 2.62
5/29/2024 7:22:58 15.8 17.2 2.63
5/29/2024 7:23:58 15.94 17.19 2.63
5/29/2024 7:24:58 15.98 17.2 2.63
5/29/2024 7:25:58 16.08 17.19 2.63
5/29/2024 7:26:58 16.1 17.19 2.64
5/29/2024 7:27:58 16.1 17.19 2.64
5/29/2024 7:28:58 16.05 17.18 2.64
5/29/2024 7:29:58 16.09 17.19 2.64
5/29/2024 7:30:58 16.18 17.19 2.64
5/29/2024 7:31:58 16.32 17.19 2.64
5/29/2024 7:32:58 16.32 17.19 2.64
5/29/2024 7:33:58 16.32 17.19 2.64
5/29/2024 7:34:58 16.31 17.18 2.65
5/29/2024 7:35:58 16.2 17.17 2.65
5/29/2024 7:36:58 16.26 17.18 2.65
5/29/2024 7:37:58 16.26 17.19 2.65
5/29/2024 7:38:58 16.28 17.18 2.65
5/29/2024 7:39:58 16.2 17.19 2.64
5/29/2024 7:40:58 16.32 17.19 2.65
5/29/2024 7:41:58 16.26 17.17 2.65
5/29/2024 7:42:58 16.25 17.16 2.66
5/29/2024 7:43:58 16.21 17.15 2.66
5/29/2024 7:44:58 16.21 17.13 2.67
5/29/2024 7:45:58 16.21 17.12 2.67
5/29/2024 7:46:58 16.28 17.12 2.68
5/29/2024 7:47:58 16.32 17.11 2.68
5/29/2024 7:48:58 16.27 17.11 2.68
5/29/2024 7:49:58 16.16 17.11 2.68
5/29/2024 7:50:58 15.98 17.12 2.68
5/29/2024 7:51:58 15.98 17.12 2.67
5/29/2024 7:52:58 16.04 17.13 2.66
5/29/2024 7:53:58 16.09 17.13 2.67
5/29/2024 7:54:58 16.09 17.13 2.67
5/29/2024 7:55:58 16.09 17.12 2.68
5/29/2024 7:56:58 16.04 17.13 2.67
5/29/2024 7:57:58 16.04 17.13 2.67
5/29/2024 7:58:58 16.09 17.13 2.67
5/29/2024 7:59:58 16.05 17.13 2.67
5/29/2024 8:00:58 16.13 17.12 2.67
5/29/2024 8:01:58 16.08 17.12 2.67
5/29/2024 8:02:58 16.08 17.13 2.67
5/29/2024 8:03:58 16.18 17.13 2.67
5/29/2024 8:04:58 16.08 17.13 2.67
5/29/2024 8:05:58 16.05 17.12 2.67
5/29/2024 8:06:58 15.98 17.12 2.67
5/29/2024 8:07:58 15.98 17.12 2.67
5/29/2024 8:08:58 16.17 17.11 2.67
5/29/2024 8:09:58 16.21 17.11 2.66
5/29/2024 8:10:58 16.17 17.1 2.66
5/29/2024 8:11:58 16.2 17.1 2.67
5/29/2024 8:12:58 16.11 17.09 2.67
5/29/2024 8:13:58 16.17 17.09 2.66
5/29/2024 8:14:58 16.21 17.09 2.66
5/29/2024 8:15:58 16.21 17.08 2.67
5/29/2024 8:16:58 16.27 17.08 2.67
5/29/2024 8:17:58 16.31 17.09 2.67
5/29/2024 8:18:58 16.31 17.07 2.68
5/29/2024 8:19:58 16.32 17.06 2.68
5/29/2024 8:20:58 16.39 17.05 2.69
5/29/2024 8:21:58 16.44 17.05 2.69
5/29/2024 8:22:58 16.35 17.05 2.69
5/29/2024 8:23:58 16.35 17.05 2.69
5/29/2024 8:24:58 16.21 17.06 2.68
5/29/2024 8:25:58 16.19 17.06 2.68 <Start Run 1
5/29/2024 8:26:58 16.2 17.06 2.68
5/29/2024 8:27:58 16.21 17.06 2.68
5/29/2024 8:28:58 16.22 17.07 2.67
5/29/2024 8:29:58 16.3 17.06 2.68
5/29/2024 8:30:58 16.24 17.05 2.68
5/29/2024 8:31:58 16.27 17.06 2.68
5/29/2024 8:32:58 16.21 17.06 2.67
5/29/2024 8:33:58 16.11 17.07 2.67
5/29/2024 8:34:58 16.14 17.06 2.67
5/29/2024 8:35:58 16.21 17.06 2.67 <point
5/29/2024 8:36:58 16.23 17.06 2.67
5/29/2024 8:37:58 16.33 17.05 2.68
5/29/2024 8:38:58 16.35 17.06 2.67
5/29/2024 8:39:58 16.12 17.06 2.67
5/29/2024 8:40:58 16.16 17.06 2.67
5/29/2024 8:41:58 16.32 17.05 2.67
5/29/2024 8:42:58 16.27 17.06 2.67
5/29/2024 8:43:58 16.27 17.05 2.67
5/29/2024 8:44:58 16.31 17.05 2.67
5/29/2024 8:45:58 16.5 17.05 2.67 <point
5/29/2024 8:46:58 16.51 17.05 2.67
5/29/2024 8:47:58 16.41 17.05 2.68
5/29/2024 8:48:58 16.32 17.05 2.68
5/29/2024 8:49:58 16.32 17.05 2.68
5/29/2024 8:50:58 16.28 17.08 2.65
5/29/2024 8:51:58 16.16 17.11 2.64
5/29/2024 8:52:58 16.38 17.1 2.64
5/29/2024 8:53:58 16.33 17.1 2.64
5/29/2024 8:54:58 16.17 17.1 2.64
5/29/2024 8:55:58 16.21 17.09 2.65 <point
5/29/2024 8:56:58 16.31 17.07 2.66
5/29/2024 8:57:58 16.48 17.07 2.66
5/29/2024 8:58:58 16.48 17.08 2.65
5/29/2024 8:59:58 16.36 17.07 2.66
5/29/2024 9:00:58 16.37 17.07 2.66
5/29/2024 9:01:58 16.52 17.06 2.66
5/29/2024 9:02:58 16.55 17.07 2.66
5/29/2024 9:03:58 16.52 17.07 2.65
5/29/2024 9:04:58 16.43 17.06 2.66
5/29/2024 9:05:58 16.3 17.06 2.66 <point
5/29/2024 9:06:58 16.21 17.04 2.68
5/29/2024 9:07:58 16.16 17.04 2.68
5/29/2024 9:08:58 16.1 17.03 2.68
5/29/2024 9:09:58 16.16 17.02 2.69
5/29/2024 9:10:58 16.29 17.02 2.69
5/29/2024 9:11:58 16.7 17.02 2.69
5/29/2024 9:12:58 16.88 17.02 2.68
5/29/2024 9:13:58 16.55 17.02 2.68
5/29/2024 9:14:58 16.46 17.02 2.68
5/29/2024 9:15:58 16.53 17.02 2.67 <point
5/29/2024 9:16:58 16.47 17.02 2.67
5/29/2024 9:17:58 16.44 17.02 2.67
5/29/2024 9:18:58 16.4 17.03 2.67
5/29/2024 9:19:58 16.32 17.03 2.66
5/29/2024 9:20:58 16.27 17.04 2.66
5/29/2024 9:21:58 16.17 17.05 2.65
5/29/2024 9:22:58 16.08 17.05 2.64
5/29/2024 9:23:58 16.09 17.06 2.64
5/29/2024 9:24:58 16.09 17.06 2.64
5/29/2024 9:25:58 16 17.06 2.64 <point
5/29/2024 9:26:58 16.04 17.06 2.64
5/29/2024 9:27:58 16.19 17.06 2.65
5/29/2024 9:28:58 16.5 17.06 2.64
5/29/2024 9:29:58 16.71 17.06 2.64
5/29/2024 9:30:58 16.64 17.05 2.65
5/29/2024 9:31:58 16.39 17.05 2.65
5/29/2024 9:32:58 16.08 17.05 2.65
5/29/2024 9:33:58 16.24 17.05 2.65
5/29/2024 9:34:58 16.46 17.05 2.65
5/29/2024 9:35:58 16.41 17.05 2.64 <point
5/29/2024 9:36:58 16.33 17.04 2.64
5/29/2024 9:37:58 16.21 17.02 2.65
5/29/2024 9:38:58 16.31 17.01 2.66
5/29/2024 9:39:58 16.32 16.99 2.66
5/29/2024 9:40:58 16.26 16.98 2.67
5/29/2024 9:41:58 16.32 16.98 2.66
5/29/2024 9:42:58 16.18 16.97 2.67
5/29/2024 9:43:58 16.18 16.95 2.67
5/29/2024 9:44:58 16.17 16.95 2.67
5/29/2024 9:45:58 16.28 16.95 2.66 <point
5/29/2024 9:46:58 16.44 16.95 2.66
5/29/2024 9:47:58 16.43 16.95 2.66
5/29/2024 9:48:58 16.45 16.94 2.66
5/29/2024 9:49:58 16.33 16.94 2.66
5/29/2024 9:50:58 16.27 16.94 2.65
5/29/2024 9:51:58 16.28 16.95 2.65
5/29/2024 9:52:58 16.26 16.95 2.65
5/29/2024 9:53:58 16.18 16.95 2.65
5/29/2024 9:54:58 16.21 16.95 2.65
5/29/2024 9:55:58 16.2 16.95 2.64 <point
5/29/2024 9:56:58 16.14 16.95 2.64
5/29/2024 9:57:58 16.09 16.95 2.65
5/29/2024 9:58:58 16.22 16.94 2.65
5/29/2024 9:59:58 16.25 16.93 2.65
5/29/2024 10:00:58 16.38 16.94 2.64
5/29/2024 10:01:58 16.5 16.94 2.64
5/29/2024 10:02:58 16.53 16.94 2.64
5/29/2024 10:03:58 16.37 16.94 2.64
5/29/2024 10:04:58 16.26 16.93 2.64
5/29/2024 10:05:58 16.23 16.92 2.65 <point
5/29/2024 10:06:58 16.33 16.9 2.65
5/29/2024 10:07:58 16.33 16.87 2.67
5/29/2024 10:08:58 16.49 16.85 2.68
5/29/2024 10:09:58 16.56 16.84 2.69
5/29/2024 10:10:58 16.49 16.84 2.68
5/29/2024 10:11:58 16.44 16.84 2.68
5/29/2024 10:12:58 16.44 16.85 2.67
5/29/2024 10:13:58 16.38 16.85 2.67
5/29/2024 10:14:58 16.37 16.84 2.67
5/29/2024 10:15:58 16.48 16.85 2.66 <point
5/29/2024 10:16:58 16.55 16.84 2.67
5/29/2024 10:17:58 16.53 16.84 2.67
5/29/2024 10:18:58 16.54 16.84 2.67
5/29/2024 10:19:58 16.45 16.84 2.65 NOxppm = 16.33
5/29/2024 10:20:58 16.36 16.84 2.66 02%= 17.00
5/29/2024 10:21:58 16.32 16.84 2.66 CO2%= 2.66
5/29/2024 10:22:58 16.39 16.84 2.65
5/29/2024 10:23:58 16.55 16.84 2.65
5/29/2024 10:24:58 16.45 16.84 2.65 <End Run
5/29/2024 10:25:58 16.75 12.79 1.77
5/29/2024 10:26:58 25.58 0.22 0.13
5/29/2024 10:27:58 24.91 0.07 0.12
5/29/2024 10:28:581 24.891 0.021 0.111
5/29/2024 10:29:58 19.18 5.96 3.62
5/29/2024 10:30:58 1.03 9.61 9.72
5/29/2024 10:31:58 0.38 10.2 10.11
i
I
11
5/29/2024 10:32:581 -0.041 10.221 10.131
5/29/2024 10:33:58 -0.06 10.23 10.01
5/29/2024 10:34:58 12.89 16.64 3.23
5/29/2024 10:35:58 15.8 17.74 2.82
5/29/2024 10:36:58 16.57 17.76 2.81
5/29/2024 10:37:58 16.79 17.77 2.8
5/29/2024 10:38:58 16.95 17.78 2.79
5/29/2024 10:39:58 16.79 17.79 2.79
5/29/2024 10:40:58 16.72 17.79 2.78
5/29/2024 10:41:58 16.87 17.8 2.78
5/29/2024• 10:42:58 16.71 17.8 2.77
5/29/2024 10:43:58 16.74 17.8 2.78
5/29/2024 10:44:58 16.88 17.8 2.77
5/29/2024 10:45:58 16.9 17.82 2.76
5/29/2024 10:46:58 16.84 17.81 2.76
5/29/2024 10:47:58 16.76 17.79 2.77
5/29/2024 10:48:58 17.02 17.8 2.76
5/29/2024 10:49:58 16.97 17.8 2.77
5/29/2024 10:50:58 17.1 17.79 2.76
5/29/2024 10:51:58 17.15 17.79 2.76
5/29/2024 10:52:58 17.03 17.77 2.77 <Start Run 2
5/29/2024 10:53:58 16.81 17.77 2.77
5/29/2024 10:54:58 16.94 17.78 2.76
5/29/2024 10:55:58 17.1 17.79 2.76
5/29/2024 10:56:58 16.93 17.8 2.75
5/29/2024 10:57:58 16.91 17.8 2.75
5/29/2024 10:58:58 17.08 17.79 2.75
5/29/2024 10:59:58 17.05 17.79 2.76
5/29/2024 11:00:58 17.04 17.76 2.77
5/29/2024 11:01:58 16.84 17.76 2.77
5/29/2024 11:02:58 17.17 17.75 2.77 <point
5/29/2024 11:03:58 17.26 17.74 2.78
5/29/2024 11:04:58 17.2 17.74 2.78
5/29/2024 11:05:58 17.15 17.73 2.78
5/29/2024 11:06:58 16.96 17.73 2.78
5/29/2024 11:07:58 17.07 17.75 2.77
5/29/2024 11:08:58 17.36 17.74 2.78
5/29/2024 11:09:58 17.23 17.73 2.78
5/29/2024 11:10:58 17.18 17.73 2.77
5/29/2024 11:11:58 17.15 17.72 2.78
5/29/2024 11:12:58 16.83 17.72 2.78 <point
5/29/2024 11:13:58 17.05 17.71 2.78
5/29/2024 11:14:58 17.23 17.72 2.77
5/29/2024 11:15:58 17 17.71 2.77
5/29/2024 11:16:58 16.05 16.61 2.77
5/29/2024 11:17:58 16.31 16.78 2.77
5/29/2024 11:18:58 16.26 16.83 2.77
5/29/2024 11:19:58 16.2 16.84 2.77
5/29/2024 11:20:58 16.15 16.83 2.77
5/29/2024 11:21:58 16.28 16.82 2.78
5/29/2024 11:22:58 16.51 16.83 2.77 <point
5/29/2024 11:23:58 16.41 16.83 2.77
5/29/2024 11:24:58 16.32 16.83 2.77
5/29/2024 11:25:58 16.28 16.82 2.78
5/29/2024 11:26:58 16.33 16.82 2.78
5/29/2024 11:27:58 16.34 16.82 2.78
5/29/2024 11:28:58 16.42 16.82 2.78
5/29/2024 11:29:58 16.26 16.82 2.78
5/29/2024 11:30:58 16.35 16.83 2.78
5/29/2024 11:31:58 16.38 16.82 2.78
5/29/2024 11:32:58 16.26 16.82 2.79 <point
5/29/2024 11:33:58 16.27 16.82 2.78
5/29/2024 11:34:58 16.82 16.84 2.78
5/29/2024 11:35:58 16.91 16.84 2.78
5/29/2024 11:36:58 16.75 16.84 2.78
5/29/2024 11:37:58. 16.68 16.85 2.78
5/29/2024 11:38:58 16.47 16.85 2.78
5/29/2024 11:39:58 16.45 16.85 2.78
5/29/2024 11:40:58 16.73 16.84 2.78
5/29/2024 11:41:58 16.79 16.84 2.78
5/29/2024 11:42:58 16.88 16.85 2.79 <point
5/29/2024 11:43:58 17.29 16.86 2.78
5/29/2024 11:44:58 17.13 16.85 2.79
5/29/2024 11:45:58 16.99 16.86 2.78
5/29/2024 11:46:58 16.71 16.86 2.78
5/29/2024 11:47:58 16.79 16.87 2.78
5/29/2024 11:48:58 16.74 16.86 2.78
5/29/2024 11:49:58 16.74 16.86 2.78
5/29/2024 11:50:58 16.49 16.86 2.78
5/29/2024 11:51:58 16.72 16.86 2.79
5/29/2024 11:52:58 16.81 16.86 2.78 <point
5/29/2024 11:53:58 16.77 16.86 2.79
5/29/2024 11:54:58 17.01 16.85 2.79
5/29/2024 11:55:58 17 16.85 2.79
5/29/2024 11:56:58 16.81 16.84 2.79
5/29/2024 11:57:58 16.99 16.83 2.8
5/29/2024 11:58:58 16.87 16.85 2.79
5/29/2024 11:59:58 16.6 16.85 2.79
5/29/2024 12:00:58 16.82 16.85 2.79
5/29/2024 12:01:58 16.83 16.84 2.79
5/29/2024 12:02:58 16.83 16.85 2.78 <point
5/29/2024 12:03:58 16.73 16.85 2.78
5/29/2024 12:04:58 16.72 16.84 2.78
5/29/2024 12:05:58 16.8 16.83 2.79
5/29/2024 12:06:58 16.8 16.82 2.79
5/29/2024 12:07:58 16.8 16.8 2.8
5/29/2024 12:08:58 16.9 16.8 2.8
5/29/2024 12:09:58 17.11 16.8 2.8
5/29/2024 12:10:58 17.23 16.81 2.79
5/29/2024 12:11:58 17.19 16.81 2.79
5/29/2024 12:12:58 17.18 16.8 2.8 <point
5/29/2024 12:13:58 17.36 16.81 2.79
5/29/2024 12:14:58 17.46 16.81 2.79
5/29/2024 12:15:58 17.21 16.82 2.78
5/29/2024 12:16:58 17.11 16.82 2.78
5/29/2024 12:17:58 17.23 16.82 2.77
5/29/2024 12:18:58 17.02 16.84 2.76
5/29/2024 12:19:58 17.34 16.84 2.76
5/29/2024 12:20:58 17.33 16.83 2.77
5/29/2024 12:21:58 17.32 16.82 2.77
5/29/2024 12:22:58 17.18 16.82 2.78 <point
5/29/2024 12:23:58 17.26 16.8 2.78
5/29/2024 12:24:58 17.19 16.79 2.78
5/29/2024 12:25:58 17.15 16.77 2.79
5/29/2024 12:26:58 17.04 16.78 2.79
5/29/2024 12:27:58 17.07 16.76 2.8
5/29/2024 12:28:58 17.24 16.77 2.79
5/29/2024 12:29:58 17.26 16.79 2.78
5/29/2024 12:30:58 17.26 16.79 2.78
5/29/2024 12:31:58 17.17 16.78 2.78
5/29/2024 12:32:58 17.3 16.79 2.78 <point
5/29/2024 12:33:58 17.14 16.77 2.78
5/29/2024 12:34:58 16.97 16.78 2.78
5/29/2024 12:35:58 17.27 16.79 2.77
5/29/2024 12:36:58 17.19 16.8 2.76
5/29/2024 12:37:58 17.33 16.8 2.76
5/29/2024 12:38:58 17.58 16.8 2.77
5/29/2024 12:39:58 17.6 16.8 2.76
5/29/2024 12:40:58 17.44 16.79 2.77
5/29/2024 12:41:58 17.68 16.75 2.79
5/29/2024 12:42:58 17.74 16.72 2.8 <point
5/29/2024 12:43:58 17.56 16.7 2.82
5/29/2024 12:44:58 18.06 16.71 2.81
5/29/2024 12:45:58 17.85 16.71 2.81
5/29/2024 12:46:58 17.63 16.68 2.82 NOxppm = 16.99
5/29/2024 12:47:58 17.95 16.67 2.82 02%= 17.00
5/29/2024 12:48:58 18.03 16.68 2.82 CO2%= 2.78
5/29/2024 12:49:58 17.8 16.68 2.82
5/29/2024 12:50:58 17.82 16.69 2.81
5/29/2024 12:51:58 17.74 16.69 2.81 <End Run
5/29/2024 12:52:58 17.53 8.69 1.53
5/29/2024 12:53:58 25.19 -0.07 0.14
5/29/2024 12:54:58 24.77 0.05 0.12
5/29/2024 12:55:581 24.771 ol 0.111
5/29/2024 12:56:58 22.93 2.23 2.34
5/29/2024 12:57:58 0.9 9.94 9.86
5/29/2024 12:58:58 0.35 10.06 10
5/29/2024 12:59:581 0.131 10.141 10.011
5/29/2024 13:00:58 8.11 13.89 5.81
5/29/2024 13:01:58 17.21 17.27 2.86
5/29/2024 13:02:58 17.05 17.13 2.83
5/29/2024 13:03:58 17.23 17.14 2.82
5/29/2024 13:04:58 16.72 17.05 2.81
5/29/2024 13:05:58 16.8 17.03 2.8
5/29/2024 13:06:58 16.86 17.05 2.79
5/29/2024 13:07:58 16.87 17.05 2.79
5/29/2024 13:08:58 16.92 17.05 2.79
5/29/2024 13:09:58 16.88 17.05 2.79
5/29/2024 13:10:58 16.94 17.05 2.79
5/29/2024 13:11:58 16.87 17.06 2.78
5/29/2024 13:12:58 16.84 17.05 2.79
5/29/2024 13:13:58 16.74 17.07 2.78 <Start Run 3
5/29/2024 13:14:58 16.72 17.09 2.77
5/29/2024 13:15:58 16.95 17.11 2.76
5/29/2024 13:16:58 16.85 17.11 2.75
5/29/2024 13:17:58 16.74 17.11 2.75
5/29/2024 13:18:58 16.74 17.09 2.76
5/29/2024 13:19:58 16.64 17.11 2.76
5/29/2024 13:20:58 16.73 17.09 2.77
5/29/2024 13:21:58 16.72 17.08 2.77
5/29/2024 13:22:58 16.85 17.07 2.78
5/29/2024 13:23:58 16.75 17.06 2.79 <point
5/29/2024 13:24:58 17.13 17.06 2.79
5/29/2024 13:25:58 17.1 17.06 2.78
5/29/2024 13:26:58 17.08 17.07 2.77
5/29/2024 13:27:58 16.94 17.09 2.76
5/29/2024 13:28:58 16.67 17.09 2.76
5/29/2024 13:29:58 16.92 17.1 2.76
5/29/2024 13:30:58 16.85 17.08 2.76
5/29/2024 13:31:58 16.98 17.07 2.77
5/29/2024 13:32:58 17.06 17.06 2.77
5/29/2024 13:33:58 17.07 17.07 2.77 <point
5/29/2024 13:34:58 16.86 17.09 2.76
5/29/2024 13:35:58 16.85 17.08 2.76
5/29/2024 13:36:58 16.93 17.08 2.76
5/29/2024 13:37:58 16.71 17.07 2.76
5/29/2024 13:38:58 16.64 17.08 2.76
5/29/2024 13:39:58 16.62 17.09 2.76
5/29/2024 13:40:58 16.58 17.07 2.76
5/29/2024 13:41:58 16.84 17.08 2.76
5/29/2024 13:42:58 16.73 17.06 2.76
5/29/2024 13:43:58 16.62 17.08 2.76 <point
5/29/2024 13:44:58 16.67 17.07 2.76
5/29/2024 13:45:58 16.71 17.07 2.76
5/29/2024 13:46:58 16.62 17.07 2.76
5/29/2024 13:47:58 16.62 17.06 2.76
5/29/2024 13:48:58 16.61 17.09 2.74
5/29/2024 13:49:58 16.5 17.08 2.75
5/29/2024 13:50:58 16.55 17.07 2.75
5/29/2024 13:51:58 16.57 17.06 2.76
5/29/2024 13:52:58 16.59 17.05 2.76
5/29/2024 13:53:58 16.74 17.05 2.76 <point
5/29/2024 13:54:58 16.7 17.06 2.76
5/29/2024 13:55:58 16.52 17.06 2.75
5/29/2024 13:56:58 16.69 17.05 2.76
5/29/2024 13:57:58 16.56 17.05 2.76
5/29/2024 13:58:58 16.67 17.06 2.75
5/29/2024 13:59:58 16.86 17.08 2.74
5/29/2024 14:00:58 16.71 17.08 2.74
5/29/2024 14:01:58 16.7 17.07 2.75
5/29/2024 14:02:58 16.86 17.06 2.75
5/29/2024 14:03:58 16.87 17.05 2.76 <point
5/29/2024 14:04:58 17.03 17.04 2.76
5/29/2024 14:05:58 16.85 17.05 2.76
5/29/2024 14:06:58 16.76 17.04 2.76
5/29/2024 14:07:58 16.76 17.04 2.77
5/29/2024 14:08:58 16.8 17.03 2.77
5/29/2024 14:09:58 16.87 17.04 2.76
5/29/2024 14:10:58 16.73 17.04 2.76
5/29/2024 14:11:58 16.65 17.05 2.75
5/29/2024 14:12:58 16.72 17.07 2.74
5/29/2024 14:13:58 16.57 17.07 2.73 <point
5/29/2024 14:14:58 16.39 17.1 2.71
5/29/2024 14:15:58 16.46 17.11 2.71
5/29/2024 14:16:58 16.48 17.12 2.71
5/29/2024 14:17:58 16.5 17.1 2.72
5/29/2024 14:18:58 16.51 17.08 2.73
5/29/2024 14:19:58 16.5 17.07 2.74
5/29/2024 14:20:58 16.65 17.06 2.74
5/29/2024 14:21:58 16.67 17.06 2.75
5/29/2024 14:22:58 16.82 17.06 2.75
5/29/2024 14:23:58 16.77 17.07 2.74 <point
5/29/2024 14:24:58 16.79 17.06 2.74
5/29/2024 14:25:58 16.73 17.07 2.73
5/29/2024 14:26:58 16.65 17.1 2.71
5/29/2024 14:27:58 16.48 17.12 2.71
5/29/2024 14:28:58 16.64 17.1 2.72
5/29/2024 14:29:58 16.53 17.09 2.72
5/29/2024 14:30:58 16.7 17.08 2.73
5/29/2024 14:31:58 16.68 17.05 2.75
5/29/2024 14:32:58 16.85 17.01 2.77
5/29/2024 14:33:58 17.09 17.01 2.78 <point
5/29/2024 14:34:58 17.19 17 2.78
5/29/2024 14:35:58 17.05 16.99 2.78
5/29/2024 14:36:58 17.19 16.99 2.78
5/29/2024 14:37:58 17.19 17.01 2.76
5/29/2024 14:38:58 17.09 17 2.77
5/29/2024 14:39:58 17.2 17 2.77
5/29/2024 14:40:58 17.25 17.02 2.77 «Computer Froze
5/29/2024 14:41:58 17.14 17.01 2.77
5/29/2024 14:43:58 16.98 17.01 2.78 <point
5/29/2024 14:47:58 17.18 17.01 2.77 «Computer Froze
5/29/2024 14:48:58 17.29 17.01 2.77
5/29/2024 14:49:58 17.05 17.02 2.77
5/29/2024 14:50:58 17.04 17.01 2.77
5/29/2024 14:51:58 17.01 17.02 2.76
5/29/2024 14:52:58 16.98 17.02 2.76
5/29/2024 14:53:58 17.01 17.02 2.76 <point
5/29/2024 14:54:58 16.97 17.02 2.76
5/29/2024 • 14:55:58 16.98 17.02 2.76
5/29/2024 14:56:58 16.91 17.01 2.77
5/29/2024 14:57:58 17.01 17 2.77
5/29/2024 14:58:58 17.19 16.99 2.78
5/29/2024 14:59:58 17 16.99 2.78
5/29/2024 15:00:58 17.04 17.01 2.76
5/29/2024 15:01:58 16.87 17.02 2.75
5/29/2024 15:02:58 16.9 17.04 2.75
5/29/2024 15:03:58 16.95 17.04 2.74 <point
5/29/2024 15:04:58 16.93 17.05 2.74
5/29/2024 15:05:58 16.81 17.03 2.75
5/29/2024 15:06:58 16.86 17.01 2.77
5/29/2024 15:07:58 16.99 17.02 2.76 NOxppm = 16.82
5/29/2024 15:08:58 17.11 17.01 2.76 02%= 17.05
5/29/2024 15:09:58 16.98 17.03 2.75 CO2%= 2.76
5/29/2024 15:10:58 16.97 17.05 2.75
5/29/2024 15:11:58 16.87 17.06 2.75
5/29/2024 15:12:58 16.8 17.03 2.76 <End Run
5/29/2024 15:13:58 15.15 12.55 2.04
5/29/2024 15:14:58 25.77 0.24 0.13
5/29/2024 15:15:58 25.31 0.06 0.11
5/29/2024 15:16:581 24.921 0.011 0.11
5/29/2024 15:17:58 15.22 5.62 5.58
5/29/2024
5/29/2024
5/29/2024
15:18:58 0.34 10.15 10.03
15:19:58 0.12 10.21 10.08
15:20:581~---o-.o-5~1 --1-0-.2-2 l~--10-.1---.1 I
Roll Mill Crusher #2
Inlet Opacity
Western Environmental Services and Testing, Inc.
Source Name
Address
City State Zip
Phone Source ID Number
Process Equipment Operating Mode
Control Equipment Operating Mode
Describe Emission Point
Height Above Ground Level JO.f.f Height Relative to Observer
Distance From Observer ':Jli/.f Direction From Observer
Describe Emissions
Start y.' ~ :6 /4
Emission Color
Start ,¥/,A Stop
Water Droplets Present
Yes D No 'lt.,
Plume Type -Continuous
Fugitive -lntennittent N:·
[f Water Droplet Plume
Attached D Detached D
2
3
4
5
6
7
8
9
11
12
13
[4
Point in the Plume at which opacity was determined 15
' ():J{p Stop Time
45
Start Stop ~-'/i"'-----!lt:;i!£.'..-------+-l-6 -+"-'«--1--l.4'-+-\;,l'--l+b!~l---+--='---+-"-+--'"'----+--'------l
Describe Background 1 7
Stai-t 18
Start k Stop f3 t l
Wind Speed, mph
Start s Sto J ~
Ambient Temp., "F
Start Stop ~o
Source Layout Sketch
Sun {} Wind ...._,
I
Plumeand ~
Stack v_
Stop
Wind Direction, degrees
Sta1i / J,0 Stop I ~Q
Wet Bulb Temp., °F RH percent
'37--
Draw North Arrow ~
X Emission Point
Observers Position
Sun Location Line
Comments
I have received a copy of these Opacity Observations
Signature
Title Date
19
20
21
22
23
24
25
26
27
28
29
30
Average Opacity For
Highest Period Q
Range of Opacity Readings
Minimum (!j
Observers Name (Print)
Organization:
Number of Readings Above
% Were Q
Maximum Q
Outlet Opacity
Western Environmental Services and Testing, Inc.
Source Name./.., LJ. ....r. ,/ JJ.;/r>.,,A,1,,-,'-/,,p __ ,A,_.. .. ,._,, I Observation Date5/J1/,J, Start Time ~19/i, Stop Time /0.3(.,.
Address 1(/Jt'-y--1/',,,_j --
.~ ~ 0 15 30 45 0 15 30 45 Mm n
I 0 '(;} (5) (j) 31 0 0 Ci) 0
City V,w,,.,,.,,J State llT Zip 2 0 (""11 n n 32 0 n 0 n,.
Phone Source ID Number 3 r., n n, I"}. 33 r.:, ~ 0 n
Process Equipment£, ;1,,,tl,,,, Operating Mode fl. 0 -
t 4 l',J a G' 34 0 ta ~ {?
Control Equipment Operating Mode 5 0 Q 0 6) 35 0 r, 0 Q
Describe Emission Point ('l ef ,✓ :/1.,Jawl-U 6 a r) 0 CJ 36 a n Al rJ
Height Above Ground Level ,f':tf Height Relative to Observer 10 .f,J 7 rJ> r) 0 ('} 37 0 n c> f"l
Distance From Observer rJ.1t.tJ Direction From Observer JV 8 r,) Q 0 CJ 38 0 ,:-> I? ,0 -
Describe Emissions 9 Q 0 0 0 39 a r, /? t9
Start /J/1/A Stop /V'/A-10 0 0 (2 r.) 40 n n 17 n.
Emission Color Plume Type -Continuous 11 G) a 0 0 41 0 0 0 n
Start # IA Stop Ai/A Fugitive -l'ntermittent 12 0 (") r> () 42 a 0 0 0 , -
Water Droplets Present lf Water Droplet Plume 13 {J 10 0 n 43 0 n C) /v
Yes D No 1J Attached □ Detached D 14 a .0 a () 44 0 0 n 0
Point in the Plu1:~_at wh'ch opacity was <let2·nni1: ~cl 15 Q 0 0 n 45 0 0 'I? t2
Start Jb,,,,J f) .-1/ __j Stop .. · , ,.~/2A,_/ .. 16 0 0 0 0 46 a n a 0 . .. . . -Describe Background 17 0 0 r:, n 47 ~ n n 0
Start (9 Jo..t, k.. /on1n.tA er Stop :JlL,1 k /_._ A• A A fill" 18 C') 0 0 0 48 0 0 0 ()
Background Color r Sky Conditions 19 (J) 0 10 10 49 0 D 0 0
Start 'lJ/o11,lc. Stop /?J,.,//r Start tf.t(),/ Stop t/,{/i.,,., 20 (j) 0 0 jC) 50 /) 0 0 /')
-·
Wind Speed, mph Wind Direction, degrees 21 0 C) 0 n 51 n 0 Ci) G>
5' .? -
Start Stop Start )':) 0 Stop /20 22 0 0 0 0 52 a Q 0 ·G y, 0 0 Q ID Ambient Temp., "F Wet Bulb Temp., °F RH percent 23 0 0 Q 53 Q
Start U, 7, Stop 7o 3? 24 0 0 (2,, 0 54 0 0 a ..(;)
Source Layout Sketch Draw North Arrow ® 25 0 0 0 n 55 () 0 0 0
26 0 0 Qi a 56 C> () /) a
27 0 0 G 0 57 n 0 a ·O
X Emission Point 28 ..A., n C) 0 58 Q 0 0 (l
29 0 0 0 0 59 0 0 0 0
Sun -6-Wind ...... 30 Q 0 0 .9 60 Q 0 0 e
I Observers Position Average Opacity For Number of Readings Above Plume and a: Highest Period G 0 Stack ~~ ¾ Were
Range of Opacity Readings
Sun Location Line ~ Minimum 0 Maximum 0
' Observers Name (Print)l;J3' cl. k
Comments . r "-(J,rt,,,' • /A4,n. , .,er---
Observer's Signatur,, ~
;' ~---_,,,.,..-i9atS"/~o/~J
I have received a copy of these Opacity Observations Organization: Western Environmental, Casper, Wyoming
Signature Cert•~·fi d By/'/-, f~, KJi j f,40, 'f>f'\ ,.<""> . ao Dat'lf /:;_1 't/"-</
IDat~ •
Verified'I5y Date
Title
APPENDIXC
Computer Data Entry
Particulate Run Sheets
Ramsey Hill Exploration, LLC Run: 1 Western Environmental
Vernal, Utah Sand Dryer #3 Particulate
Method: 5 Static Pressure: 0.54 In. H20 Meter No: 12
For Particulate Barometric: 24.22 In. Hg Meter Correction Factor: 0.978
Area: 1328.32 sq.in. Condensate Mass: 289.8grams Pilot Tube Cp: 0.837
Time/Point: 5.0 min. % CO2: 2.60 Probe Tip Diameter 0.279
Sample Time: 120.0 min. % 02: 16.99 Filter No: XT756
Date/Start Time 5/29/24 8:25 Date/Stop Time 5/29/24 10:30:00
Pretest Leak Rate 0.000 cfm@ 10.0 in.Hg Posttest Leak Rate 0.000 cfm@ 10.0 In.Hg
Clock Dry Gas Pilot Actual Stack D[Y Gas Meter Temg. Vol. ger
Point Time Meter (in. H2Ol llH Temg. Inlet Outlet Point
12 8:25:00 150.476 0,38 1.30 186 72 72 3.564
11 8:30:00 154.040 0.40 1.40 187 72 72 3.730
10 8:35:00 157.770 0.43 1.60 188 72 72 3.970
9 8:40:00 161.740 0.45 1.70 189 72 72 4.130
8 8:45:00 165.870 0.48 1.80 189 72 72 4,250
7 8:50:00 170.120 0.50 1.90 190 72 72 4.370
6 8:55:00 174.490 0.38 1.40 191 72 72 3.920
5 9:00:00 178.410 0.38 1.40 191 73 73 3.850
4 9:05:00 182.260 0.31 1.20 191 73 73 3.600
3 9:10:00 185.860 0.28 1.00 190 73 73 3.260
2 9:15:00 189.120 0.25 0.90 188 73 73 3.170
9:20:00 192.290 0.20 0.75 180 73 73 2.722
Stop 9:25:00 195.012
12 9:30:00 195.171 0.30 1.10 181 74 74 3.419
11 9:35:00 198.590 0.30 1.10 188 74 74 3.240
10 9:40:00 201.830 0.34 1.30 188 74 74 3.620
9 9:45:00 205.450 0.38 1.40 187 74 74 3.780
8 9:50:00 209.230 0.40 1.50 187 74 74 3.920
7 9:55:00 213.150 0.45 1.70 186 74 74 4.160
6 10:00:00 217.310 0.48 1.80 187 75 75 4.290
5 10:05:00 221.600 0.43 1.60 186 75 75 4.110
4 10:10:00 225.710 0.38 1.40 186 75 75 3.890
3 10:15:00 229.600 0.35 1.30 185 76 76 3,780
2 10:20:00 233.380 0.28 1.00 182 76 76 3.270
10:25:00 236.650 0.23 0.90 175 76 76 3.092
End 10:30:00 239.742
0.37 1.35 187 74 89.107
Ramsey Hill Exploration, LLC Run: 2 Western Environmental
Vernal, Utah Sand Dryer #3 Particulate
Method: 5 Static Pressure: 0.54 in. H20 Meter No: 12
For Particulate Barometric: 24.22 in. Hg Meter Correction Factor: 0.978
Area: 1328.32 sq.in. Condensate Mass: 277.9grams Pilot Tube Cp: 0.842
Time/Point: 5.0 min. % CO2: 2.70 Probe Tip Diameter 0.278
Sample Time: 120.0 min. % 02: 17.04 Filter No: XT755
Date/Start Time 5/29/24 10:52 Date/Stop Time 5/29/24 12:58
Pretest Leak Rate 0.001 cfm@ 10.0 in.Hg Posttest Leak Rate 0.001 cfm@ 10 in.Hg
Clock Dry Gas Pilot Actual Stack D!Y Gas Meter Tem12. Vol. 12er
Point Time Meter (in. H2O) LiH Tem12. Inlet Outlet Point
12 10:52:00 239.905 0.28 1.05 189 77 77 3.205
11 10:57:00 243.110 0.31 1.20 189 77 77 3.520
10 11 :02:00 246.630 0.34 1.30 190 77 77 3.640
9 11:07:00 250.270 0.34 1.30 190 77 77 3.680
8 11:12:00 253.950 0.40 1.50 190 78 78 3.930
7 11 :17:00 257.880 0.45 1.70 189 78 78 4.150
6 11 :22:00 262.030 0.48 1.80 189 78 78 4.310
5 11 :27:00 266.340 0.43 1.60 189 78 78 4.160
4 11 :32:00 270.500 0.40 1.50 188 78 78 4.050
3 11 :37:00 274.550 0.35 1.30 188 79 79 3.750
2 11 :42:00 278.300 0.30 1.10 187 79 79 3.610
1 11 :47:00 281.910 0.25 0.90 179 79 79 3.189
Stop 11 :52:00 285.099
12 11 :58:00 285.187 0.40 1.50 190 79 79 3.893
11 12:03:00 289.080 0.38 1.40 189 79 79 3.830
10 12:08:00 292.910 0.40 1.50 190 79 79 3.930
9 12:13:00 296.840 0.43 1.60 192 79 79 3.970
8 12:18:00 300.810 0.45 1.70 192 79 79 4.370
7 12:23:00 305.180 0.48 1.80 193 79 79 4.210
6 12:28:00 309.390 0.38 1.40 194 79 79 3.960
5 12:33:00 313.350 0.35 1.30 194 80 80 3.740
4 12:38:00 317.090 0.33 1.20 195 80 80 3.650
3 12:43:00 320.740 0.28 1.00 194 80 80 3.270
2 12:48:00 324.010 0.23 0.90 193 80 80 3.110
1 12:53:00 327.120 0.20 0.75 190 81 81 2.963
End 12:58:00 330.083
0.36 1.35 190 79 90.090
Ramsey Hill Exploration, LLC Run: 3 Western Environmental
Vernal, Utah Sand Dryer #3 Particulate
Method: 5 Static Pressure: 0.54 In. H20 Meter No: 12
For Particulate Barometric: 24.22 in. Hg Meter Correction Factor: 0.978
Area: 1328.32 sq.in. Condensate Mass: 277.8grams Pilot Tube Cp: 0.837
Time/Point: 5.0 min. % CO2: 2.69 Probe Tip Diameter 0.279
Sample Time: 120.0 min. % 02: 17.09 Filter No: XT757
Date/Start Time 5/29/24 13: 13 Date/Stop Time 5/29/24 15: 18
Pretest Leak Rate 0.000 cfm@ 10.0 in.Hg Postles! Leak Rate 0.000 cfm@ 10.0 in.Hg
Clock Dry Gas Pilot Actual Stack D!Y Gas Meter TemQ. Vol. Qer
Point Time Meter {in. H2O) I\H TemQ. Inlet Outlet Point
12 13:13:00 330.104 0.30 1.10 189 81 81 3.446
11 13:18:00 333.550 0.34 1.30 188 80 80 3.550
10 13:23:00 337.100 0.34 1.30 189 80 80 3.900
9 13:28:00 341.000 0.43 1.60 189 81 81 3.910
8 13:33:00 344.910 0.45 1.70 189 81 81 4.220
7 13:38:00 349.130 0.48 1.80 188 81 81 4.330
6 13:43:00 353.460 0.38 1.40 189 81 81 3.980
5 13:48:00 357.440 0.32 1.20 187 81 81 3.700
4 13:53:00 361.140 0.28 1.00 184 81 81 3.290
3 13:58:00 364.430 0.28 1.00 183 81 81 3.280
2 14:03:00 367.710 0.28 1.00 183 82 82 3.260
14:08:00 370.970 0.28 1.00 184 82 82 3.264
Stop 14:13:00 374.234
12 14:18:00 374.401 0.30 1.10 188 82 82 3.349
11 14:23:00 377.750 0.30 1.10 188 82 82 3.420
10 14:28:00 381.170 0.32 1.20 188 82 82 3.540
9 14:33:00 384.710 0.35 1.30 190 82 82 3.660
8 14:38:00 388.370 0.38 1.40 190 82 82 3.850
7 14:43:00 392.220 0.40 1.50 190 82 82 3.980
6 14:48:00 396.200 0.43 1.60 189 82 82 4.120
5 14:53:00 400.320 0.40 1.50 187 82 82 4.010
4 14:58:00 404.330 0.38 1.40 187 82 82 3.900
3 15:03:00 408.230 0.35 1.30 186 82 82 3.860
2 15:08:00 412.090 0.35 1.30 184 82 82 3.660
1 15:13:00 415.750 0.35 1.30 186 82 82 3.771
End 15:18:00 419.521
0.35 1.31 187 82 89.250
Opacity
Diyer#3
Ogaclt~ Calculations
OPACITY
Wednesday, May 29, 2024
8:25-9:25
Minute Seconds Average for period 0 15 30 45
1 0 0 0 0
2 0 0 0 0 0.00
3 0 0 0 0
4 0 0 0 0
5 0 0 0 0
6 0 0 0 0
2 7 0 0 0 0
8 0 0 0 0 0.00
9 0 0 0 0
10 0 0 0 0
11 0 0 0 0
12 0 0 0 0
3 13 0 0 0 0
14 0 0 0 0 0.00
15 0 0 0 0
16 0 0 0 0
17 0 0 0 0
18 0 0 0 0
4 19 0 0 0 0
20 0 0 0 0 0.00
21 0 0 0 0
22 0 0 0 0
23 0 0 0 0
24 0 0 0 0
5 25 0 0 0 0
26 0 0 0 0 0.63
27 0 0 0 0
28 0 0 0 5
29 0 5 0 0
30 5 0 0 0
6 31 0 5 0 0
32 0 0 0 0 0.21
33 0 0 0 0
34 0 0 0 0
35 0 0 0 0
36 0 0 0 0
7 37 0 0 0 0
38 0 0 0 0 0.00
39 0 0 0 0
40 0 0 0 0
41 0 0 0 0
42 0 0 0 0
8 43 0 0 0 0
44 0 0 5 0 0.21
45 0 0 0 0
46 0 0 0 0
47 0 0 0 0
48 0 0 0 0
9 49 0 0 0 0
50 5 0 0 0 0.63
51 5 5 0 0
52 0 0 0 0
53 0 0 0 0
54 0 0 0 0
10 55 0 0 0 0
56 0 0 5 0 0.21
57 0 0 0 0
58 0 0 0 0
59 0 0 0 0
60 0 0 0 0
0.19
Dr:yer#3
OQacity Calculations
OPACITY
Wednesday, May 29, 2024
11:10-12:10
Minute Seconds Average for period 0 15 30 45
1 0 0 0 5
2 0 0 0 0 0.21
3 0 0 0 0
4 0 0 0 0
5 0 0 0 0
6 0 0 0 0
2 7 0 0 0 0
8 0 0 0 0 0.25
9 0 0 0 0
10 5 0 0 0
11 0 0 0 0
12 0 0 0 0
3 13 0 0 0 0
14 0 0 0 0 0.42
15 0 0 0 0
16 0 0 0 5
17 0 0 0 0
18 0 0 5 0
4 19 0 0 0 0
20 0 0 0 0 0.00
21 0 0 0 0
22 0 0 0 0
23 0 0 0 0
24 0 0 0 0
5 25 0 0 0 0
26 0 0 0 0 0.00
27 0 0 0 0
28 0 0 0 0
29 0 0 0 0
30 0 0 0 0
6 31 0 0 0 0
32 5 5 0 0 0.42
33 0 0 0 0
34 0 0 0 0
35 0 0 0 0
36 0 0 0 0
7 37 0 0 0 0
38 0 0 5 0 0.21
39 0 0 0 0
40 0 0 0 0
41 0 0 0 0
42 0 0 0 0
8 43 0 0 0 0
44 0 0 0 0 0.00
45 0 0 0 0
46 0 0 0 0
47 0 0 0 0
48 0 0 0 0
9 49 0 0 0 0
50 0 0 0 0 0.21
51 0 0 0 0
52 0 0 0 5
53 0 0 0 0
54 0 0 0 0
10 55 0 0 0 0
56 0 0 0 0 0.21
57 0 5 0 0
58 0 0 0 0
59 0 0 0 0
60 0 0 0 0
0.19
DtYer#3
OQacity Calculations
OPACITY
Wednesday, May 29, 2024
13:14-14:14
Minute Seconds Average for period 0 15 30 45
1 0 0 0 0
2 0 0 0 0 0.00
3 0 0 0 0
4 0 0 0 0
5 0 0 0 0
6 0 0 0 0
2 7 0 0 0 0
8 0 0 0 0 0.00
9 0 0 0 0
10 0 0 0 0
11 0 0 0 0
12 0 0 0 0
3 13 0 0 0 0
14 0 0 0 0 0.00
15 0 0 0 0
16 0 0 0 0
17 0 0 0 0
18 0 0 0 0
4 19 0 0 0 0
20 0 0 0 0 0.00
21 0 0 0 0
22 0 0 0 0
23 0 0 0 0
24 0 0 0 0
5 25 0 0 0 0
26 0 0 0 0 0.21
27 0 0 0 0
28 0 0 0 0
29 0 5 0 0
30 0 0 0 0
6 31 0 0 0 0
32 0 0 0 0 0.00
33 0 0 0 0
34 0 0 0 0
35 0 0 0 0
36 0 0 0 0
7 37 0 0 0 0
38 0 0 0 0 0.00
39 0 0 0 0
40 0 0 0 0
41 0 0 0 0
42 0 0 0 0
8 43 0 0 0 0
44 0 0 0 0 0.00
45 0 0 0 0
46 0 0 0 0
47 0 0 0 0
48 0 0 0 0
9 49 0 0 0 0
50 0 0 0 0 0.00
51 0 0 0 0
52 0 0 0 0
53 0 0 0 0
54 0 0 0 0
10 55 0 0 0 0
56 0 5 0 0 0.21
57 0 0 0 0
58 0 0 0 0
59 0 0 0 0
60 0 0 0 0
0.04
CEMS
PLANT RHEx Vernal (ARC) METHOD 3A(O2)
SOURCE Dryer #3 ANALYZER MODEL CAIZRE
COMMENTS 24-1043 ANALYZER RANGE 0-20.4
DATE 05/29/24 CALIBRATION DATA FOR RUNS 1-3
OPERATOR T. Cordell
ANALYZER CALIBRATION DATA
ANALYZER CALIBRATION
CYLINDER CALIBRATION ERROR
CALIBRATION VALUE RESPONSE DIFFERENCE PERCENT
GAS (eem/%) (eem/%) (eem/%) OF SPAN
ZERO GAS: 0.00 -0.01 0.01 0.05%
HIGH RANGE: 20.40 20.39 -0.01 -0.05%
MID RANGE: 10.20 10.18 -0.02 -0.10%
LOW RANGE: N/A N/A N/A N/A
Calibration error must be less than +/-2%
Dilution System Serial Number: 3278 DIiution System Calibration Date: 07/17/23
CYLINDER
CALIBRATION VALUE CYLINDER CYLINDER EXPIRATION
GAS (eem/%) PRESSURE NUMBER DATE
REFERENCE
GAS: 20.40 800 EB0157262 09/18/31
ZERO GAS: 0.00 1400 N/A N/A
HIGH RANGE: 20.40 N/A N/A N/A
MID RANGE: 10.20 N/A N/A N/A
LOW RANGE: N/A N/A N/A N/A
PLANT RHEx Vernal (ARC)
SOURCE Dryer #3
COMMENTS 24-1043
DATE 05/29/24
SYSTEM BIAS AND DRIFT DETERMINATIONS
CALIBRATION
GAS
RUN: 1 ZERO
TIME: 08:25 -10:25
UPSCALE
RUN: 2 ZERO
TIME: 10:52 -12:52
UPSCALE
RUN: 3 ZERO
TIME: 13:13 • 15:13
UPSCALE
DRIFT
BIAS
METHOD 3A (02)
SPAN 0-20.4
OPERATOR T. Cordell
INITIAL VALUES FINAL VALUES
ANALYZER SYSTEM SYSTEM SYSTEM
CALIBRATION CALIBRATION CAL. BIAS CALIBRATION
RESPONSE RESPONSE % OF RESPONSE
(ppm/%) (ppm/%) SPAN (ppm/%)
-0.01 0.03 0.20% 0.02
10.18 10.21 0.15% 10.22
-0.01 0.02 0.15% 0.00
10.18 10.22 0.20% 10.14
-0.01 0.00 0.05% 0.01
10.18 10.14 -0.20% 10.22
SYSTEM FINAL BIAS -SYSTEM INITIAL BIAS
SPAN
Zero and upscale drift must be less than +/-3%
SYSTEM CAL. RESPONSE -ANALYZER CAL. RESPONSE
SPAN
Zero and upscale bias must be less than +/-5%
SYSTEM
CAL. BIAS DRIFT
%OF %OF
SPAN SPAN
0.15% -0.05%
0.20% 0.05%
0.05% -0.10%
-0.20% -0.39%
0.10% 0.05%
0.20% 0.39%
X 100
X 100
PLANT RHEx Vernal (ARC) METHOD 3A(O2)
SOURCE Dryer #3 SPAN 0-20.4
COMMENTS 24-1043 OPERATOR T. Cordell
DATE 05/29/24
EMISSION CALCULATIONS
~
Cgas ( C Co) X Cm Co
RUN NO. 10.20
TIME 08:25 • 10:25 Cgas 17.00 0.03 X 10.22 0.03
16.99 %02 (dry basis)
RUN NO. 2 10.20
TIME 10:52 • 12:52 Cgas 17.00 0.01 X 10.18 0.01
17.04 % 02 (dry basis)
RUN NO. 3 10.20
TIME 13:13 -15:13 Cgas 17.05 0.01 X 10.18 0.01
17.09 % 02 (dry basis)
Where Cgas Effluent gas concentration, dry basis, percent.
C Avg. concentration indicated by analyzer, dry basis, percent.
Co Avg. of the inilial and final calibration bias responses for the zero gas, percent.
Cm Avg of initial and final calibration responses for the upscale calibration gas, percent.
Cma Actual concentration of the upscale calibration gas, percent.
C 00009
PLANT RHEx Vernal (ARC) METHOD 3A(CO2)
SOURCE Dryer #3 ANALYZER MODEL CAI ZRE
COMMENTS 24-1043 ANALYZER RANGE 0-20.19
DATE 05/29/24 CALIBRATION DATA FOR RUNS 1-3
OPERATOR T. Cordell
ANALYZER CALIBRATION DATA
ANALYZER CALIBRATION
CYLINDER CALIBRATION ERROR
CALIBRATION VALUE RESPONSE DIFFERENCE PERCENT
GAS (eem/%) (eem/%) (eem/%) OF SPAN
ZERO GAS: 0.00 0.00 0.00 0.00%
HIGH RANGE: 20.19 20.20 0.01 0.05%
MID RANGE: 10.10 10.09 -0.01 -0.05%
LOW RANGE: N/A N/A N/A N/A
Calibration error must be less than +/-2%
Dilution System Serial Number: 3278 Dilution System Calibration Date: 07/17/23
CYLINDER
CALIBRATION VALUE CYLINDER CYLINDER EXPIRATION
GAS (eem/%) PRESSURE NUMBER DATE
REFERENCE
GAS: 20.19 800 EB0157262 09/18/31
ZERO GAS: 0.00 1400 N/A N/A
HIGH RANGE: 20.19 N/A N/A N/A
MID RANGE: 10.10 N/A N/A N/A
LOW RANGE: N/A N/A N/A N/A
PLANT RH Ex Vernal (ARC)
SOURCE Dryer #3
COMMENTS 24-1043
DATE 05/29/24
SYSTEM BIAS AND DRIFT DETERMINATIONS
CALIBRATION
GAS
RUN: 1 ZERO
TIME: 08:25 • 10:25
UPSCALE
RUN: 2 ZERO
TIME: 10:52 -12:52
UPSCALE
RUN: 3 ZERO
TIME: 13:13 -15:13
UPSCALE
DRIFT
BIAS
METHOD 3A (CO2)
SPAN 0-20.19
OPERATOR T. Cordell
INITIAL VALUES FINAL VALUES
ANALYZER SYSTEM SYSTEM SYSTEM
CALIBRATION CALIBRATION CAL. BIAS CALIBRATION
RESPONSE RESPONSE % OF RESPONSE
(ppm/%) (ppm/%) SPAN (ppm/%)
0.00 0.04 0.20% 0.11
10.09 10.10 0.05% 10.13
0.00 0.11 0.54% 0.11
10.09 10.13 0.20% 10.07
0.00 0.11 0.54% 0.10
10.09 10.07 -0.10% 10.11
SYSTEM FINAL BIAS -SYSTEM INITIAL BIAS
SPAN
Zero and upscale drift must be less than +/-3%
SYSTEM CAL. RESPONSE -ANALYZER CAL. RESPONSE
SPAN
Zero and upscale bias must be less than +/-5%
SYSTEM
CAL. BIAS DRIFT
%OF %OF
SPAN SPAN
0.54% 0.35%
0.20% 0.15%
0.54% 0.00%
-0.10% -0.30%
0.50% -0.05%
0.10% 0.20%
X 100
X 100
PLANT RH Ex Vernal (ARC) METHOD 3A(CO2)
SOURCE Dryer #3 SPAN 0-20.19
COMMENTS 24-1043 OPERATOR T. Cordell
DATE 05/29/24
EMISSION CALCULATIONS ~
Cgas (C Co ) X Cm Co
RUN NO. 1 10.10
TIME 08:25 -10:25 Cgas 2.66 0.08 X 10.12 0.08
2.60 % CO2 (dry basis)
RUN NO. 2 10.10
TIME 10:52 • 12:52 Cgas 2.78 0.11 X 10.10 0.11
2.70 % CO2 (dry basis)
RUN NO. 3 10.10
TIME 13:13 -15:13 Cgas 2.76 0.11 X 10.09 0.11
2.69 % CO2 (dry basis)
Where Cgas Effluent gas concentration, dry basis, percent.
C Avg. concentration indicated by analyzer, dry basis, percent.
Co Avg. of the initial and final calibration bias responses for the zero gas, percent.
Cm Avg of initial and final calibration responses for the upscale calibration gas, percent.
Cma Actual concentration of the upscale calibration gas, percent.
C 00012
PLANT RHEx Vernal (ARC)
SOURCE Dryer #3
COMMENTS 24-1043
DATE 05/29/24
ANALYZER CALIBRATION DATA
CYLINDER
CALIBRATION VALUE
GAS (ppm/%)
ZERO GAS: 0.00
HIGH RANGE: 50.00
MID RANGE: 25.00
LOW RANGE: N/A
ANALYZER
CALIBRATION
RESPONSE
(ppm/%)
0.12
50.02
25.03
N/A
METHOD 7E
ANALYZER MODEL API 200AH
ANALYZER RANGE 0-50
CALIBRATION DATA FOR RUNS 1-3
OPERATOR T. Cordell
CALIBRATION
ERROR
DIFFERENCE PERCENT
(ppm/%) OF SPAN
-0.12 -0.24%
0.02 0.04%
0.03 0.06%
N/A N/A
Calibration error must be less than +/. 2%
Dilution System Serial Number: 3278 Dilution System Calibration Date: 07/17/23
CYLINDER
CALIBRATION VALUE CYLINDER CYLINDER EXPIRATION
GAS (ppm/%) PRESSURE NUMBER DATE
REFERENCE
GAS: 502.70 800 CC339895 11/01/30
ZERO GAS: 0.00 1400 N/A N/A
HIGH RANGE: 50.00 N/A N/A N/A
MID RANGE: 25.00 N/A N/A N/A
LOW RANGE: N/A N/A N/A N/A
PLANT RH Ex Vernal (ARC)
SOURCE Dryer #3
COMMENTS 24-1043
DA TE 05/29/24
SYSTEM BIAS AND DRIFT DETERMINATIONS
CALIBRATION
GAS
RUN: 1 ZERO
TIME: 08:25 -10:25
UPSCALE
RUN: 2 ZERO
TIME: 10:52 -12:52
UPSCALE
RUN: 3 ZERO
TIME: 13:13 • 15:13
UPSCALE
DRIFT
BIAS
METHOD 7E
SPAN 0-50
OPERATOR T. Cordell
INITIAL VALUES FINAL VALUES
ANALYZER SYSTEM SYSTEM SYSTEM
CALIBRATION CALIBRATION CAL. BIAS CALIBRATION
RESPONSE RESPONSE %OF RESPONSE
(ppm/%) (ppm/%) SPAN (ppm/%)
0.12 0.03 -0.18% -0.04
25.03 25.00 -0.06% 24.89
0.12 -0.04 -0.32% 0.13
25.03 24.89 -0.28% 24.77
0.12 0.13 0.02% -0.05
25.03 24.77 -0.52% 24.92
SYSTEM FINAL BIAS· SYSTEM INITIAL BIAS
SPAN
Zero and upscale drift must be less than +/-3%
SYSTEM CAL. RESPONSE -ANALYZER CAL. RESPONSE
SPAN
Zero and upscale bias must be less than +/-5%
SYSTEM
CAL. BIAS DRIFT
%OF %OF
SPAN SPAN
-0.32% -0.14%
-0.28% -0.22%
0.02% 0.34%
-0.52% -0.24%
-0.34% -0.36%
-0.22% 0.30%
X 100
X 100
PLANT RHEx Vernal (ARC) METHOD 7E
SOURCE Dryer #3 SPAN 0-50
COMMENTS 24-1043 OPERATOR T. Cordell
DATE 05/29/24
EMISSION CALCULATIONS
____Q_o:@
Cgas ( C Co ) X Cm Co
RUN NO. 25.00
TIME 08:25 • 10:25 Cgas 16.33 -0.01 X 24.95 -0.01
16.37 ppm NOx (dry basis)
RUN NO. 2 25.00
TIME 10:52 -12:52 Cgas 16.99 0.05 X 24.83 0.05
17.09 ppm NOx (dry basis)
RUN NO. 3 25.00
TIME 13:13 -15:13 Cgas 16.82 0.04 X 24.85 0.04
16.91 ppm NOx (dry basis)
Where Cgas Effluent gas concentration, dry basis, ppm.
C Avg. concentration indicated by analyzer, dry basis, ppm.
Co Avg. of the initial and final calibration responses for the zero gas, ppm.
Cm Avg. of the initial and final calibration responses for the upscale calibration gas, ppm.
Cma Actual concentration of the upscale calibration gas, ppm.
C 00015
Roll Mill Crusher #2
Inlet Opacity
Crusher #2 Inlet
0Qacity Calculations
OPACITY
Wednesday, May 29, 2024
9:36-10:36
Minute Seconds Average for period 0 15 30 45
1 0 0 0 0
2 0 0 0 0 0.00
3 0 0 0 0
4 0 0 0 0
5 0 0 0 0
6 0 0 0 0
2 7 0 0 0 0
8 0 0 0 0 0.00
9 0 0 0 0
10 0 0 0 0
11 0 0 0 0
12 0 0 0 0
3 13 0 0 0 0
14 0 0 0 0 0.00
15 0 0 0 0
16 0 0 0 0
17 0 0 0 0
18 0 0 0 0
4 19 0 0 0 0
20 0 0 0 0 0.00
21 0 0 0 0
22 0 0 0 0
23 0 0 0 0
24 0 0 0 0
5 25 0 0 0 0
26 0 0 0 0 0.00
27 0 0 0 0
28 0 0 0 0
29 0 0 0 0
30 0 0 0 0
6 31 0 0 0 0
32 0 0 0 0 0.00
33 0 0 0 0
34 0 0 0 0
35 0 0 0 0
36 0 0 0 0
7 37 0 0 0 0
38 0 0 0 0 0.00
39 0 0 0 0
40 0 0 0 0
41 0 0 0 0
42 0 0 0 0
8 43 0 0 0 0
44 0 0 0 0 0.00
45 0 0 0 0
46 0 0 0 0
47 0 0 0 0
48 0 0 0 0
9 49 0 0 0 0
50 0 0 0 0 0.00
51 0 0 0 0
52 0 0 0 0
53 0 0 0 0
54 0 0 0 0
10 55 0 0 0 0
56 0 0 0 0 0.00
57 0 0 0 0
58 0 0 0 0
59 0 0 0 0
60 0 0 0 0
Outlet Opacity
Crusher #2 Outlet
Ogacity Calculations
OPACITY
Wednesday, May 29, 2024
9:36-10:36
Minute Seconds Average for period 0 15 30 45
1 0 0 0 0
2 0 0 0 0 0.00
3 0 0 0 0
4 0 0 0 0
5 0 0 0 0
6 0 0 0 0
2 7 0 0 0 0
8 0 0 0 0 0.00
9 0 0 0 0
10 0 0 0 0
11 0 0 0 0
12 0 0 0 0
3 13 0 0 0 0
14 0 0 0 0 0.00
15 0 0 0 0
16 0 0 0 0
17 0 0 0 0
18 0 0 0 0
4 19 0 0 0 0
20 0 0 0 0 0.00
21 0 0 0 0
22 0 0 0 0
23 0 0 0 0
24 0 0 0 0
5 25 0 0 0 0
26 0 0 0 0 0.00
27 0 0 0 0
28 0 0 0 0
29 0 0 0 0
30 0 0 0 0
6 31 0 0 0 0
32 0 0 0 0 0.00
33 0 0 0 0
34 0 0 0 0
35 0 0 0 0
36 0 0 0 0
7 37 0 0 0 0
38 0 0 0 0 0.00
39 0 0 0 0
40 0 0 0 0
41 0 0 0 0
42 0 0 0 0
8 43 0 0 0 0
44 0 0 0 0 0.00
45 0 0 0 0
46 0 0 0 0
47 0 0 0 0
48 0 0 0 0
9 49 0 0 0 0
50 0 0 0 0 0.00
51 0 0 0 0
52 0 0 0 0
53 0 0 0 0
54 0 0 0 0
10 55 0 0 0 0
56 0 0 0 0 0.00
57 0 0 0 0
58 0 0 0 0
59 0 0 0 0
60 0 0 0 0
APPENDIXD
Analytical Data
Ramsey Hill Exploration, LLC Western Environmental
Vernal, Utah Sand Dryer #3 Particulate
Particulate Weights
Run Number: 1 .6 ~
5/29/2024 8:25 5/29/2024 10:52 5/29/2024 13: 13
5/29/2024 10:30 5/29/2024 12:58 5/29/2024 15:18
Filter No: XT756 XT755 XT757
Final Weight 0.4272 g 0.4262 g 0.4294 g
Initial Weight 0.4246 g 0.4193 g 0.4244 g
Net Gain 2.60 mg 6.90 mg 5.00 mg
Acetone: Blank
Volume 125 ml 125 ml 125 ml 125 ml
Final Weight 115.3353 g 108.0848 g 108.9029 g 104.2286 g
Initial Weight 115.3346 g 108.0766 g 108.8955 g 104.2246 g
Correction Factor * 5.60 mg/I 0.70 mg 0.70 mg 0.70 mg
Corrected Net Gain 7.50 mg 6.70 mg 3.30 mg
Total Front Half Weight -mn 10.10 mg 13.60 mg 8.30 mg
* Maximum Allowable Correction factor= 8 mg/I
Filter PM Analysis
Job Number: 24-1043 Run Date 5/29/2024
Client Name: Ramsey Hill
Unit Name: Dryer #3 Method: 5
RUN 1 BEAKER# XT756 COLOR Tan Rings AVERAGE
Filter + Particulate (g) 0.4272 0.4272 0.4272
Filter Tare (g) 0.4246 0.4245 0.4246
Particulate Weight (g) 0.0026 0.0027 0.0026
RUN 2 BEAKER# XT755 COLOR Tan Rings AVERAGE
Filter+ Particulate (g) 0.4262 0.4262 0.4262
Filter Tare (g) 0.4193 0.4193 0.4193
Particulate Weight (g) 0.0069 0.0069 0.0069
RUN 3 BEAKER# XT757 COLOR Tan Rings AVERAGE
Filter + Particulate (g) 0.4294 0.4294 0.4294
Filter Tare (g) 0.4244 0.4244 0.4244
Particulate Weight (g) 0.0050 0.0050 0.0050
BLANK BEAKER# XT758 COLOR White AVERAGE
Filter+ Particulate (g) 0.4225 0.4225 0.4225
Filter Tare (g) 0.4228 0.4228 0.4228
Particulate Weight (g) -0 .0003 -0.0003 -0 .0003
Analyst: JM FINAL REPORT Started: 6/7/2024
Completed: 6/14/2024
0:000.02
Acetone PM Analysis
Job Number: 24-1043 Run Date 5/29/2024
Client Name: Ramsey Hill
Unit Name: Dryer #3 Method: 5
RUN 1 BEAKER# D8015 VOLUME 125 ml AVERAGE
Beaker+ Particulate (g) 108.0846 108.0849 108.0848
Beaker Tare (g) 108.0765 108.0767 108.0766
Particulate Weight (g) 0.0081 0.0082 0.0082
RUN 2 BEAKER# D8016 VOLUME 125 ml AVERAGE
Beaker+ Particulate (g) 108.9028 108.9029 108.9029
Beaker Tare (g) 108.8954 108.8956 108.8955
Particulate Weight (g) 0.0074 0.0073 0.0074
RUN 3 BEAKER# D8017 VOLUME 125 ml AVERAGE
Beaker+ Particulate (g) 104.2287 104.2285 104.2286
Beaker Tare (g) 104.2244 104.2247 104.2246
Particulate Weight (g) 0.0043 0.0038 0.0040
BLANK BEAKER# D8018 VOLUME 125 ml AVERAGE
Beaker+ Particulate (g) 115.3352 115.3354 115.3353
Beaker Tare (g) 115.3344 115.3348 115.3346
Particulate Weight (g) 0.0008 0.0006 0.0007
Analyst: JM FINAL REPORT Started: 6/7/2024
Completed: 6/14/2024
[):00003
APPENDIXE
Chain of Custody
• WESTERN ENVIRONMENT AL SERVICES AND TESTING, INC.
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~ CHAIN OF CUSTODY RECORD
PROJECTNO.: cit.\-\DL\""5 CONT1CTNA!:!1E ~,C Li!)Ct:"Q,Jy\ TELEPHONENO. 607 2,S9 &7}0
Recovered By: Print Name
Si~/}/'
f
ii/I/Ill ;.J ,Hr (!Ar~_\\
l RE'COVERY / S
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m .;
SAMPLE ID SAMPLE LOCATION C:
z 0~ ::, .c: REMARKS a: DATE TIME 00 FILTER# zo
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COMMENTS:
-
ri, [Fei7nquish~igj,ture) / I .A I Company r ,,-__-, I Date !Time I Rer~bf:~tu~ ~ lco~y..J.--I Date ITime
~I II Relinquishe4·b/(Signatu~) / I company !Date ITlme ~eived by: (Signature) !company I Date ITime
CS) s II Dispatched by: (Signature) !Company I Date ITime I Received for Laboratory by: I Company I Date I Time cg
&,-.;:;. 11 Method of Shipment:
WHITE COPY-WEST YELLOW COPY---{;USTOMER PINK COPY---{;OPY M00953 7/06
Appendix F
Calibration of Equipment
Dry Gas Meters
WESTERN ENVIRONMENTAL SERVICES AND TESTING INC.
METER BOX CALIBRATION FORM
Meter Box Num: 12 Average DGM Y =
Delta H@=
0.978 Tech: BW
Pb= 24.42 1.713 Date: 3/26/2024
Orifice 1.0.= BT 48 K1= 0.3478 Orifice 1.0.= BT55 K1= 0.4646
1 2 1 2
DGM Final 11.155 992.462 997.887 1001.135
Initial 8.858 990.175 994.822 998.072
Vm 2.297 2.287 3.065 3.063
Temp In/Out I 60 I 60 I 58 I 58 I 58 I 59 I 59 I 59
Avg. Tm 0R/°F 520 60 518 58 519 59 519 59
Delta H 0.50 0.50 0.92 0.92
Time: 5 0.15 5.003 5 0.03 5.001 5 0.44 5.007 5 0.04 5.001
Orifice Temp. 58 58 62 59
Vacuum "Hg 18.5 18.5 18.0 18.0
Vm (std) 1.907 1.906 2.555 2.551
Ver (std) 1.867 1.866 2.487 2.490
DGMCFY 0.979 0.979 0.973 0.976
Delta H@ 1.681 1.687 1.756 1.744
Orifice 1.0.= BT 63 K1= 0.5850 598.995
1 2 Orifice I.D.= BT48
DGM Final 4.996 8.840 DGMCFY= 0.979 Difference= -0.060%
Initial 1.164 4.996 Avg. Vm (std)= 1.906
Vm 3.832 3.844 Difference (1 )= -0.025% (2)= 0.025%
Temp In/Out I 59 I 59 I 59 I 60
Avg. Tm 0R/°F 519 59 520 60 Orifice I.D.= BT55
Delta H 1.45 1.40 DGMCFY= 0.975 Difference= 0.379%
Time: 5 0.21 5.004 5 0.22 5.004 Avg. Vm (std)= 2.553
Orifice Temp. 58 58 Difference (1 )= -0.081% (2)= 0.081%
Vacuum "Hg 17.0 17.0
Vm (std) 3.196 3.203 Orifice I.D.= BT 63
Ver (std) 3.141 3.141 DGMCFY= 0.982 Difference= -0.319%
DGMCFY 0.983 0.981 Avg. Vm (std)= 3.199
Delta H@ 1.736 1.674 Difference (1 )= 0.101% (2)= -0.101%
*Results comply with Method 5 calibration standards where: DGMCF differences are less than +/-2.0%
and average Vm (std) differences are less than +/-0.5%.
WESTERN ENVIRONMENTAL SERVICES AND TESTING INC.
POSTTEST METER BOX CALIBRATION FORM
Meter Box Number: / 2. Average DGM Y = O,q7g
Pb= z4,g5
Pretest Calibration: 0. Gf1 '8
Orifice I.D.=: ig755"
1
DGM Final l/61.8/'1/
Initial II lf{i>4. 101
Vm 3.!/q-
Delta H @ = I. 7 / g
% Difference =
K1= o. '1Gl/G
2
u70. qB6
II l/61aJli
·s./ I~
Temp In/Out -I 78 I -17~ -1"7~1-l7g -
Avg. Tm 0RfF $'133 I ~::?51
Delta H o.q> o.q5'
3
Tech: P. ~obi£:on
Date: -S / -3 / /7-0 zj,,/
Job# 2£1' /Ot-/8
y74.os3
11 '-·J?O. q 8t6
:3. / 1:;
17? I -I 7g,
c;g'.3 I
o.Y!S
Time: 1,:drJr df I 5:o<l:oq I s:0C1f oq I
Orifice Temp. 7/ 7/ 7'2
Vacuum "Hg /7.0 17. O /?.O
Vm (std) '2-,.,~72-Z .5)f!, Z.S72
Ver (std) '2..t;;CIS 2. ,;05" 2.<S0:3
DGMCFY o.q7lf o. 0nq a. q73
Delta H@
%Difference
*Post test calibration must be within +/-5% of the Pre Test calibration
Thermocouples
THERMOCOUPLE CALIBRATION SHEET
Meter Box No : 12 Tech: BW Date: 3/27/2024
Reference: Omega Calibrator CL3512A
Reference Thermometer Thermocou12le % Difference
Source: OF OR OF OR OR
Meter In:
Ice Bath
Boiling Water
Hot Oil
Meter Out:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 212 672 0.00
Hot Oil 420 880 417 877 0.34
Probe:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 212 672 0.00
Hot Oil 420 880 417 877 0.34
Stack:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 212 672 0.00
Hot Oil 420 880 417 877 0.34
Oven:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 211 671 0.15
Hot Oil 420 880 416 876 0.45
Exit:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 212 672 0.00
Hot Oil 420 880 417 877 0.34
Auxiliary:
Ice Bath 32 492 32 492 0.00
Boiling Water 212 672 212 672 0.00
Hot Oil 420 880 416 876 0.45
Pitot Tubes
I
I
WESTERN ENVIRONMENTAL
PITOT TUBE CALIBRATION
A-9 High side calibration factor 0.837 Pitot Tube ID No.
Performed by:
-----
TS Low side calibration factor : 0.841
Calibration Date: 3/25/2024 Comments: 4' w/ probe _ __,_ _____ _
A-Side Calibration {high side}
~Pstd' ~Ps' Cp (St
(in.) (in.)
H20 H20
0.480 0.680 0.839
0.480 0.690 0.833
0.480 0.680 0.839
Average (Cp') 0.837
B-Side Calibration {low side}
~Pstd' ~Ps'
(in.) (in.)
H20 H20
0.490 0.690
0.490 0.690
0.480 0.680
Average (Cp')
Cp (S)° = Cp(std),JMstd
Ms
Dev.b = Cp (S)8-Cp' (must be~ 0.01)
Cp (S)8
0.842
0.842
0.839
0.841
Cp' (A) -Cp' (8) = (0.004) (must be .'.S..,0.01) ------"----'---
Temperature (°F) :
Humidity(%) :
Date:
Cp (std)* :
I Dev.u
0.002
-0.004
0.002
I
Dev.b
0.001
0.001
-0.002
61
25
3/25/2024
0.999
Cp' (A) = 0.837 Cp' (8) = 0.841 Standard Pitot No. : 3
*Cp (std) obtained from Dwyer Instruments air velocity calculator.
Calibrations were done in accordance with CFR Title 40, Part 60, Appendix A, July 1, 1994.
I
I
WESTERN ENVIRONMENTAL
PITOT TUBE CALIBRATION
Pitot Tube ID No. : B-14 0.842 ------High side calibration factor : ------
Performed by: TS Low side calibration factor : 0.841 ------
Calibration Date : 4/4/2024 Comments: 4' w/ probe _ __._ ______ _ ------
A-Side Calibration {high side}
LlPstd' LlPs' Cp (S)"
(In.) (in.)
H2O H20
0.530 0.730 0.851
0.520 0.740 0.837
0.520 0.740 0.837
Average (Cp') 0.842
B-Side Calibration {low side}
LlPstd' LlPs'
(in.) (in.)
H2O H20
0.520 0.740
0.520 0.730
0.520 0.730
Average (Cp')
Cp (SY = Cp(std).J Mstd Ms
Dev.b = Cp (S)8 -Cp' (must be .'.S 0.01)
Cp (S)8
0.837
0.843
0.843
0.841
Cp' (A) -Cp' (B) = 0.001 (must be ~0.01) ------
Temperature (°F) :
Humidity(%) :
Date:
Cp (std)*:
I
Dev.u
0.009
-0.005
-0.005
I
Dev.0
-0.004
0.002
0.002
67
23
3/10/2023
0.999
Cp' (A)= 0.842 Cp' (B) = 0.841 Standard Pitot No. : 3
*Cp (std) obtained from Dwyer Instruments air velocity calculator.
Calibrations were done in accordance with CFR Title 40, Part 60, Appendix A, July 1, 1994.
Nozzles
WESTERN ENVIRONMENTAL SERVICES AND TESTING, INC.
NOZZLE CALIBRATION DATA
Date: 3/10/2024
Technician: PR
Page: of 1
0.212
/
0.212 Difference: 0.002
Nozzle ID#:
0.214 (low) .{b_jg_b_)
U-1 Random: 0.212 0.214
0.214 Average: 0.213
0.279
/
0.280 Difference: 0.002
Nozzle ID#:
0.278 (low) .(b1gh}
U-2 Random: 0.278 0.280
0.280 Average: 0.279
0.308
Nozzle ID#: /
0,307 Difference: 0.002
U-3
0.309 (low) .(b1gh}
Random: 0.307 0.309
0.307 Average: 0.308
The difference between the high and low must be within 0.004 inches.
WESTERN ENVIRONMENTAL SERVICES AND TESTING, INC.
NOZZLE CALIBRATION DATA
Date: 3/10/2024
Technician: BW
Page: 1 of 1
0.214
/
0.214 Difference: 0.002
Nozzle ID#:
0.215 (low) !bl9h)
V-1 Random: 0.213 0.215
0.213 Average: 0.214
0.277
/
0.278 Difference: 0.002
Nozzle ID#:
0.277 (low) !bl9h)
V-2 Random: 0.277 0.279
0.279 Average: 0.278
0.341
Nozzle ID#: /
0,341 Difference: 0.002
V-3
0.340 {low) !bl9h)
Random: 0.340 0.342
0.342 Average: 0.341
The difference between the high and low must be within 0.004 inches.
Opacity Certifications
i1
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~f _r-=~I t !!!!'!!!)~:_ __ ~-...'.
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This is to certify that
fuwfYldor/ iJ~~-
did complete a course in the opacity method of determining visible
emission from sources as specified by Federal Reference Method "9"
conducted by Singleton Smoke School of Tennessee.
rF·· 1,1 y;<', b\:'✓;:,,},,J ~~~) }
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Protocol Gas Certifications
Airgas®
an Air Liquide company
Part Number:
Cylinder Number:
Laboratory:
Analysis Date:
Lot Number:
Ah-gas Intcrmountain region
Airgas USA LLC
29550 Highway 96 East
Pueblo, CO 81001
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: CERTIFIED STANDARD-SPEC
X02Nl90C15A3081
EB0165775
104 -Pueblo/East (SAP) -CO
Feb 27, 2024
96-402981 053-1
Expiration Date: Feb 27, 2032
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
96-402981053-1
146.0 CF
2016 PSIG
690
Product composition verified by dlrec.t comparison to _calibration standards traceable to N.l.S,T. weights and/or N'.I.S.T,
Gas Mixture reference materials.
Component
OXYGEN
NITROGEN
Req Cone
10,00 %
Balanoe
ANALYTICAL RESULTS
Actual Concentration
(Mole%)
10,09 %
:~ Approved for Release
Analytical
Uncertainty
+/-2%
Page 1 of 1
an Air Liquide company
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
Airgas Specialty Gases
Airgas USA LLC
525 North Industrial Loop Road
Tooele, UT 84074
Airgas.com
CERTIFICATE OF ANALYSIS
Grade of Product: EPA PROTOCOL STANDARD
E02Al99E15W0048
CC510998
124 -Tooele (SAP) -UT
B72024
NO2,BALA
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
Mar 21 2027
153-402981054-1
146.0 CF
2015 PSIG
660
Mar 21, 2024
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
uncertainly as stated below wilh a confidence level of 95%. There are no significant Impurities which affect the use of this callbrallon mixture. All concentrations are on a
mole/mole basis unless ol~erwlse noted"-T):le results re[?Je only lo tlltl'l.ms tested. The repoJI shall nol be reproduced except in full without approval of the laboratory. Do
Nol Use This Cylinder below 100 pslg, i.e. 0.7 megapascals.
ANALYTICAL RESULTS
Component Requested Actual Protocol Total Relative Assay
Concentration Concentration Method Uncertainty Dates
NITROGEN DIOXIDE 35.00 PPM 36.31 PPM G1 +/-2.0% NIST Traceable 03/14/2024, 03/21/2024
AIR Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
GMIS 1534022022406 CC517972 30.86 PPM NITROGEN DIOXIDE/NITROGEN 1.6% Feb 17, 2026
PRM 12409 D913660 15.01 PPM NITROGEN DIOXIDE/AIR 1.5% Feb 17, 2023
The SRM, NTRM. PRM, or RGM noted above is only in reference to the GMIS used In the assay and not part of the analysis.
ANALYTICAL EQUIPMENT
Instrument/Make/Model Analytical Principle Last Multipoint Calibration
MKS FTIR N02 018143349 FTIR Mar 13, 2024
Triad Data Available Upon Request
Approved for Release Page 1 of 1
F 00010
Ah•g11s S't\e!ilfolty Onsc.s
Airgn1,. tJ#J\ f,LC •
5a5 North ltt1hu;trl(tl !..Mp Rond
'foocTQ, tt(8it074·
.Airy,mWl(!l
CERTIFICATE OF.ANALYSIS
P~rtNumber:
Cy Under Number:
La~.PfaJ~ryi ' PGVP Number:
Gai:i Cgge;
. . .. ,. : ----' ,,
Grade.of Product: EPA PROTOCOL STA.NPARD --·. -,--=·-·· __ ,_.. -. ·. -'. --, .. -_._,_ .... -'.
e:.o3N1aoe16Ao2aa ~eterenee Nµml;ler:
f;B01S7262 . ..·. .• Cylinder\lolume!
jg4.:. Tohele ($AP)., UT cyUnder Pr(!lssure: 872023 ', " , Yalve·Outlijf: •.•
902i0~.BAL,N certiiltatlon t:fate:
.l:l<l)il'ation· Date: sap 1·8(2031
153w4028433.78•1
1S9,;(;, Of
2cf1s PSiG.
59Q, .•.. ·., .. ·,, Sep 181 2023
peiliifcatrpn,poJ1qr11 • or~ii!)0,01',1/[~ ".EPATmcout,i)!ty P,r,9tQgji.[Q(,A$Sfl'f a,n,cl<;)(lt)JQ~tiong( l38$~0U!i'<:;allbratroh' SUlndar~li(fvlilfW12)' di)CU)\Wi/lt.~f>A ..
. ·.·.·. .·· . pr(i,\'l,:J/JJ,/IOli 1/~r~d. AnalyIic~I ,Met~'¢doI9.gy~Qpfn.~t.rii:qt!lrl¼ ciirr~Gilpn !otii11,alytl~!!l lh\!iJf/lten.p_1Y\ ThYs.◊Wln(ler l)@SJ1JQlal ar1111yt1cal uncortaln , . . .. . conQdeMe ltiyeLof,9~%.'Tllere' ?re r,o sJg(IIOcanumplJcltles whlch .. a.ffo.et,.thl.➔.use. ot,11\rs eall!lra,t]Qn mlxt\Jr~. AJL¢qri:!lt1lra11qn~i•r.e.pri ~ .
molu/ml)l<1 l)~$IS µnle.$~J))lt/lr1YIS!l, l)O!!l~, .The re.suits rel~l/J.(/nly IO,lh/lll(m1$ JO&led; TM repott~hiiil(n<:il~e f!lP(C)(hJce<J .e~CQPl lnf~UWl\[1¢Ut 11pproval 61 the lal:ioratoty, Do • • • •• •• • · " • •• • ·:" • •• ;,.; •• • • Not Use,;Thls'Cyllni:lar belovi 100 pslg,J:e/Q,7 megapolical,t. . .' :· •. •• • •• • • •
ty!~~ QIOX\bE
NITROGEN
Type
NTRM
J\(f'RM
Lotto.
13060802
09061434
Reqµested
. .CoMentratlon
2d,OQ°4.
2.Q,Ori¾:
·Biili1nce
CyllniforNo
CQ4l539t·
00282492
Actual
CoMentratlon
:20;19%
2Q)N% · •
Protocol
Method
G1
.(31
CALlllltAl'ION StA:NPARPS
Qoncentratlot:i •
. ·• 24.04 .% ,QARBQN,PIOXID!=/NiTRJ:lGEN
22.li3 %. QXY.GgN/NITROGEN
ANAtYrICA:i:, EQtJIPM'.ENT
tofal Rela.tlve
Unc~rfah:ify
+l• o:a% NtSTftaceiHite .·
+/, 0,6% NIST Trai:(iable
IJhcertah:ity
·9A<il
OA%
Assjiy
Q~tes;
b9il8l2023 riMtaiidi~
Plff1., 8Q~ir Mayf :\, 2!l~ti
lhslrvirl,eht/M.akq/Model, Ar.-alytlc~l lfrln1;!i;l1~· , C.a!ifMu!tlppJ\;ltCafibratir>rt' .• :,..;; ........................................ """"----------............ ~"""''~--.-------.................. ~,;,,,;,,;; ............................. -----= H9.nt,i~V1A,~~ro.~Y4t,,1,EYW c.p~ co2 NDIR (OJxoh) Aug 2a, 2020
Homia MPA;.61PW(l03°MM5/t02 b2,F!ai:am:a?iit$HcC(Ol)(ON) ,·, . Ali~,23, 2023
Triad Data Available l,Jpcm ~eq1,1e$t
Airgas$
an Air Liquide company
CERTIFICATE OF ANALYSIS
Afrgas Specialty Gases
Airgas USA I.LC
525 North Industrial Loop Road
Tooele, UT 84074
Airgas.com
Grade of Product: EPA PROTOCOL STANDARD
Part Number:
Cylinder Number:
Laboratory:
PGVP Number:
Gas Code:
E02Nl99E15A0919
CC339895
124 -Tooele (SAP) -UT
872022
NO,NOX,BALN
Expiration Date:
Reference Number:
Cylinder Volume:
Cylinder Pressure:
Valve Outlet:
Certification Date:
. Nov 01 2030
153-40257 4359-1
144.0 CF
2016 PSIG
660
Nov 01, 2022
Certification performed In accordance with "EPA Traceability Protocol for Assay and Certification of Gaseous Calibration Standards (May 2012)" document EPA
600/R-12/631, using Iha assay procedures listed, Analyllcal Methodology does not require correction for.analytical Interference. This cylinder has a total analytical
uncertainty as stated below with a confidence level of 96%. There are no significant Impurities which affect the use of this c_allbratlon 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, Po
Not Use This Cylinder below 100 pslg, l,e, 0,7 megapasoals,
... ANALYTICAL RESULTS .. . ..
Component Requested Actual Protocol Total Relative Assay
Concentration • Concentration Method Uncertainty Dates
NOX 500.0 PPM 502,7 PPM G1 +/-0.7% NIST Traceable 10/25/2022, 11/01/2022
NITRIC OXIDE 600,0 PPM 502,7 PPM G1 +/. 0,7% NIST Traceable 10/26/2022, 11/01/2022
NITROGEN Balance
CALIBRATION STANDARDS
Type Lot ID Cylinder No Concentration Uncertainty Expiration Date
NrRM 15010116 KAL003474 494,6 PPM NITRIC OXIDE/NITROGEN 0.6% Aug 16, 2027
PRM 12409 D913660 15,01 PPM NITROGEN DIOXIDE/AIR 1.5% Feb 17, 2023
GMIS 1534012021103 ND73012 4.956 PPM NITROGEN DIOXIDE/NITROGEN 1.6% Jun 15, 202'6
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 1S50 AUP2110269 NO MNO FTIR Oct 12, 2022
Nicolet 1S50 AUP2110269 NO2 Impurity FTIR NO2 Impurity Oct 12, 2022
Triad Data Available Upon Request
Page 1 of 1
N02 Converter Check
Western Environmental Service and Testing, Inc.
NOx Analyzer Converter Efficiency Test Sheet
Date of Test: 5/29/2024
Analyzer Serial Number: 349
Zero Gas: N2
Zero Gas Analyzer Response: 0.12
NO High Gas Concentration (ppm): 50.00
High Gas Analyzer Resonse: 50.02
NO Mid Gas Concentration (ppm): 25.00
Mid Gas Analyzer Response: 25.03
NO2 Gas Concentration (ppm): 36.31
Cylinder Number: CC510998
Cylinder Pressure: 2,000
Cylinder Expiration Date: 3/21/2027
Average NO2 Gas Analyzer Response: 35.09
Converter Efficiency: 96.64%
NO2 response should be an average of five one minute points.
efficiency = NO2 response/actual NO2 concentration x 100
Dilution System Certifications
I
Unit Summary
Model #: 4040
Unit SN : 3278
69 Industrial Park Rd E, Tolland CT 06084
https://www.environics.com/service-request
(860) 872-11 11 [e-mail]
ENVIRONICS FLOW CONTROLLER CALIBRATION REPORT
Std Conditions MFC Summary
Temp: 32°F MFC#: 1
Pressure: 29 .92 in. Hg MFC FS Flow: 15000
Gas: NITROGEN MFC S/N: 2009500001
Flow Calibration Data is not performance data. This data is used by the system operating mode to improve the flow accuracy. The Flow
Verification Data is performance data.
5%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
99%
85%
55%
25%
10%
Flow Calibration Data
Set Flow True Flow
750 770.867
1500 1600.185
3000 3161 .258
4500 4700.777
6000 6162.138
7500 7768 005
9000 9280.574
10500 10707.248
12000 12274.81 1
13500 13833.736
15000 15449.002
All values in SCCM
Flow Verification Data
Set Flow True Flow
14850 14879.611
12750 12791 .648
8250 8242.896
3750 3748.196
1500 1506.507
All values 1n SCCM
% dev
0.20%
0.33%
-0.09%
-0.05%
0.43%
This calibration complies with ISO 17025-2005 [non-accredited] and is traceable to the National Institute of Standards and Technology (NIST). Calibration and verification
are accomplished exclusively by qualified personnel following controlled procedures under ISO 9001:2015. For questions or concerns, contact Customer Service via our
website, email or by phone, weekdays from BAM -4PM.
Verified by: ___ .....7-+-'C~#~=-----Date:
F 000:14
I
Unit Summary
Model #: 4040
Unit SN : 3278
69 Industrial Park Rd E, Tolland CT 06084
https://www.environics.com/service-request
[phone] [e-mail]
ENVIRONICS FLOW CONTROLLER CALIBRATION REPORT
Std Conditions MFC Summary
Temp: 32°F MFC#: 2
Pressure: 29.92 in. Hg MFC FS Flow: 15000
Gas: NITROGEN MFC S/N: 2009500002
Flow Calibration Data is not performance data. This data is used by the system operating mode to improve the flow accuracy. The Flow
Verification Data is performance data.
5%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
99%
85%
55%
25%
10%
Flow Calibration Data
Set Flow True Flow
750 816.331
1500 1623.834
3000 3196.153
4500 4740.936
6000 6238.722
7500 7695.252
9000 9180.734
10500 10618.265
12000 12098.602
13500 13641 .838
15000 15211 .376
All values in SCCM
Flow Verification Data
Set Flow True Flow
14850 14899.113
12750 12795.052
8250 8263.069
3750 3749.445
1500 1506.225
All values in SCCM
% dev
0.33%
0.35%
0.16%
-0.01 %
0.41%
This calibration complies with ISO 17025-2005 [non-accredited] and is traceable to the National Institute of Standards and Technology (NIST). Calibration and verification
are accomplished exclusively by qualified personnel following controlled procedures under 150 9001:2015. For questions or concerns, contact Customer Service via our
Verified by:-~~L~---==-
website, email or by phone, weekdays from 8AM -4PM.
Date 7 /21 l:n ---+-ti ·L--;-f--'=-'---..,,,_____
F 000~t5
Unit Summary
Model II: 4040
Unit SN : 3278
I 69 Industrial Park Rd E, Tolland CT 06084
https://www.environics.com/service-request
[phone] [e-mail]
ENVIRONICS FLOW CONTROLLER CALIBRATION REPORT
Std Conditions
Temp: 32'F
Pressure:
Gas :
29.92 in. Hg
NITROGEN
MFC Summary
MFCII: 3
MFC FS Flow: 1500
MFC S/N: 2009600001
Flow Calibration Data is not performance data. This data is used by the system operating mode to improve the flow accuracy. The Flow
Verification Data is performance data.
5%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
99%
85%
55%
25%
10%
Flow Calibration Data
Set Flow True Flow
75 73.280
150 149.761
300 302.861
450 454.649
600 608.192
750 760.81 0
900 912.792
1050 1066.473
1200 1222.370
1350 1379.391
1500 1540.402
All values 1n SCCM
Flow Verification Data
Set Flow True Flow
1485 1485.464
1275 1275.083
825 824.119
375 375.550
150 150.528
All values 1n SCCM
% dev
0.03%
0.01%
-0 .11%
0.15%
0.35%
This calibration complies with ISO 17025-2005 [non-accredited) and is traceable to the National Institute of Standards and Technology {NIST). Calibration and verification
are accomplished exclusively by qualified personnel following controlled procedures under ISO 9001:2015. For questions or concerns, contact Customer Service via our
website, email or by phone, weekdays from 8AM -4PM.
Verified by: _~V-7"'~ ......... ~----r.'M"'=:::--Date:
F 00016
Unit Summary
Model #: 4040
Unit SN : 3278
69 Industrial Park Rd E, Tolland CT 06084
https://www.environics.com/service-request
[phone] [e-mail]
ENVIRONICS FLOW CONTROLLER CALIBRATION REPORT
Std Conditions
Temp: 32°F
Pressure:
Gas:
29.92 in. Hg
NITROGEN
MFCSummary
MFC#: 4
MFC FS Flow: 150
MFC S/N: 2009700001
Flow Calibration Data is not performance data. This data is used by the system operating mode to improve the flow accuracy. The Flow
Verification Data is performance data.
5%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
99%
85%
55%
25%
10%
Flow Calibration Data
Set Flow True Flow
7.5 8.317
15 16.641
30 32.874
45 48.602
60 63.878
75 78.883
90 93.620
105 108.240
120 122.986
135 137.994
150 153.049
All values In SCCM
Flow Verification Data
Set Flow True Flow
148.5 148.413
127.5 127.422
82.5 82.496
37.5 37.590
15 15.024
All values In SCCM
% dev
-0.06%
-0.06%
0.00%
0.24%
0.16%
This calibration complies with ISO 17025-2005 [non-accredited] and is traceable to the National Institute of Standards and Technology (NIST). Calibration and verification
are accomplished exclusively by qualified personnel following controlled procedures under ISO 9001:2015. For questions or concerns, contact Customer Service via our
website, email or by phone, weekdays from 8AM -4PM.
Date:
F 00017
Dilution System Verification
Method 205 Dilution System Verification
Company Name RHEx Vernal
Job Number 24-1043
Date May 28, 2024
Dilution System Make Environics
Series Number 4040
System Serial Number 3278
Analyzer Make CAI ZRE
Analyzer Identification Number A9L4312T
Analyzer Span 0-20.4
Reference Gas 02
Reference Gas Concentration 20.40
Reference Gas Cylinder Number EB0157262
Reference Gas Expiration Date September 16, 2030
Reference Gas Cylinder Pressure 1400
Verification Gas 02
Verification Gas Concentration 10.09
Verification Gas Cylinder Number EB0165775
Verification Gas Expiration Date February 27, 2032
Verification Gas Cylinder Pressure 2000
High Gas Concentration 20.40 Mid Gas Concentration
High Gas Response #1 20.43 Mid Gas Response #1
High Gas Response #2 20.44 Mid Gas Response #2
High Gas Response #3 20.41 Mid Gas Response #3
Average 20.43 Average
Standard Deviation 0.02 Standard Deviation
Percent RSD* 0.07 Percent RSD*
Percent Difference** 0.13 Percent Difference**
10.20
10.18
10.18
10.19
10.18
0.01
0.06
0.16
Verification Gas Concentration
Verification Gas Response #1
Verification Gas Response #2
Verification Gas Response #3
Average
Standard Deviation
Percent RSD*
Percent Difference**
*Percent RSD must be S 2.0%
**Percent Difference must Be S 2.0%
10.09
10.10
10.11
10.14
10.12
0.02
0.21
0.26
F 00018
APPENDIXG
Resumes of Test Personnel
Technical
Expertise:
Technical
Experience:
Education:
Certification:
PROFESSIONAL PROFILE
TYLER CORDELL
Project Manager
• Source Emission Testing
• Visible Emissions
• Field Sampling and Recovery
• CEMS Operation and Emissions Testing
• Project Leader
• Monitoring Equipment Repair
• Calibration and Maintenance of Sampling Equipment
Mr. Cordell has been participating in and leading projects for Western
Environmental since 2007. He has assisted in and lead numerous source
emission projects throughout the United States and internationally. His
experience includes source emission testing projects utilizing many EPA
test methods.
Mr. Cordell has 2 years of college education through the Casper College
accounting program
First Aid/CPR
OSHA 40-Hour Safety Training Course
H2S Safety Training
MSHA Miner Training
Fire Extinguisher Training
HAZWOPER 8 Hour Refresher
CSTOP
Defensive Driving Training
Technical
Expertise:
Technical
Experience:
Education:
Certification:
PROFESSIONAL PROFILE
Josh Trennell
Environmental Specialist I
o Source Emission Testing
• Field Sampling
• Calibration and Maintenance of Sampling Equipment
Mr. Trennell is a relatively new addition to the staff of Western
Environmental. He has participated in numerous source emission surveys
across the United States. Mr. Trennell has experience in sample train
preparation, stack work, and equipment calibration and Maintenance.
High School Graduate
OSHA 40-Hour Safety Training Course-Current
H2S Safety Training-Current
Defensive Driver Training-Current
Fire Extinguisher Training-Current
Technical
Expertise:
Technical
Experience:
Education:
Certification:
PROFESSIONAL PROFILE
Brandon Wenberg
Environmental Specialist I
• Source Emission Testing
• Field Sampling
• Calibration and Maintenance of Sampling Equipment
Mr. Wenberg is a relatively new addition to the staff of Western
Environmental. He has participated in numerous source emission surveys
across the United States. Mr. Wenberg has experience in sample train
preparation, stack work, and equipment calibration and Maintenance.
Graduate of Kelly Walsh High School, Casper, Wyoming
OSHA 40-Hour Safety Training Course-Current
H2S Safety Training-Current
Defensive Driver Training-Current
Fire Extinguisher Training-Current
Technical
Expertise:
Technical
Experience:
Education:
Certification:
PROFESSIONAL PROFILE
Patricia Robison
Environmental Specialist I
• Source Emission Testing
• Field Sampling
• Calibration and Maintenance of Sampling Equipment
Ms. Robison is a relatively new addition to the staff of Western
Environmental. She has participated in numerous source emission
surveys across the United States. Ms. Robison has experience in sample
train preparation, stack work, and equipment calibration and
Maintenance.
OSHA 40-Hour Safety Training Course-Current
H2S Safety Training-Current
Defensive Driver Training-Current
Fire Extinguisher Training-Current
APPENDIXH
Process Data
Ramsey Hill Exploration, LLC -Vernal Sand Plant
Stack Test -Dryer #3, Sand Dryer with Cyclone and Baghouse
!Date: 5/29/20241 [Run#: 1
!start nme: I 8:25AM I [End Time: I 10:30AM
Read Time: Dryer 3 Feed Rate: Dryer 3 Feed Scale Tare: Propane Differential Pressure:
[00:00 am/pm] [tph] [tons] [gpm approximation] ["W.C.]
8:25AM 184 294 6 2.9
8:40AM 183 6 2.9
8:55AM 185 6 2.9
9:10AM 185 6 3.0
9:25AM 182 6 3.0
9:40AM 186 6 3.0
9:55AM 186 6 3.0
10:10AM 184 6 3.1
10:25AM 183 6 3.1
10:30AM 185 680 6 3.1
3.0
ARC Notes: Sand moisture check 3.0% at 8:15am
~
Q rs ~ s N
ARC Notes:
Ramsey Hill Exploration, LLC -Vernal Sand Plant
Stack Test -Dryer #3, Sand Dryer with Cyclone and Baghouse
[Date: 5/29/2024] [Run#: 2
[start nme: 10:52AM [End Time:
Read nme: Dryer 3 Feed Rate: Dryer 3 Feed Scale Tare: Propane
[00:00 am/pm] [tph] [tons] [gpm approximation]
10:52AM 182 705 6
11:07 AM 185 6
11:22AM 186 6
11:37 AM 181 6
11:52 AM. 187 6
12:07 PM 184 6
12:22 PM 182 6
12:37 PM 183 6
12:52 PM 182 6
12:58 PM 182 1089 6
Average: 183 384
Sand moisture check 3.0% at 11:00am
12:58 PM
Differential Pressure:
["W.c.]
3.2
3.2
3.3
3.3
3.3
3.3
3.3
3.4
3.4
3.4
• ~
s SI ~ s vl
ARC Notes:
Ramsey Hill Exploration, LLC -Vernal Sand Plant
Stack Test -Dryer #3, Sand Dryer with Cyclone and Baghouse
I Date: 5/29/20241 [Run#: 3
I start Time: I 1:13 PM I [End Time:
Read Time: Dryer 3 Feed Rate: Dryer 3 Feed Scale Tare: Propane
[00:00 am/pm] [tph] [tons] [gpm approximation]
1:13 PM 182 1166 6
1:28 PM 182 6
1:43 PM 183 6
1:58 PM 188 6
2:13 PM 188 6
2:28 PM 184 6
2:43 PM 188 6
2:58 PM 186 6
3:13 PM -183 6
3:19 PM 184 1556 6
Sand moisture check 3.0% at 1:30pm
I 3:19 PM
Differential Pressure:
["W.C.]
3.5
3.6
3.6
3.6
3.6
3.7
3.7
3.7
3.7
3.7
IARC Notes:
J:
joate:
jstartTime:
Read Time:
[00:00 am/pm]
9:36AM
9:51AM
10:06AM
10:21AM
Ramsey Hill Exploration, LLC -Vernal Sand Plant
Stack Test -Inertia Crusher #2, with Optional Spray Bar
5/29/2024]
9:36AM]
Crusher 2 Feed Rate:
[tph]
445
452
430
444
Crusher 2 Feed Scale Tare:
[tons]
762
1207
[Run#: 1
[End Time:
No opacity observed. Per NSPS Subpart 000, the test can be kept to 1 hour only.
Water Sprayed:
[gpm]
0.0
0.0
0.0
0.0
10:36AM]
0.0
--------·------------~-~-------~••.o••-----------------------