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HomeMy WebLinkAboutDAQ-2024-0079601 DAQC-412-24 CAERS ID 10253 (B4) MEMORANDUM TO: STACK TEST FILE – UGC MIDSTREAM, LTD, LLC – Westwater Compressor Station – Grand County, Utah THROUGH: Rik Ombach, Minor Source Oil and Gas Compliance Section Manager FROM: Kyle Greenberg, Environmental Scientist DATE: May 1, 2024 SUBJECT: Sources: Three (3) Caterpillar G3516 LE compressor engines; SN: WPT00216, WPT00215, and WPT00209 Contact: Ken Secrest: 970-675-4400 Location: Remote location in Grand County, UT Test Contractor: Great Plains Analytical Services, Inc. Permit/AO#: DAQE-AN102530014-18 dated April 6, 2018 Action Code: TR Subject: Review of Stack Test Report dated April 11, 2024 On April 11, 2024, Utah Division of Air Quality (DAQ) received a test report for the above listed units. Testing was performed February 21-22, 2024, to demonstrate compliance with the emission limits found in Condition II.B.2 of Approval Order DAQE-AN102530014-18 and 40 CFR Part 60 Subpart JJJJ. The calculated test results are: Source Test Date Test Method Pollutant Tester Results DAQ Results Limits Unit A: Cat G3516LE; SN: WPT00216 Feb. 21, 2024 7E NOx 21.897 ppm @15% O2 0.267 g/hp-hr 21.896 ppm@15% O2 0.799 lb/hr 0.271 g/hp-hr 76.6 ppm@15% O2 2.79 lb/hr 2.0 g/hp-hr 10 CO 0.578 ppm @15% O2 0.004 g/hp-hr 0.578 ppm@15% O2 0.013 lb/hr 0.004 g/hp-hr 125.7 ppm@15% O2 2.79 lb/hr 4.0 g/hp-hr 25A VOC 15.215 ppm@15% O2 0.177 g/hp-hr 15.027 ppm@15% O2 0.176 g/hp-hr 86 ppm@15% O2 1.0 g/hp-hr Unit B: Cat G3516LE; SN: WPT00215 Feb. 22, 2024 7E NOx 42.011 ppm @15% O2 0.618 g/hp-hr 42.007 ppm@15% O2 1.310 lb/hr 0.611 g/hp-hr 76.6 ppm@15% O2 2.79 lb/hr 2.0 g/hp-hr 10 CO 0.118 ppm @15% O2 0.002 g/hp-hr 0.118 ppm@15% O2 0.002 lb/hr 0.001 g/hp-hr 125.7 ppm@15% O2 2.79 lb/hr 4.0 g/hp-hr 25A VOC 8.774 ppm@15% O2 0.124 g/hp-hr 8.774 ppm@15% O2 0.122 g/hp-hr 86 ppm@15% O2 1.0 g/hp-hr 2 Source Test Date Test Method Pollutant Tester Results DAQ Results Limits Unit C: Cat G3516LE; SN: WPT00209 Unit C: Cat G3516LE; SN: WPT00209 Feb. 22, 2024 Feb. 22, 2024 7E NOx 31.708 ppm @15% O2 1.304 g/hp-hr 31.706 ppm@15% O2 0.849 lb/hr 0.378 g/hp-hr 76.6 ppm@15% O2 2.79 lb/hr 2.0 g/hp-hr 10 CO 0.647 @15% O2 0.016 g/hp-hr 0.647 ppm@15% O2 0.011 lb/hr 0.005 g/hp-hr 125.7 ppm@15% O2 2.79 lb/hr 4.0 g/hp-hr 25A VOC 16.653 ppm@15% O2 0.655 g/hp-hr 16.652 ppm@15% O2 0.187 g/hp-hr 86 ppm@15% O2 1.0 g/hp-hr DEVIATIONS: None. CONCLUSION: The stack test report appears to be acceptable. RECOMMENDATION: It’s recommended the emissions from the three (3) Caterpillar G3516 LE compressor engines be considered to have been in compliance with the emission limits of the Approval Order and 40 CFR Part 60 Subpart JJJJ. There was a clerical error in the report for Unit C; the stack diameter is 14 inches, see attached email clarifying this. This test is in response to Compliance Advisory (DAQC-351-23), for not conducting subsequent compliance tests at least once every two years. ATTACHMENTS: DAQ Stack Test Review Excel Spreadsheets, UGC Midstream Test Report. UGC MIDSTREAII/I, LTD, LLC Westwater Compressor Station Grand County, Utah Unit A; Caterpillar G35l6LE; SN: WPT002'16 TeslDalei2l2l12024 Emissions 1 Start Time 1 1:55 Stop Time 12:55 2 13:33 14:33 60 14:49 15:49 60 BHP Engine Load -Actual (bhp)Ds Stack Diameter (inches) VAPouo Average (Delta p)% (" Hro)%p Pitot Tube Constant (unitless) s Stack Temperature ("F) bar Barometric Pressure (mbar) bar Barometric Pressure (" Hg), Stack Pressure (" H2O) %vd O, (%vd) )2o/ovd CO, (%vd) o/ovd N, (%vd) 1339 1338 1339 14.0 14.0 14.0 't .1727 1.1867 1.0210 0.99 0.99 0.99 789 793 755 848 848 848 25.05 25.05 25.05 1 .38 ',t.41 1.04 9.3 9.7 9.5 5.6 5.5 5.4 85.1 84.9 85.1 50.2 38.8 38.3 2.0 0.3 1.0 1 339 't4.0 1.1268 0.99 779 848 25.0s 1.28 OE 5.5 85.0 42.4 1.1 ws Measured Moisture Content (%/100) ws Saturated Moisture Content (%/100) ws Actual Moisture Content (%/100) lo Molecular Weight Dry (lb/lb-mole) lr Molecular Weight Wet (lb/lb-mole) s Gas Velocity (tusec) ACFM Gas Flow (acfm) DSCFM Gas Flow (dscfm) wscFrv Gas Flow (wscfm) KWSoFH Gas Flow (kwscfh) KWSoFM Gas Flow (kwscfm) lnt Gas Flow (lb/hr)'o Fo (unitless) 0.093 0.097 0.095 388.396 396.245 325.453 0.093 0.097 0.095 29.267 29.261 29.244 28.223 28.172 28.177 131.662 133.554 113.197 u44.884 8566.293 7260.546 2720.370 2739.136 2396.400 3000.519 3034.598 2649.612 180.031 182.076 158.977 3.001 3.035 2.650 13187.342 13313.028 11626.178 2.075 2.056 2.112 8.417 8.736 8.593 5.080 4.93'1 4.887 0.095 370.032 0.095 29.257 24.191 126.1 38 8090.574 2618.635 2894.91 0 173.695 2.895 12708.849 2.081 8.582 4.966 wet NO1(ppmvw) 15 NOx (ppmvd @ 15% 02) 45.519 35.028 34.704 25.472 20.380 19.838 0.977 0.761 0.658 0.331 0.258 0.223wet CO (ppmvw) 15 CO (ppmvd @ 15% o2) 1.804 0.313 0.949 1.009 0.182 0_543 0.024 0.004 0.011 0.008 0.001 0.004 15 NMEOC (ppmvd as CaHs @ 15% 02) 22.412 31.898 32.746 11.377 16.762 16.940 0.418 0.599 0.538 142 0.203 0.1 Page 1 of 5 Linearity UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit A; Caterpillar G3516LE; SN: WPT00216 Test Date:?2112024 Gas Value/Range Bias Check (Zero) Bias Check (Span) I 2 3 4 Results Bias Bias Calibration Error Page 2 of 5 Run 1 UGC MIDSTREAM, LTD, LLC Westwater Gompressor Station Grand Gounty, Utah Unit A; Gaterpillar G3516LE; SN: WPT002i5 Test Date:2/2112024 Run I Start Time Run LengthTime 12:55 lnstrument Range Span Gas Value Pretest Calibration Post Test Calibration Page 3 of 5 Run 2 UGC MIDSTREAM, LTD, LLC Westwater Gompressor Station Grand County, Utah Unit A; Gaterpillar G3515LE; SN: WPT00216 Test Date:212112024 Run 2 Start Time Run LengthTime 14:33 lnstrument Range Span Gas Value Pretest Calibration Span% Post Test Calibration Zeroo/o Span% Its Absolute Drift (Zero) Page 4 of 5 Run 3 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit A; Caterpillar G3516LE; SN: WPT00216 Test Date:?2112024 Run 3 Start Time Run Length Time 15:49 !nstrument Range Span Gas Value Calibration Pretest Calibration Post Test Calibration Page 5 of 5 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit B; Caterpillar G35l6LE; SN: WPT00215 TeslDalei2l22l2024 Emissions 3 11:11 12:11 60 973 14.0 0.8980 0.99 726 857 25.32 0.82 8.7 5.9 85.4 86.8 0.2 16.1 BHP Engine Load - Actual (bhp) Ds Stack Diameter (inches) iAPorn Average (Delta P)% (" Hro)%ip Pitot Tube Constant (unitless) s Stack Temperature ("F) ,, Barometric Pressure (mbar) * Baromehic Pressure (" Hg) Stack Pressure (" H2O) %ud 02 (%vd) 999 953 968 14.0 14.0 14.0 0.9240 0.8537 0.9163 0.99 0.99 0.99 727 721 729 857 858 857 25.31 25.34 25.31 0.86 0.74 0.85 8.7 8.7 8.7 5.9 5.9 5.9 85.4 85.4 85.4 89.3 89.7 81.4 0.4 0.2 0.2 276.144 266.6s4 279.289 0.1't2 0.112 0.111 29.289 29.291 29.291 28.024 28.030 28.035 101.037 93.065 100.269 6480.626 5969.237 6431.33s 2168.920 20t0.500 2150.677 2444.555 2264.983 2421.812 146.673 't35.899 145.309 2.445 2.265 2.422 10668.214 9886.640 10572.90',1 2.077 2.070 2.067 7.696 7.735 7.774 123 0.112 0.112 0.111 5.229 5_231 5.225 Average 0.112 274.O29 0.112 29.290 28.030 98.124 6293.732 2110.032 2377.117 142.627 2.377 1 0375.91 I 2.071 7.735 5.229 ws Measured Moisture Content (%/100) ws Saturated Moisture Content (%/100) s Actual Moisture Content (%/100) lo Molecular Weight Dry (lb/lb-mole) In Molecular Weight Wet (lb/lb-mole) s Gas Velocity (fvsec) DscFM Gas Flow (dscfm) wscFM Gas Flow (wscfm) KwscFH Gas Flow (kwscfh) KwscFM Gas Flow (kwscfm) 15 NOx (ppmvd @ 15% o2) 1 .387 1.291 1.254 0.630 0.614 0.587 0.319 0.152 0.181 0.173 0.083 0.099 0.003 0.001 0.002 0.002 0.001 0.001 15 CO (ppmvd @ 15% 02) 15 NMEOC (ppmvd as C3Hs@ 15% O2) 122 0120 0.1 18.009 18.231 18.147 8.687 8.823 8.811 0_268 0.251 0.268 Page 1 of 5 Linearity UGC MIDSTREAM, LTD, LLC Westwater Gom pressor Station Grand Gounty, Utah Unit B; Caterpillar G3516LE; SN: WPT002i5 Test Date:2/2212024 Gas Value/Range Gas Value Check (Zero'1 Check (Span) 1 2 3 4 1 2 3 4 1 2 3 4 Results Calibration Error Page 2 of 5 Run 1 UGC MIDSTREAM, LTD, LLC Westwater Compiessor Station Grand County, Utah Unit B; Gaterpillar G3516LE; SN: WPT00215 Test Date:2/2212024 Run { Start Time Run Length Time 9:41 lnstrument Range Span Gas Value Pretest Calibration Zeroo/o Span% Post Test Calibration Zeroo/o Span% Page 3 of 5 Run 2 UGC MIDSTREAM, LTD, LLC Westwater Com pressor Station Grand Countyr, Utah Unit B; Gaterpillar G3516LE; SN: WPT00215 Test Date:2122i2024 Run 2 Start Time Run LengthTime 10:57 lnstrument Range Span Gas Value Pretest Calibration Zeroo/o Span% Post Test Calibration Zeroo/o Span% Page 4 of 5 Run 3 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand Gounty, Utah Unit B; Caterpillar G35{6LE; SN: WPT00215 Test Date:212212024 Run 3 Start Time Run Length Time 12:11 lnstrument Range Span Gas Value Pretest Calibration Zeroo/o Span% Post Test Calibration Zeroo/o Span% Results Page 5 of 5 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit C; Caterpillar G3516LE; SN: WPT00209 TeslDalet2l22l2024 Emissions I '13:10 14:10 60 2 14:48 15:48 60 3 '16:04 17104 1183 552 952 14.0 14.0 t4.0 0.7768 0.8478 0.8142 0.99 0.99 0.99 714 749 744 856 856 856 25.28 25.27 25.28 0.61 0.73 0.67 9.6 9.2 9.1 5.5 5.7 5.8 84.9 85.1 85.1 65.8 55.2 66.'l'1.3 1.1 1.4 35_4 26.5 25.6 1029 14.0 0.8129 0.99 737 856 25.28 0.67 9.3 5.7 85.0 62.4 1.3 29.2 TS Pu", Pr", Ps O2Yovd CO2o/ovd Nr%vd dry Engine Load - Actual (bhp) Stack Diameter (inches) Average (Delta P)% (" HrO)v' Pitot Tube Constant (unitless) Stack Temperature ('F) Barometric Pressure (mbar) Barometric Pressure (" Hg) Stack Pressure (" H2O) Oz (%vd) CO2 f/ovd) N, (%vd) NOx (ppmvd) CO (ppmvd) 1230.107 0.108 0.109 256.825 312.603 310.837 0.107 0.108 0.109 29.270 29.280 29.285 28.070 28.061 28.055 84.483 93.596 89.852 918.802 6003.295 5763.164 1841.681 1977.625 1898.380 2062.718 2214.952 2132.428 123.763 ',t3?.'.137 127.946 2.063 2.219 2.132 9016.722 9696.373 9316.193 2.040 2.057 2.050 8.574 8.165 8.102 4.949 5.092 5.131 Average 0.1 08 293.422 0.1 08 29.278 28.062 89.310 5728.420 '1905.895 21 38.033 128.282 2.138 9343.096 2.049 8.280 5.058 r*" Measured Moisture Content (%/100) ,*" Saturated Moisture Content (%/100) ,* Actual Moisture Content (%/100),lo Molecular Weight Dry (lb/lb-mole),lo Molecular Weight Wet (lb/lb-mole) '" Gas Velocity (fusec) AcFM Gas Flow (ac'fm) DscFM Gas Flow (dscfm) wscFM Gas Flow (wscfm) KwscFH Gas Flow (kwscfh) KWScFM Gas Flow (kwscfm) 58.788 49.236 58.879 34.349 27.735 33.034 0.868 0.782 0.898 0.333 0.372 0.428 '15 NO1 (ppmvd @15%02) 1.',t57 0.968 1 .280 0.676 0.546 0.718 0.010 0.009 0.012 0.004 0.004 0 CO (ppmvw) CO (ppmvd @ 15% o2) 5 NMEOC (ppmvd as CaHs@ 15% Or) o.1s2 0.178 39.617 29.666 28.758 20.680 14.903 14.373 0.500 0.402 0.374 Page 1 of 5 Linearity UGC MIDSTREAM, LTD, LLC Westwater Com pressor Station Grand Gounty, Utah Unit C; Caterpillar G3516LE; SN: WPT00209 Test Date:22212024 Gas Value/Range Gas Value Check (Zero) Check (Span) 1 2 3 4 1 2 3 4 1 2 3 4 Results Calibration Error Page 2 of 5 Run 1 ucc MIDSTREAM, LTD, LLC Westwater Gompressor Station Grand Gounty, Utah Unit C; Caterpillar G3516LE; SN: WPT00209 Test Date:2/2212024 Run I :Time Length Time '14:10 lnstrument Range Span Gas Value Pretest Calibration Zeroo/o Span% Post Test Calibration Zeroo/o Spano/o Page 3 of 5 Run 2 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit C; Caterpillar G35l6LE; SN: WPT00209 Test Date:22212024 Run 2 Start Time Run Length Time 15:48 lnstrument Range Span Gas Value Pretest Calibration ZeroYo Span% Post Test Galibration Zeroo/o Span% Page 4 of 5 Run 3 UGC MIDSTREAM, LTD, LLC Westwater Compressor Station Grand County, Utah Unit C; Caterpillar G3516LE; SN: WPT00209 Test Date:2/2212024 Run 3 Start Time Run LengthTime 17:04 Instrument Range Span Gas Value bration Pretest Calibration Zeroo/o Span% Post Test Calibration Zeroo/o Span% Page 5 of 5 #RS. 303 West 3rd Street , Elk Ci4t, Oklahoma 73644 . 580-225-0403 April 11,2024 Utah Department of Environmental Quality State Office Building - Air Quality Division 195 North 1950 West Salt Lake city, Utah 84116 RE: Utah Gas Corp. 40 CFR Part 60 Subpart JJJJ - Test Report Submittal To Whom It May Concem, Please find enclosed the performance testing reports for 40 CFR Part 60 Subpart JJJJ on behalf of Utah Gas Corp. The testing took place the week of February 19,2024. Please see below for the information pertinent to the enclosed report. For information regarding the performance test, you can contact me by email at acarlson@gasinc.us or by phone at580-225-0403. For information regarding engine or location information, please contact Chris Forster by email at chris.forster@.utahgascorp.com or by phone at (970)250-3385. Regards, Andrea Carlson Client Analyst GAS GAS Inc. www.gasinc.tts Facilitv Unit #Serial #Location West Water CS Unit A wPT002l6 Grand Co. Utah West Water CS Unit B wPT002l5 Grand Co. Utah West Water CS Unit C wPT00209 Grand Co. Utah 40 CFR Part 60 Subpart JJJJ Performance Test Report Test Type: Initial Test Date: A21nO24 DOM: 111109 Source: Caterpillar G3516LE Lean Burn (4 Cycle) Unit Number: Unit A Serial Number: WPT0021 6 Engine Hours: 62793.3 Location: West Water CS Grand County, Utah Prepared on Behalf of: Utah Gas Corp Test Started: 11:55 AM Test Completed: 04:14 PM #As 303 W.3rd St (580) 225-0403 Elk City , OK73644 lndex 1.0 Key Personnel.... ............. 3 2.0 Sampling System..... ..:.... 3 3.0 Methods Used............ ......................... 3 4.0 Test Summaries.. ............ 5 5.0 Run Summaries.. ............ 6 6.0 Volumetric Flow Rate Data.... ............. 7 7.0 Calculations.............. ...... 8 8.0 Oxygen Calibration... ...... I 9.0 Engine Parameter Data Sheet.. .......... 10 10.0 QA/QC Results........ ........ 11 11.0 D6348 Annexes...... ........ 12 12.0 Signature Page........ ....... 18 13.0 Appendices.............. ....... 19 14.0 Bottle Certs............ ......... 20 '15.0 Tri Probe Certification via GD-031 ...... 25 16.0 GAS ALT 141_FT|R EPA......... ...........26 17.0 Tester Qualifications (resume)... ......... 28 18.0 RawData............. irbi;; .......... 2e Table 5.1 (Run Summaries)............. ........... 6 Table 6.1 (Volumetric Flow Rate Data)............ ............... 7 Table 6.2 (Stack Gas Measurements)....... ......................7 Table 8.1 (Oxygen Calibration).. ................. I Annex Table 1.2.1 (Certified Calibration Bottle Concentrations)......... 12 Annex Table 1.2.2 (Measurement System Capabilities)..................... 12 AnnexTable1.3.1 (TestSpecificTargetAnalytes)............................. 13 Annex Table 4.1 (Measure System Capabilities) ............ 15 Figures Figure 6.1 (Location of Traverse Points per Method 1) ... .. .7 Annex Figure 1.4.1 (Sampling Train)..... ..... 13 Annex Figure 1.4.2 (Sampling Points)... ...... 14 Annex Figure 1.4.3 (Sampling Port Locations).... ............ 14 Appendices Certified Calibration Bottle Certificates............... ............. 20 Tri Probe Certification via GD-031 .............. 25 GAS ALT 141_FT|R EPA............. ............... 27 Tester Qualifications (resume)... ................. 28 Raw Data.... ... .... 29 3 1.0 Key Personnel GAS Utah Gas Corp Lucas Ennis Derrick Timothy 2.0 Sampling System The sampling system used consisted of a Stainless steel probe, heated Teflon line, gas conditioning system, and a Gasmet model DX4000 FTIR analyzer. The gas conditioning system used was a Gasmet Personal Sampling System with a Zirconium Oxide oxygen sensor. 3.0 Methods Used ASTM D6348.03 This extractive FTIR based field test method is used to quantify gas phase concentrations of multiple target analytes (CO, NOX, CH2O, & VOC's)from stationary source etfluent. Because an FTIR analyzer is potentially capable of analyzing hundreds of compounds, this test method is not analyte or source specific. The analytes, detection levels, and data quality objectives are expected to change for any particular testing situation. lt is the responsibility of the tester to define the target analytes, the associated detection limits for those analytes in the particular source etfluent, and the required data quality objectives for each specific test program. Provisions are included in this test method that require the tester to determine critical sampling system and instrument operational parameters, and for the conduct of QA/QC procedures. Testers following this test method will generate data that will allow an independent observer to verify the valid collection, identification, and quantification of the subject target analytes. EPAMethodl &1A The purpose of the method is to provide guidance for the selection of sampling ports and traverse points at which sampling for air pollutants will be performed pursuant to regulations set forth in this part. EPA Method 2 &2C This method is applicable for the determination of the average velocity and the volumetric flow rate of a gas stream. The average gas velocity in a stack is determined from the gas density and from measurement of the average vetocity head with a standard pitot tube. Velocity readings are taken from each stack at 16 separate traverse points (Table 6.1) and used to determine the engines mass emissions rate, calculated utilizing the formulas seen in section 7.0 of this report. EPA Method 3A This is a procedure for measuring oxygen (O2) and carbon dioxide (CO2) in stationary source emissions using a continuous instrumental anatyzer. Quality assurance and quality control requirements are included to assure that the tester collects data of known quality. Documentation to these specific requirements for equipment, supplies, sample collection and analysis, calculations, and data analysis will be included. GAS 4.0 Test Summary Unit Unit A with a serial number of WPT00216 which is a Caterpillar G3516LE engine located at West Water CS and operated by Utah Gas Corp was tested for emissions of. Carbon Monoxide, Oxides of Nitrogen, and Volatile Organic Compounds. The test was conducted on 212112024 by Lucas Ennis with Great Plains Analytical Services, lnc. All quality assurance and quality controltests were within acceptable tolerances. The engine is a naturalgas fired Lean Burn (4 Cycle) engine rated at 1340 brake horse power (BHP) at 1400 RPM. The engine was operating at 1339 BHP and 1399 RPM which is 99.91% of maximum engine load during the test. The test HP calculation can be found on page 8. The engine was running at the maximum load available at the test site. This test will satisfy the testing requirements for 40 CFR Part 60 Subpart JJJJ. Site Verification Photos li. r GAS GAS 6 5.0 Run Summaries Table 5.1 Run Summaries GAS Table 6.1. Data used for volumetric flow rate (Method 2) Pitot Tube Coefficient Co(std)= .99 or: 1 or:I 'l 10.51 square Feet 10.64 s.60 5.46 5.40 5.49 8.38 8.76 8.61 8.58 1.77 0.31 0.94 't.01 29.22 Molecular Weight Stack Gas wet basis (Ms lo/o mole 24.O2 28.03 28.03 28.03 Stack Static Pressure "t'l?t)l.5u 1.41 1.O4 1.26 Stack Static Pressure "Hq 0.10 0.10 0.08 0.09 AtmosDheric Pressure at Location (Pbal MtsAR 848.18 848.00 848.00 8/l8.06 Atmosoheric Pressure at Location (Pbal "H 25.05 25.05 25.05 25.05 Absolute Stack Pressure (Pr "H 25.15 25.15 25.12 25.'.t4 Stack Temperature I Deo G 420.s6 422.78 40't.67 415.00 Stack TemDerature I Deo F 789.00 793.00 755.00 779.OO Stack Temperature I Deg R 1248.67 1252.67 't214.67 1238.67 Stack Gas Velocity I fUsec 132.22 133.90 113.48 126.76 tilack Flow HaIe Q I cfs 141.35 143.14 121.31 't35.51 stacl( Gas wet volmetnc Flow Hate I sct/hr 180888.18 182572.O0 159395.1 6 174739 33 Stack Gas IJry Volumetric Flow Ftate I scf/hr 161333.26 163207.50 142638.75 156141.53 -mtsstons samoilno i-otnls - iJ Dotnl lono ilne samDilno Droo€lnches FirstSamDlinq PointTaken @ 16.7o/o olStacl Diameter 2.34 Second SamDlinq Point Taken @ 50% of Stac Diameter 7 Third SamDlinq Point aken @ 8( 3% of Stack Diameter 11.66 6.0 Volumetric Flow Rate Data Table 6.2. Stack gas pressure measured with a standard tube use for Volumetric Flow Bate 7 Aostd = Velocitv head measured bv the' standard pitot tube, (in.) H2O.' uamDle after BacK Puroe:1.06 Within 5% of Last Apstd reading:Yes Stack Diameter (inches)14.00 lnches upstream from disturbance 26.00 lncnes downstream lrom dtsturbance 92.UU Pitot readings are taken for Method 2 calculations using measuring points outlined in Method 1 'The exhauet stack dld not prosont cyclonlc flow conditions at the sampling locatlon due to the absence of cyclones, lnertlal demlsterc, venturl scrubbers, oi tangential inlets. * Cyclonlc Flow Check (Pass,Fall): PASS GAS 7.0 Calculations Method 2: Determination of Stack Gas Velocitv and Volumetric Flow Rate *Note- Use of this method neqates the need for anv fuel related numbers for emissions calculations Ap(avg) = Velocity head of stack gas, mm H2O (in. H2O). 3600 = Conversion Factor, sec/hr. A = Cross-sectional area of stack, m2 (ft2). Bws = Water vapor in the gas stream (from ASTM Dffi€) Cp(std) = Standard pitot tube coefficient; use 0.99 Kp = Velocity equation constant. Md = Molecular weight of stack gas, dry basis, g/g-mole (lb./lb.-mole). Ms = Molecular weight of stack gas, wet basis, g/g-mole (lb.flb. -mole). Ps = Absolute stack pressure (Pbar+ Pg), mm Hg (in Hg) Pstd = Standard absolute pressure, 760 mm Hg (29.92 in. Hg). Qsd = Dry volumetric stack gas flow rate corrected to standard conditions, dscm/hr. (dscf/hr.). Ts(abs) = Absolute stack temperature, oK ("R). = 460 + Ts for English units. Tstd = Standard absolute temperature, 293"K (528'R). Vs = Average stack gas velocity, m/sec (ft./sec). Md = .44(.056)+.32(.093)+.28(.851+0) = 29.232 LB/I-B-MOLE Ms = 29.232(1 -.10811)+.18.0(.10811) = 28.018 LB/I-B-MOLEMs = Md(1 -Bws)+18.0(Bws) vs = 85.49..99.vl .38',v(1 248.671(25.15',28.018)) = 13Z.ZZ FTISEC Qsd = 3600(1 -Bws)Vs.A((Tstd'Ps)(Ts(abs)'Pstd))= 3600(1 -.1 08)1 32.224''t.O69l(528', 2s.15)t (1248.67'.29.92)) = 1 6 r 333.26 O = '161333.262135.315 = 4568.406 DSCM/l-lR Emission Rates (Examples use CO Run 1 453.6= Conversion factor lb. to gram HP= Engines rated Horsepower A = Cross-sectional area of stack, m2 (tt2). Mfg.= y2nulscturer Exhaust flow rate at 100% (tf3/min) BHP/HR. = Brake work of the engine, horsepower-hour (HP-HR.). 02 = Concentration of oxygen on a dry basis, percent. BTU/HP-HR. = Brake Specific FuelConsumption (HHV) ppm= Parts Per Million (CO) ER = Emission rate of (CO) in g/HP-hr. ppm@ 1 5% 02= PPM corrected lo 15/" 02 F(d )= Volurngs of combustion components per unit of heat Qsd = Dry volumetric stack gas flow rate corrected content, scm/J (scf/million Btu). to standard conditions, dscm/hr. (DSCF/HR.). Q = Stack gas volumetric flow rate, in standard cubic meters Run Time = Run Time in Minutes per hour, dry basis Tpy= Tons per year LB/HR.= Emission rate of (CO) in LB/HR. Vs = Average stack gas velocity, m/sec (ft./sec). Molwt.= Mol Weight of CO (28.01) ppm @ 15% 02 = PPM'(20.9-1 5o/o02')l(20.9-O2))ppm @'l5olo 02 = 1.988{20.9-15y(20.9-9.3%)) = 1.01 t PPM @ 15% 02 (1.988'(1.164.1 0^-3)'4568.406'(Run Time/60))/1339.043 = .008 G/HP-HBg/hp-hr - (PPM11 . 1 64-1 0r3)'Q.(Run Time/60))rBHP/HR LB/HR = .008'1/453.6-1339.043 = .023 LB/HR TPY = .023'4.38 = .101 TPY ppm wet * (U1-H2O) - ppm dry 1.99 = 1.7735-(1(1 -.1 1)) GAS 8.0 Oxygen Calibration 9 8.1 Calibration error test; how do I confirm my analyzer calibration is correct? After the tester has assembled, prepared and calibrated the sampling system and analyzer, they conduct a 3-point analyzer calibration error test before the first run and again after any failed system bias test or failed drifl test. They then introduce the low-, mid-, and high-level calibration gases sequentially in direct calibration mode. At each calibration gas level (low, mid, and high) the calibration error must be within t 2.0 percent of the calibration span. 8.2 lnitial system bias and system calibration error checks. Before sampling begins, it is determined whether the high- level or mid-level calibration gas best approximates the emissions and it is used as the upscale gas. The upscale gas is introduced at the probe upstream of all sample- conditioning components in system calibration mode. ('1) Next, zero gas is introduced as described above. The response must be within 0.5 percent ofthe upscale gas concentration. (2) Low-level gas reading is observed until it has reached a final, stable value and the results are recorded. The measurement system will be operated at the normal sampling rate during all system bias checks. (3) lf the initial system bias specification is not met, corrective action is taken. The applicable calibration error test from Section 8.2.3 of EPA Method 7E is repeated along with the initial system bias check until acceptable results are achieved, after which sampling will begin. The pre- and post-run system bias must be within t 5.0 percent of the calibration span for the low-level and upscale calibration gases. 8.3 Post-run system bias check and drift assessment - confirming that each sample collected is valid. Sampling may be performed for multiple runs before performing the poslrun bias or system calibration error check provided this test is passed at the conclusion of the group of runs. A failed final test in this case will invalidate all runs subsequent to the last passed test. (1) lfthe posfrun system bias check is not passed, then the run is invalid. The problem is then diagnosed and fixed, then another calibration error test and system bias is passed before repeating the run. (2) After each run, the low-level and upscale drift is calculated, using Equation 7E-4 in Section 12.5 from EPA Method 7E. lf the post-run low- and upscale bias checks are passed, but the low-or upscale drift exceeds the speciflcation in Section 13.3, the run data are valid, but a 3-point calibration error test and a system bias check must be performed and passed prior to additional testing. Table 8.1 Oxygen Calibration Method 7E 3,4 To the extent practicable, the measured emissions should be between 20 to 100 percent of the selected calibration span. This may not be practicable in some cases of low concentration measurements or testing for compliance with an emission limit when emissions are subslantially less than the limit. EPA Method 3A CIA Worksheet Certilied Gas Concentralon I Certlned Gas Concentralon I Certified Gas Co Low-Level (%l I Mid-Levet (%l I Hhh.Leve 0.00% I 9.12o/o I 21.O2o, ncentraion 7E 8.5: Note: that you may risk sampling for multiple runs before performing the poslrun bias provided you pass this test at the conclusion ofthe group of runs (DIRECT) Analyzer Calibration Error (5 2%) L Check Certified Concentration Value (%) Direct Calibration Response (9 Absolute Analyzer Calibration Enor (7o) Zero Gas o/o 0.00o/o 0.000/o 0.00o/o 0.00% Mid-Level Gas o/o High-Level Gas % 9.12o/o 21.02o/o 9.270/o 20.960/o 0.150h 0.06% 0.71o/o 0.29o/o (SYSTEM) Calibration Bias Checks (S 5%) and Drift Checks (5 3%)Upscale Gas 9.12ok Zero Offset 0.00% Bias Pre lnitial Value Bias Post lnital Values Span 2'1.02 Analyzer Calibration Response (o/o) Zero Gas 0.00% System Calibrations Response Pre (o/o) iystem Bias (ol of Span) Pre System Calibration Response Post (Yo) iystem Bias (o/ of Span) Post Drift (o/o of Span) 0.000/o 0.00%0.000/o 0.00o/o 0.00o/o Upscale Gas 9.27o/o 9.30%0.15o/o 9.18%0.43o/o 0.01olo (SYSTEM) Calibration Bias Checks (S 5%) and Drift Checks (S 3%) Avo. Gas Concentration (Run 1)9.4Oo/o Effluent Gas (Coas) Run 1 9.28o/o Avg. Gas Concentration (Run 2)9.807o Effluent Gas (Cgas) Run 2 9.68o/o Avg. Gas Concentration (Run 3)9.620/o Eff,uent Gas (Cgas) Run 3 9.5Oo/o EPA Method 3A QA Workshdet Zero Gas 100% Nitrogen Mid-Level Gas 9.120/o High-Level Gas 21.02o/o Zero Gas % Mid-Level Gas o/o High-Level Gas o/o zero Gas y" l-;6;;-l Upscale Used upscate cat I ,18% I etzo/o GAS 10 9.0 Engine Parameter Data Sheet AS Analgtiml Seruices, lnc Company Utah Gas Corp Facility West Water CS Date 2t21t2024 Site Elevation (ft)5121 Unit ID Unit A Make Caterpillar Model G3516LE Serial Numbel wPT00216 Technician Lucas Ennis Run 3 Completed Engine Parameter Data Run 1 Bun 2 Run 3 Average Enqine Speed (RPM)1399.0 1398.0 1399.0 1398.7 lntake Manifold Pressure (psi)31.U 32,U 2A.O 30.3 lntake Manifold Temp'F 129.2 129.2 121.4 128.6 Enqine Load (BHP)1339.0 1338.1 1339.0 1338.7/ Ambient Temp'F 50.0 53.0 53.0 52.O Humidity 70 4s.0 39.0 42.O 42.O Dew Point "F 30.0 29.O 30.o 29.7 AFR Manufacturer/Type Caterpillar Caterpillar I Caterpillar L;aterprllar suction Pressure (psi 't5.0 117.O 115.8 15.9 DischarEe Pressure 760.0 753.0 749.O 754.O catalyst (Yes or No)Yes Catalvst Manufacturer EmeriChem EmeriChem EmeriChem Emeri(.)hem # of Catalyst lnstalled 1 1 Catalvst lnlet Temp "F 85't.O E51 .0 826.0 842.7 Gatalvst Outlet Temp "F 474.O 874.0 853.0 867.0 Catalvst Pressure Drop H2o 4.9 5.1 4.5 4.8 GAS 11 10.0 QA/QC Results Equilibration Response Spike Reported Spike Expected Value:250.96 Value: 251.00 System Response Time 45 seconds Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Average:0.00 Average:0.15 Average:0.16 Average:0.04 Average:0.00 CTS Compound Concentration Avg Tolerance Difference between measured and expected Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Oxygen Average:0.48 Average:0.03 Average:0.51 Average:0.39 Average:0.00 Mechanical Response Time CTS Bottle Concentration CTS Compound Concentration Avg Tolerance Ditference between measured and expected 45 seconds Value: 100.00 Value:99.02 s.00% 0.98% Gas, lnc. 12 11.0 D6348 Annexes 1{ The test quality objectives completed for the emissions test are demonstrated throughout Annexes 1,.2,3, 4, 5, 6, Z & A ds lalred out per ASTM D6348-03. All reference methods, pre-test and post test procedures were within acceptable limits. Data generated during the pre-tesl and post-test procedures are summarized below in order of the distinctive Annex. Three 60 minute test runs were performed. The final analyte concentrations are the average of each test run. Data was taken at 60 second intervals. Each 60 second measurement was the average of 600 scans. Propane is used as the surrogate compound for the Annex 5 Spiking Technique due to.Propane being the VOC that is most commonly f-ound in the combustion process of naturalgas. Additionally, the molecular weight of Propane coincides with with molecular weight of VOC's per the EPA. Annex Table 1.2.1 Certified Calibration Bottle Concentrations Botile ExDiration NO2 Ethylene SF6 02P/ol uL;419/50 5t8t2026 99.10 9.12Yo cc1 17503 8t't5t2031 100.00 ALMO209E2 11PAP{J3IJ 21.OZe/o Cylinder # CC142828 Expiration: 12-06-2030 Propane co NO sF6 tsotue value 251.00 501.40 z5z.4u 9.73 Analvzer svstem Response 250.96 505.52 :z5:z.5U 9.74 Percent Ditference O.O2"/o 0.82'/o O.O4"/"O.13olo An nex T able 1 .2.2 Measu rement System Capabi ! ities GAS Annex Table 1.3.1 Test Specific Target Analytes and Data Quality Objectives Compounds lnfrared Analysis Region (cm-1) Expected Concentration Range Measuremenr System Achievable Minimum Detectable Concentrations Hequrreq Measurement System Accuracy and Precision for fest Application (r()zt.](.]{.J-22tJt)0-1200 ppm u.tozol Dom 4 ppm NO 1 8/5-21 38 0-1000 ppm 0.400/ ppm 2 ppm NO2 2too-295td 0-'100 ppm 0.4899 ppm 2 ppm VOC 2600-3200 0-100 ppm 1.8520 ppm Total VOC's 1 ppm perVOC91 0-1 1 50 2550-2950 CH2O 2550-2850 0-100 oom 0.7878 pom 1 ppm lnterfering Compounds . CO is analyzed in a separate analysis region than CO2 and H2O co2 926-1 150 0-10o/o 0o/o nla water vapor 3200-3401 O-22"/o 0.2O"/o n/a * VOCs compiled of Acetaldehyde, Ethylene, Hexane, and Propane. GASMET FTIR FLOW MTR. Figure Annex 1.4.1 Sampling Train The testing instrumentation is housed in an enclosed vehicle which is located approximately 45 feet from the source. A heated sample line (sixty feet in length) is attached to the inlet of analyzer system and the source effluent discharges through the FTIR outlet. {t l H GAS PROBE STACK 14 Sampling Point Locations in lnches 1tj.7'h 2.338 5O"/o 7.OOO E3.3%1.002 TRI.PROBE SAMPLE POINT LOCATIONS AS PERCENTAGE OF STACK DIAMETER Figure Annex 1.4.2 Sampling Points lnterior Stack Diameter (inches): lnches Upstream: 26 lnches Downstream: 92 SAMPLE PORT LOCATION DETERMINED BY DISTAI.ICE FROM DISruRBANCE Figure Annex 1.4.3 Sample Port Location GAS Target Analyte Results (ppm) CO o.1621 NO U.4UUr NO2 0.489S Ethvlene o.378i Prooane 0.4351 Hexane 0.223i Acetaldehvde 0.815i Formaldehvde u. /6/t NEA 7N :rTIIS REF T71 -T'TILS ,l*Li :7 /r y **^ ("rrlTf4n/.i:t_ NEA rtt rMDC#1.- 'un'g*" * Lre{Lref REF 'tc Lcelt r???s Annex 3. callbration Transler standard Expectecl Measured Path Length Validated Ethvlene 100 99.49 4.975 Passed nnex.Iest Procedures ,,.,: Annex Table 1.2.2 Measurement System Capabilities l,arameler Measured Gas uoncentralron {nnm)Path Length EquilrDrailon Time Dilution Factor 7" Recovery Path Lenqth Ethvlene 99.494 497 Spike Direct Propane 250.231 SFTJ 9./'t / CL)504.401 NO 252.596 Mechanical Response Time Ethylene 99.023 1B seconds Analyzer Response Propane 250.956 45 secondsSF69.743 CO 505.515 NO 252.496 Analyte Spike Recovery Propane & SF6 8.15%100.35o/" 7.84o/o 103.14% 7.78%15. /4"k SVStem zero Nitroqen 45 seconds Post Spike System Propane 251 .774 CC)498.999 NO 252.617 SF6 9.751 GAS Parameter Gas Concentratlon Measureal o/o Difference Soecilication Validated Spike Direct Propane 251.000 250.231 O.31"/o +l'2/o PaSS SF6 9.730 9.717 O-13o/o +l- 2'k Pass CO 501.400 504.401 o.60%+l- 2'/o PaSS NO 252.400 252 59tj O.O8o/o *l'2"/o Pass Spike Run 1 via the System Source Output spil(e Averaqe Dilution Factor Expected 70 Recovery Specification Propane 1.45J 31 .086 30.976 100.350%7O'13oo/o SF6 0.000 u.t92 8.151%<1Oe/o Soike Run 2 via the Svstem Source Output Spike Averaqe Dilution Factor Expected % Recovery Specification Propane 21.778 4U.996 3!l.t4!,103.140%7O-130"/" SF6 0.000 0.762 7.842o/o <'|.0"/" Spike Run 3 via the System source output spike Averaqe Dilution Factor Expected 70 Recovery specification Propane 16.t14 40.44'l 34.941 115.74Oo/o 7O-13O"/o SF6 0.000 o.756 l6U"/o 11Oo/o Noise Equivalent Absorbance (NEA) RMS High 0.000058 RMS Mid 0.000038 RMS Low 0.000090 Line Position 0.20 0.15 0.10 0.05 0.00 -0.05 0.20 0.15 0.10 0.05 0.00 -0.05 2092 2069 2046 2023 1999 1976 1953 1930 1907 1884 1861 1837 1814 @ o.oo% Pass Pass GAS The Gasmet GICCOR (Genzel !nterferometer with Cube Corner Retroreflectors) interferometer is specially designed for maximum optical throughput and maximum signal to noise ratio of 7.72 (cm-1) remaining stable with any vibration and temperature changes. The Gasmet DX4000 is a low resolution spectrometer where the aperture is fixed to a maximum angle setting and the detector linearity was tested with an alternate approach. A three point linerarity of the CTS gas was performed and validated. Linearity 172.5586 162.5586 152.5586 142.5586 132.5586 122.5586 112.5586 102.5586 92.5586 82.5586 172.5586 162.5586 1s2.5586 142.5586 132.5586 122.5586 1 12.5586 102.5586 92.5586 695 687 679 672 664 656 648 641 82.5586633 625 618 610 602 15.6889597 Pass The analytical accuracy of the quantification algorithm is satisfied via the results from Annex 5 per Annex 7.6 POST CTS Sy3tem Chock: CTS Bottle Concentration:100.00 u ls uample uoncentratron Averaqe:99.36 urrerence oetween measureo ano expecteo:0.6570 lolerance:5.UU7o HUn UAta ValmaflOn. AUtOilatot0 va ManUal Readlno Valldated (;OmnienlS Run 1 Points 1 & 2on CO/NO/Propane Allwithin 20%Passed Demonstrates no interferences observed. Run 2 Points 'l & 2 on CO/NO/Prooane All within 20olo Passed Demonstrates no interferences observed. Run 3 Points 1 & 2 on CO/NO/Prooane All within 20olo Passed Demonstrates no interferences observed. GAS 18 12.0 Signature Page Job/File Name: Utah Gas Corp;West Water CS; Unit A;JJJJ GAS We certify that based on review of test data, knowledge of those individuals directly responsible for conducting this test, we believe the submitted information to be accurate and complete. Company: G.A.S. lnc. Print Name: Lucas Ennis Title: Emissions Specialist Date:212112024 Company: Utah Gas CorP Print Name, Ttryn Weiner Date: 4t11t2024 Signature: Ti,e: Manager, Air and Sustainability phone Number: 970-307-5032 Company: G.A.S. lnc. Print Name: Travis Hartley Dale:212112024 Title: Director of Stack Testing Signature: Phone Number: 580-225-0403 GAS Appendices GAS Airgas Spike (5 Gas) Airgas Specialty Gases Ai!96 U$4, LLC P722 S. Wentworth A!e. Chiago, IL 60628 Airgs.@m CERTIFICATE OF ANALYSIS Grade of Product: EPA PROTOCOL STANDARI) Part Number: Cylinder Number: Laboratory: PGVP Number: Gas Code: E05Nl94E1 5AC014 cc142828 124 - Chicago (SAP) - lL 812022 CO,CO2.NO.NOX.PPN.BALN Reference Number: 54-402601324-1 Cylinder Volume: 147 .o CF Cylinder Pressure: 2015 PSIG Valve Outlet: 660 CertificationDate: Dec06,2022 Date: Cedifi€ton perfomed in a@ordance with "EPA Tra@ability ProtocolfoaAssy and Cedif€tion of 2012)" document EPA 600/R-12/531, using the assay procedures listed. Analyti€l Methodology dos not requare @r*tron for analyx@l inteferen@. This cylinder has a total analyti€l uncertainty as stated belowwith a conflden@ levelof 95%. There are no signifi€nt impurities which affect the use of this €libration mixtu6. All @n@nt6tions a.e on a rcle/mle basis unlessotheNise noted. The resulis relate only to the items tested. The reporl shall not bs r6produced exepl in lull without approval ofthe laboratory. Do Triad Data Available Upon Request PERMANENT NOTES:Mixture contains nominal 1 oppm Sulfur Hexafluoride as a tracer component. Actual tested value included within the original Certificate of Analysis. Contact the Airgas laboratory if a reprint is required NOTES:Mixture contains nominal 1 0ppm Sulfur Hexafluoride as a tracer component. Actual tested value included within the original Certific€te of Analysis. Contact the Airgas laboratory if a reprint is required. SFO Results: JMR137-9.73|PPM. i r : l Approved for Release Page I of I i.e. Compon6nt ANALYTICALRESULTS Requested Actual Protocol Total Relative Concentration Concontration Method Uncertainty Assay Dates NOX 250.0 PPM 253.0 PPlu Gl +/- 1.2% NlsTTraceable 11128t2022,12n6n022 NITRIC OXIDE 250.0 PPM 252.4PPM Gl +/- 1.0olo NlsTTra@able fnBP022,12l06DO22 PROPANE 250.0PPM 251.0PPM G1 +/-0.7%NISTTraeable 11EO2022 CARBON MONOXIDE 500.0 PPM 501.4 PPM Gl +/- 0.6% NIST Tra@able 11f2912022 CARBON DIOXIDE 5.000 % 5.025 o/o G1 +/- 1.4% NIST Traeable f nBD022 NITROGEN Balan@ CALIBRATION STANDARDS TvDe Lot lD Cvlinder No Concentration Uncertaintv ExDiration Date od29,2026 Feb 20.2o2o Feb 18, 2023 Ma( 17,2027 Jul 03,2024 May 14,2025 NTRM 200603-31 E80113125 250.3PPMNlTRlCOXIDE/NITROGEN +t-0.80/o PRI\il 12386 D685025 9.9'! PPM NITROGEN DlOxlDE/AlR +l-2.oo/o GMIS 401423838104 CC505590 4.373 PPM NITROGEN DIOXIDE/NITROGEN +l'2.0o/o NTRM 200602-13 6162697Y 243.3 PPM PROPANE/AIR +l-0.5o/o NTRlil 130'10109 KAL003925 495.4 PPM CARBON MONOXIDE/NITROGEN +l-0.6% NTRM 13060423 CC41 3685 7.489 % CARBON OIOXIDE/NITROGEN +l- 0.66/0 ftesRM NTRM PRM orRGMnoledeboveisonlvinrefercncetotheGM|S6edintheasavandnotertoftheanalvsis. ANALYTICALEQUIPMENT lnstrumenuMake/Model Analytical Principle Last Multipoint Calibration Ni@let iS50 AUP2010242 CO,1 SIEMENS ULTRAMAI 6E N1J57OO Ni@let iS50 AUP2010242 Ni@let iS50 AUP2010242 Ni@let iS50 AUP2110277 FTIR NDIR FTIR FTIR FTIR NoY 07,2022 NoY 28,2022 Oec05.2022 oec05.2022 Nov 07, 2022 GAS AiruAS 9o/o O2|NO2 Airgas Specialty Gases Airgas USA LLC 525 North Industrial lnop Road Tooele, IIT 84074 Airg6.conr CERTIFICATB OF ANALYSIS Grade of Product: EPA PROTOCOL STANDARI) Part Number: E03N190E15W0003 CylinderNumber: CC419750Laboratory: 124 - Tooele (SAP) - UT PGVP Number: 872023 Gas Code. NO2,O2,BALN Reference Number: 1 53-402732424-1 Cylinder Volume: 145.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 660 Certification Date: May 08, 2023 Expiration Date: Mav 08. 2026 Cedifl€tion performed in a@rdance with "EPA Traceability Protocol for Assy and Cedifi@tid of Gasus Calibration Shndards (May 2012)' document EPA 600/R-12J531, using ihe assay pocedur6s listed- Analytiml Methodology does not require cor4tion for analyti€l interferen@. This cylinder has a total analyliml uncedainty as stated below with a confiden@ level of95%. There are no signili@nt impuiltes which aflect the use ofthis calib6tion mixture. All @n@nbations are on a mle/mle basis unless otheMise noted. The Esults relate only to the ilems tested. The report shall not be reproduced ex@pt in full without approval ofthe laboratory. Do Triad Data Available Upon Requast Approved for Release Page I of I Component ANALYTICALREST]LTS Requested Actual Protocol Total Relative Concentration Concentration Method Uncertaintv Assay Dates NITROGEN DIOXIDE 100.0 PPI\il 99.10 PPM G1 +/-2.0% N|STTra@able 05n1n023.05n8/2023 OXYGEN 9.000 % 9.119 Vo G1 +/- 0.6% NIST Tra@able O5lO2n023 NITROGEN Balan@ CALIBRATION STANDARDS Type Lot lD Cylindor No Concentration Uncertainty Expiration Date GM|S 1534012021601 CC502090 PRI\rl 12389 D685050 NTRM 14060629 CC436987 The SRM NmM PRM or RGM noled above is ontu in ,IOO.5 PPM NITROGEN OIOXIDE/NITROGEN 1.1'/O 99.0 PPM NITROGEN DIOXIDE/NITROGEN 1.ovo 4.794 % OXYGEN/NITROGEN O.4O/O ce to th. GMIS us.d in lhe asev and not Md oftho anatusis Oec'17,2024 Feb '19, 2020 Oct 29, 2025 lnstrumonUMake/Model AIIALYTICALEQUIPMENT Analytical Principle Last Multipoint Calibration FIIR 02 Paramagnetic (DIXON) May 03, 2023 Apr 06, 2023 MKS FT|R NO2 018143349 Horiba MPA-s10 U,603MM58 02 GAS Airuas. a Alr Lhllde mpey Ethylene Only Airtu Specialty GroeB Airgs USALLC P722 S. Wentrcfih Ave. Chi@go, IL 60628 Arrgr.om CERTIFICATE OF ANALYSIS Grade of Product: PRIMARY STAIYDARI) GREAT PLAINS ANALYTICAL SERVICE,Customer: Part Number: Cylinder Number: Laboratory: Analysis Date: Lot Number: x02Nl99P'lsACVH8 cc1 17503 124 - Chicago (SAP) - lL Aug 1 5, 2023 54-402811378-1 Expiration Date: Aug 15,2031 Reference Number: 54402811378-1 Cylinder Vofume'. 144.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 350 Primary Standard Gas Mixtures are traceable to N.I.S.T. weights and/or N.I.S.T. Gas Mixture reference materials. Component ANALYTICAL RESI'LTS Req Conc Actual Concentration (Mote %) Analytical Uncertainty ETHYLENE NITROGEN 100.0 PPM Balance r00.0 PPM +l- 1o/o Notos:GREAT PLAINS ANALYTICAL, CERTIFIED BY FTIR Sldniftrh 6h fil. Approved for Release P.ga I of I GAS BIP Airgas. a Alr Liqjdo mp8rry AirguMid South region Airg6 USA LLC 974r E. S6th St. North Tirs, oK74u7 Airt6.@h CERTIFICATE OF BATCH ANALYSIS Grade of Product: BIP-BUILT IN PURIFIER Part Number: Nl BlP300 Reference Number: 29-400672389-1 CylinderAnalyzed: TW05-867349 Cylindervolume: 304.0 CFLaboratory: 106 - Tulsa Fast Fill (SAP) - OK Cylinder Pressure: 2640 PSIG Analysis Date: Feb 10, 2016 Valve Outlet: 580 Component ANALYTICAL REST]LTS Requested Pudty Certlfled Concentration NITROGEN OXYGEN WATER TOTAL HYDROCARBONS CARBON DIOXIDE CARBON MONOXIDE Permanent Note3:This cerl indudes values from the'fill" side and is not representalive ofthe "use' side purity. Contad an Airgas Sales Representative for this information. Cylinder! ln Batch: 4263617y, Tt 04671107, Tt Offi31574, T\ 0$€05966, TVV0$867349, T\4i05467538, T\ O5€67578, T\A'0fi81687, TW$.881820, Tt o!920689, T\ ,05.920760, TW)5848694, TW05867441, Tt /05897265, T\M5897512, T\ 05920678, TIA/05920686, T\ O5920695, TW5920781, TW05920874 lmpurities verified against analytical standards traceable to NIST by weight and/or analysis. Approved for Release P.gp I of I 99.999 % 1 PPM ,I PPM 0.1 PPM 0.5 PPM 0.5 PPM 99.999 % 0.94 PPM 0.058 PPM 0.1 PPM 0.235 PPM 0.235 PPM GAS Airgas il Air Uquido compay 210h 02 Airgas specialty cses Airgas USA LLC 525 Noth Industrial t op Road Tooele, uT 84074 Air8s.@m CERTIFICATE OF AT{ALYSIS Grade of Product: EPA PROTOCOL STANDARD Part Number: Cylinder Number: Laboratory: PGVP Number: Gas Code: E02Nl79E1 5A00Bl 41M020982 124 - Tooele (SAP) - UT 872022 02,BALN Reference Number: 153-402603461-1 Cylinder Volume: 146.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 590 Certification Date: Nou 28,2022 Date: Nov 28.2030 Certifieton perfomed in amrdanco wiih 'EPA Traceability Prolocol for Asey and Cedification of Gaseous Calibration Standards (May 2012)' 600/R-12y531, using the a$ay prccedurB listed. Analyti@l Methodology does not require correction for analytical interfercn@. This cylinder has a total analyti€l uncedainty as slated below with a @nliden@ level of 95%. There ar6 no signili€nt impuriliss which aflect the use of this €labration mixture. All on@ntrations are on a mle/mole basis unless otheNise noted. The results relate only io tha items tested. The repod shall not be reproduced exepl in full without approval ofthe laboratory. Do Triad Data Available Upon Request Approved for Release Page 'l of I Component R6quested Concentralion ANALYTICALRESI.'LTS Actual Protocol Concentration Method Total R6lative Uncertainty Assay Dates oxYGEN 21.000k 21.020/o NITROGEN Balance G1 +/- '1.0% NIST TGeable f nBD022 CALTBRATION STANDARDSTyp6 Lot lD Cylinder No Concentration Uncartainty Expiration Oate NTRM 09061434 CC282492 22.53 "/" OXYGEN/N|TROGEN 0.40h Mav 13. 2025 lnstrumenUMake/Model ANALYTICAL EQUIPMENT Analytical Principle Last Multipoint Calibration Horiba MPA-510 V1603Ml!158 02 02 PaEmaonetic (Mason)Nov 17. 2022 GAS Tri Probe Certification #es Part Number: Laboratory: Analysis Date: LOT Number: SN: Great Plalns Analyucal Servlces 303 w gd st Elk Ctty, OK, 73644 [580)225-0403 Fax: (580)225-2672 CERTIFICATE OF ANALYSIS Grade of Product: CERTIFIED STAI{DARD-PROBE 145 GAS INC. 3t312022 A 22P.145 Reference 22 Number: Stack Diameter'. 14" Target Flow 3Umin Rate: Number of 3 Points: Product performance verified by direct comparison to calibration standards traceable to N.I.S.T. *The probe listed on this form meets the multipoint traverse requirement of EPA Method 7e, section 8.4 as shown in the accompanying data. Method 7e, section 8.4 states that the multipoint traverse requirement can be satisfied by sampling via "a multi-hole probe designed to sample at the prescribed points with a flow +/- l0 percent ofmean flow rate". ANALYTICAL RESULTS Total Flow (Vm) Measured Flow Measured Flow Mea3ured Flow Mern Probe Port A (Vml Port B (Vm) Port C (Vm) Port Sampled lDelta o1l lDelta o2l lDelta o3l F'low (I-lmI Rul Rm2 2 LPM 4 LPM 0.720 0.660(8.00a) (-1.00a) l.4t l.3t(7.09A) ({.sla) 0.620 0.($7 (-7.00a) 1.23 1.32 (-6.58A) 'Calibration conducted in accordance with Emission Measurement Center Guideline Docrment - EMC GD-031 3t3t2022 DateApproved for Release Probe size: 14S o+rrtD sreO eAo- LYJ UNITED STATES ENVIRONMENTAL PROTECTION AGENCY RESEARCH TRIANGLE PARK, NC 27711 March 15,2021 ,ro I 1L5 r)t Atfr ouAt llY r][ANNtN(i AN[] IiTANI}AI{t)T; Mr. Jordan Williamson CEO GAS Inc. 303 W. 3ra Street Elk City, OK73644 Dear Mr. Williamson: We are writing in response to your letter received on September 17, 2020, in which you request the approval of alternative testing procedures. The EPA's Office of Air Quality Planning and Standards (OAQPS) is the delegated authority for consideration of major alternatives to test methods and procedures as set forth in 40 CFR parts 60 and 63 under which your request must be addressed. GAS Inc. is requesting a change to one of the test methods, ASTM D6348-03, used for conducting performance tests to determine compliance under 40 CFR part 60, Subpart JJJJ - Standards of Performance for Stationary Spark Ignition Internal Combustion Engines (Subpart JJJJ) and 40 CFR part63, Subpart ZZZZ -National Emissions Standards for Hazardous Air Pollutants for Performance for Stationary Reciprocating Internal Combustion Engines (Subpart ZZZZ). The change being requested will be used to check detector linearity of the Fourier Transform Infrared (FTIR) instrumentation used to conduct this method. Specifically, you are requesting that the procedures of section 8.3.3 of Method 320 (40 CFR part 60, Appendix A), another FTIR-based method allowed under Subparts JJJJ and ZZZZ, be used in lieu of section A6.4.1 of ASTM D6348-03 when conducting testing using ASTM D6348-03 under 40 CFR part 60, Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. In your request, you state that this alternative linearity check procedure will produce consistent results when utilizing either Method 320 or ASTM D6348-03. Additionally, some FTIR instrumentation does not allow for reducing the size of the aperture in the instrument and, thus, it would not be feasible to properly conduct the entirety of the ASTM D6348-03 method in its current form using such an instrument. Based on our understanding of FTIR instrument principles and recognition that the requested alternative determination of detector linearity is both technically sound and contained within Method 320, we are approving the requested change. We believe that this altemative is acceptable for use for use in testing all engines subject to 40 CFR part 60 Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. Also, we will post this letter as ALT-l4l on EPA's website (atwww.epa.gov/emc/broadly-applicable-approved-alternative- testmethods) to announce that our approval of this alternative test method is broadly applicable to engines for the purposes of meeting Subparts JJJJ and ZZZZ. If you should have any questions or require further information regarding this approval, please contact David Nash of my staffat glg-541-9425 or email atnash.dove@pa.gov. STEFFAN Dlgltrl$rlgned by JOHHSON 1201t.03,15JOHNS11i?850 -0{'0S Steffan M. Johnson, Group Leader Measurement Technology Group cc: Sara Ayers, EPA/OECA/OCA{AMPD, (ayres.sara @epa.gov) Melanie King, EPA/OAR/OAQPS/SPPD, (king.melanie@epa.gov) James Leather, EPA Region 6, (leatherjanes@epa.gov) David Nash, EPA/OAR/OAQPS/AQAD, (nash.dave@epa.gov) Sincerely, Lucas Ennis GAS 580-225-0403 info@gasinc.us Type of Sources Tested: Stationary lnternal Combustion Engines. 4 Stroke Rich Burn Engines. 2 Stroke & 4 Stroke Lean Burn Engines Stationary Natural Gas Fired Generators Stationary Propane Fired Generators Gas Fired Boilers Types of Analyzers:. Gasmet DX4000 FTIR. Gasmet Portable Sampling Unit with Zirconium Oxide 02 Sensory. Testo 350. Flame lonization Detector Qualifications: Trained, studied, and fully demonstrates compliance for emissions testing via data collection outlined in the following Reference Methods:. EPA Method 1 & 1A - Sampling & Traverse Points. EPA Method 2 &2C - Velocity & Volumetric Flow Rate of a Gas Stream. EPA Method 3A - Oxygen. EPA Method 7E - NOX. EPA Method 10 - Carbon Monoxide. EPA Method 25A- Volatile Organic Compounds. ASTM D6348 - Extractive Fourier Transform lnfrared Spectroscopy Conducts emissions testing on a weekly basis including, but not limited to, the following test types: lnitial Compliance, BiennialCompliance, SemiannualCompliance & Quarterly Compliance. Alltests performed are in accordance to any and all Federal & State requirements as applicable (i.e. JJJJ, ZZZZ, 106.512, 117, PEA, etc.). Performed testing in Colorado, Utah, Wyoming, North Dakota, Montana, Kansas, New Mexico, Oklahoma, Texas, Louisiana (land and off-shore), Arkansas, Ohio, Pennsylvania, West Virginia, New York, Kentucky, & Mississippi. . Quarterly Performance Reviews covering ongoing changes with Federal Regulations, State Compliance guidelines, & site-specific safety certifications. 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' o o o=NF Z- d ool IFoag *eOF za oe o> oa o:oeg ::N]E N :@ NN@@qoodoOoqoooco : ooe? rN 'o.o @ :d:o .N:' : :ioJO :O'c i : @NAio@@oc?@oqoaNqo o@$rqu 2 .t r 3 9 t- (o co oi " i (O = 9 \.o @O NO 66 .E : " j d Nr 5E E (v ) , P P ,m - o . r ,9 ? q? .N N Ct $ NN Jo - :E . S S NN .A I A I ON @ O O $ O O O $ r $ N @ T O N N O O @ @ @ @ @ NT F N O N N T $ O V o t @ $ $ $ 6 O O N N o a N N v qq q q q q q q q q q q q q q q q q @ @ @ @ @ @ @ @ o o o o o o o o o 6 o 6 o o o o o o o o ri d ri r i 6 d d .6 AO Q @ T @ N O O @ $ N O @ F @ o @ N $ 0 O N r @o @ N O N $ @ O O O @ O N T O o O O O @ @ @ ! @ F N cq o q o q o q o q q o q q o q q q q o q q q o q q q o q q q 0q q ol oc |. i ^r oo o o a o a o o o e o o o o o o o o o o o o o o . ! d t_ = N q) $ lo \ C! o O r N o s 0 @ N o o O - N o { Lt ) @ j , in I I I I I q I 9 : . r . r . r . r . r. . . : . I . 9 ! 9 1 9\ l S l $ l $ l 9 l ! NN N N N N N N N N N N N N N N N N N N N N N N O ? 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IF8* q q q q q q c g q c q I c g c q q q q q q q q q q q q c e8 P q @@ @ @ @ @ @ @ @ @ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ ; ; @ $$ $ $ s 3 $ s s s s $ s . + s s $ $ $ $ $ s $ $ $ $ $ $ { = g $ @@ @ @ @ @ o o @ @ @ @ @ @ @ o o @ @ 6 o o 6 o 6 @ @ @ o d b 6 o OO O o O O O O O O O OO O O O O OO O O O O O O O O OO 6 N S@ r N O N @ $ O N - O @ O O N O O - O O @ O V @ O @ @ @ 6 d X '. o) g q q q - r. - c! 1 c. l a a 1 q \ \ ol q c? n - n 1 c? n q a c 9 6 @ O @ 6 o @ @ @ @ @ @ @ @ @ @ @ @ @ O r O N N N N N N r -! ? e Nr N S o o o o o O O O O oo o o o o o o o o o oo o o oo o o o o o o o o o oo o o - OO N N N - O N O r @ @ $ O @ O r @ O r N S @ O O O O F N O o X oN o $ N@ o o - @ o @ - N @ 9 o @ r N o o N r q a \ c ? \ i, j @ d Ri A i ; oi c i o c i d o i c i d c i d d N $ ; d @ d ; d ei N o N od i oo o o o 9 0 $ $ $ v $ $ $ t $ s 3 o N N N o o o o N N os Y :. $O O O O O O O O O O O O O O O O O O - O O O O O O O o O - o O ro o o o o o o o O O O O O o o o o o o o o o o o O O O O @ o O n q c q q q c q q q q q q q q q q q q q c q q q o o o o o o o o A A A A O O O O O O O A A O O O A O O A O O A O O CJ C J C J d d C , : .. O O 0 N r @ @ S A N O N Q @ @ - o r o N @ N S N O O O N O - O 6. O OO $ @ N N O O O N N O O @ N O O $ O N O O O T @ @ O O O O N O q q \ q \ q q q \ q q q q q q \ q \ a q q \ q ot N N @ o o o |: :o N N N N N N N N N N N N N N N N N N o 9 N N N N r u ci c i A J a J o i .. i , : o ,] O N O O r @ @ N O @ O @ V @ O O O O N N O N O N O O $ @ N 6 6 l O OO @ O N @ N O N O N S o O @ N O O O N O O @ r O N @ o N a u? a (? a a q a n u? q q q u ? u ? q a a q \ - o. l c l '. ' . q '. 'q c? q o ? :q o o o o o o o o o o o N -t o l VO O O O O $ N@ N N $ O N O O r O O O O O N N T O o @ @ o N NN N O @ O N N O @ O N @ r @ O O O @ O O N O O $ r O O N t s @ ;A q o q o q \ q q q - q C -. '. n a? '. q q q' . q 1 (| q a q S qq A u? oq r & ra o o o o o r o - @ @ s o N o o c j d A i d @ t N- T N N N N N N N N N N - r S N @ @ @ O @ @ r @ O ts N @ O N O O O @ N @ @ V O O O O + N '* OO O O O N $ T O O N N O O O @ @ O O N N $ O @ @ N @ @ N O t s J q q q o q o l a q a c9 - q s l q a sl \ u2 o l q u ? q q a ol o l @ o o 6 qq d ro o o O o o @ o @ @ @@ @ @ @ N N o@ $ N r oo o i S ! 9q A 3 g ; s v s $ $ $ $ $ $ $ $ $ $ s $ $ $ $ $ N N N N N N N N @ @ - ' , - ' , oo o o o o o o o o o o o o o o o o o o o o o o o o o o o Q Q N -- 8 8I I E E I I I I E E E I I I E E E I E E E E I I I I 8 E q 5 y) oo o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o \C' oo o o o o o o o o o o o o o o o o o o o o o o o o o o o a Q o oo o o o o o o o o o o o o o o o o o o o o o o o o o o o 9 9 0 c q q q a q c q q q c q c q q q c q q q q q q q q q q c q qq q OO O O O O O O O O O O O O O O O O O O O O O O O O O O O O < ) O OO @ O @ N O O N @ O @ @ @ r $ O O - O @ N O N O O O @ O N F O O$ N $ O $ @ N - @ O O $ O - @ N O @ O r N O - @ $ N N N 6 N O \ q q q q s ? q (| u? u ? q q q q \ u? q q q a q q o q q q q q a q 9l o TO O O o o O o O O O O O O O O O O O O T O O O O O O O O o o Ci OO O N O $ @N o r N N Q o O O O N N @O r @@ O @ N Q No @ @O O F O $ O N r N O o @ o s N @ N N @ o @ N $ O O ( o > < o) o) g c q o q ot - q q q q r . q o t q q ot .: q q ' : - q o q a q q ' . r q 5 NN oo o N N o N N N N o o o oN N@ o @ o o @ o q i q i o j oj 9 : A FN aa O O o O o O O O O o O o O O a O O a a O a O a o O O O o o O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O o - 'O q q q q q I q q q q q q q q g q q q q q q q c q g o o o o q q ,o o o o o o o o o o o o o o o o o o o o o o o o o o c i c i c i c i o o .c i oQ a o a o o o o o o o o o o o o o o o o o o o o o o o o Q Q a oo o o o o o o o o o o o o o o o o o o o o o o o o o o o I a o q c c q q q q q q q q q .q q c q q q q q q q q g c q q q q q q :c o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o , :o : o@ o o o o N N N N @ o o o N N $ @ s o o o N o @ @ @ o s X * r@ O O N T O O O N N O F N O O O @ So N O s s O $ N N N X - ' O \ Q I e \ q { .1 q i i q o bo @ o a, 6 q r c .q a ul N ' N er - :o j o @ @ o N N @ @ o @ o o - d j ; ; ; N + 5 I E K N P : 3 S E I :g Qq ) q ) o N O o O O O O O O O O $ s s oo o 6 n d 6 o o + < f 9 o el dEo& o!T' NEo& . r2 rE_o o -l () E !o o s= NEo&*lOFO- d o .i IEz- d ool NF Z- d o E E ts fr I I X d I P E N A E fr E A ! 8 8 R E B s s 8 I 8 s I & , s O 4 Ei ,c oi q c q ( '. c { q d A E 6 i 8 8 S S I 3 S 3 I I 3 i r, i .o :3 =: 9 P = I P : P P : : P P P P ct c i - - - oi Ai ai oi d d No ct o O o N O O r O O $ O O O @ r N N o O O O N N - F N O @ O E A . ^ oo N @ @ o o N o o o o o o o @ o N$ o $ $ oN s o o o o q ! ! 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O '1 r OT O o O o O O O o O O O O O O O o $ o @ N @ @ u ? q a ; : q ft oo d c j c j c t o o o o d o o o d c j o c t d o o o o o o o o o - o *E IEoag .eOF Z- d -ol o2 2C -oi o= () E o FO O O N @ N O O @ O N O $ @ N @ @ O O @ N N N O $ r O O SO q ) - @ @ @ N @ O @ o o N @ N n O @ @ O r o r O r O N S X U N q q q \ q q q q q q q q q q q q q q q a ? q? a a n n n n n n u? q o oo o o 6 o o a @ o o a o o o o o 6 o o @ o @ o o d ( i ( i d o o d N- $ N - @ S N $ @ $ F N O N F @ T N N O T N N O O N $ N , ^ N S O O F O O F OO O r O@ O O @@ @ N S N O@ N N O@ O + o a ot o t q q ol q q o q q q q c cc oc c q Q \ q u ? q a s @ o o o 6: . . i - oo o o o o o o o o o o o o o o o o o o o o o o o o ; ; ; i 3 : _= = r Oa N: < Iv $O O N @ O O T N O $ A @ N @ O O T N O $ OO N O O T N O *A \ N c? q? q ? g l I q? : n a s a f Y a a n y? Ll ? ct c 2 'a g? y ? {? o o o o o p, Y ' := N N N N N N N N N N N N N N N N N N N N N N N N N s si c i c i oa 4 , E qj := -o v$ $ $ $ $ $ $ $ $ $ s v $ $ $ $ { s s $ $s $ $ $ $ $ $ f tr r s NN N N N N N N N N N N N N N N N N N N N N N N N N N N N T -N oo o o o o o o o o o o o o o o o o o o o oo o o o oo o - (u o N N N N N N N E E E E S! S ! E S! E S! E E SY E S! E E E S! S S! S ! M A NN N N N N N N N N N N N N N N N N N N N N N N N N N N N N < NN N N N N N N N N N N N N N N N N N N N N N N N N N N N O J N^os () L iq q q q q q q q q q g g q q q c q q q q q q q q q q g q c c I :d d c t c i c i o o o o o o o o o o o o o o o o o o o o o o a a a Q .@ 6 6 @ @ @ @ @ @ @ @ @ O @ @ @ @ @ O O @ @ @ @ O @ @ @ @ Q a :g 3 8 e 8 8 P I 8 R 3 I R R ? 3 e I R 3 8 8 R 8 8 ? 8 ? I I E :< i A O cC Q \ \ oC Q A q ot q o q q o q q o q o q \ \ ot q q a oq q q oq q q' :o o o @ @ @ @ @ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ @ o o @ @ @ o :o o o o o o o o o o o o o o o o o o o o o o o o o q q q e q 8 cd o d d o d d d d d d c j c j d @ d qi ci c i d c t d d d d d qj o @ @ @ @ ; is $ 'f $ { $ $ v $ $ s $ t $ $ v $ s s S S S S S S $ s t S 9 : ; '@ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ @ @ @ @ o @ @ @ @ d6 :8 8 8 8 I 3 I 3 I I I R ? R e ? 3 R ? 3 I e 8 I I I 3 3 I I a :o ; ; O O N O O N $ N r N N @ O o O O N O O (o O 6 O $ r N N t @ d o i : .j , j . j : oj N N s i ^i - - - ; ; ; - - - - ; ; ; - - - -i :N 6 d o o o o o ci o o o o o o o o o o o o o o o o o o o o o o :O O O O O O O O O O O O O O O O O O O O O O O O O Q O A a Q { :O o @ @ @ O o o 6 N o o o o N @ @ @ r $ N - N @ I A > A c) .s I N :' : q q q q q c ! \ '. 02 o ? \ q \ - og \ '. q \ q q '. a sl cq ol o! a o? q :s N o o s o - N r o @ o r r $ r @ o o o $ o N I 6 S 3 I 5 :o N N N O .) O O O N N O O O O O O O O O O O O O O :,8 8 8 I 8 I 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 I I :Q E O E A q q q q q q a a q a q e q a q q q q e q q q q q q q .o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o o@ o $ N @ O - O N oo o N O$ N - Oo N O O $ O N @O O NN s e E s s 3 B I3 E * 3 S R 5 8 5 R 3 3 b E R E E P b 5 I S8 oi N oi a i c i c i a i d oi o i oi o i o i d ci d oj r i oi ci d Ai A i c i N ci o i o i ei oi ri $ O r O r N $ N @ O @ $ O O O ti O $ r N r O N O @ Q ! 9 q N C o o N @ 6 o N @ I o - @ o N @ t U) N @ $ N o o N @ @ u) c - ) (? a q\ a q' : i q q o g o? q q n c? c ? n q n a q q u ? \ q (? 02 c ? n (| a q q a q? ro o e o o o aj a j o o o o o o o o o o o o o o o o o cj a , d rj r i o i s g 3 P 3 g 5 3 3 b 3 ft 3 S R 3 P 3 E f, R b S P 6 =' - o o o 6 ln o? q ': u? \ q? q I q q q \ oq - q u ? q q q . q a ? q oq E 5 q E E \ ]: N N N I R R E N N N R N il N N E & & R R E N N E E N & & & E ,E 3 p R N S $ R R 3 R 3 \ 3 P : 5 3 $ 3 I E 3 5 3 I b s I 3 E 6, ci ; - d ; ^i o d a : : d N o; "; s d N + oi N o qi r: ( od @ d Nl > :+ N @ @ @ @ (i 6 6 F N s 6 io 6 @ @ @ @ @ @ o @ @ @ (o @ o @ @ @ :i6 o o o o o o o o o o o o o o o o o o o o o o o o o o o o o Q iE E E E E E E E E E E g E 8 8 8 8 I 8 E E E E E E E H E E E E q :- o :'o o o o o o o o o o o o o o o o o o o o o o o o e o o o o a Q .- - - 6 - 6 - - 6 - - 6 6 o o o - - 6 o O O O O O o o o o o I :- - - - - - 6 - - - 6 6 6 o - 6 o - o O o o o o o o o o o o I - - - - - - - - - 6 - - - 6 o o o c j o ci c i d o d o o d d c i o c i :o @ r o N O r @ @ N o @ $ @ N N N @ N O @ 3 @ N @ O O O O o @ :3 I 3 b 3 e 3 E E 5 I 3 a S 3 s 5 E S b 3 8 E 5 I 3 b E 3 5 E o - : o o o o ci c i - - d - d c i c i d o o ci c i - ci - - d d o o o o ,t o @ N r o o s a o o o o r @ o E q) !9 o - @ r N : t e A ! , @ Q q9 's 3 u 3 I E 3 ? i E q E s N i E I I q + 3 q q E ff E B E q E E s N @ @ @ @ o o o @ @ @ @ o o o o o o o o o @ o o o j o f d d ci p l @ o o o o o o o o o o o o o o o o o o o o Q a Q Q oa Q a a E r I I I I I I E I I I I I 8 I I I I I E E E I I I I E I I I EE OO O O O O O O O O O O O O O O O O O O O O O O O O O O O O E E I I E I E E E E I B E E E I E I E I8 8 8 8 8 q E E E EB qq q a 6 Q q e q c q c q q c q q q q q q g q q o ( o o o o o a a o o a a o a o o o o o o o o o o o o o ci d o d o N H H H $ p E 3 p E H B p e E $ p H $ H p h p il q N p I il pt E R s * i l e e e e S; B B s i r s R B B f , B B E E ts B B I3 $ - (j ( + d di - < t + + 6 < $ $ < i n s s o < $ $ v $ : : : : : E, E O :o r o o o o O N O O N F O O :+ O $ O o O O N c g @ O @ N @ O N g) :E E E E E E E ? 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O Cn qq q q q c q q c q qc q q g q c gq qq q q c o . z OO O O O O O O O O O O O O O O O O O O O O O O O \(, oo o o o o o o o o o o o o o o o o o o o o o o o oo o o o o o o o o o o o o o o o o o o o o o Q a qq q q c q c q q c q q q c q q q q c g c q q q q OO O O O O O O O O O O O O O O O O O O O O O O O N@ 0 @ O O N O @ @ N N O - r O O N r @ o $ O @ @ @O @ o o $ O N O F j @ N O N - N r r O 0 O o $ N q \ \ q q q q q q \ q q q q q \ q q q a or q o ? q q OO O O O O O O O O O O O O O O O T - o O O O O O r@ @ N O N O O O O @ N O N O n O O $ O O N N $ N @@ O N N r r N @ O O O A O @ O @ O @ N @ O N O O \ oq q q a l ' . q '' ' . e? c ' t c, . 1 q g g q q q \ q s l q ' . o q ol _N N @ O O O O O O O O O O O O O @ @ @ @ O @ O @ @ OO O O O O O O O O O O O O O O O O O O O O O O O ]O O O O O O O O O O O O O O O O O O O O O O O O O OO O O O O O O O O O O O O O O O O O O O O O O O .i c t c i d c i c i d d c i c i c i c i d c i c i d d o o o o ct c i c i o RH B g H i l E g $ S H R P P R B g $ k B S E X g $ o o cj o o O O o '_ N o r F o r o d ; ; ; o c; c j o d ro @ o N o o @ o s o o @ @ @ $ $ N O O N O @ rO $ n @ O @ 9 O O O O O N T O @ O T N O N N N O sN o o + N $ o @ o r o $ @ o @ $ @ N - o o @ v N + + c i + 6 d d i x r N N @ 6 + ci @ 6i $ d d d o o qi Co o o o o o o o o o o o o o o o N N N N N N o N N 'E o o o o o o o o o o N o o o a a ., ql o $ N r r @ 68 8 8 8 8 8 8 8 8 8 5 8 8 8 8 8 3 9 e + 3 3 3 f , 6 (o d d o o o o o c i c i c i d o o d o c i o o o o o ct c i c i o oE- 0 N N r $ o N O o o @ N o O @ $ o $ - D o o o N J@ o @ @ @ O @ @ o @ @ @ @ @ @ @ $ o o o $ o $ s o .E 6 r i r j r ; rj d d ri 6 r ; ri r , r i d 6 6 r t rt d ri d d d 6 rt tr o @ N N s a o o @ N r N N o $ s $ a o N N o N =- N O o 0 @ + N @ @ o O N @ N N O F F N @ S $ S $ O@ @ @ @ @ @ @ @ o @ @ @ @ @ o @ @ 0 o o o o o 6 0 rn c i o o o o o d d c i o o ci c i c i c i o o o ci c i c i o o o o -+ o o o 0 6 o 0 @ o o o o o o o o o o o o ' + s + + + + + + + s + Lb . ; , b 6 .b . b , b , b i' i .i j L i ' j , b , b , b CY )E $ $ $ $ s $ s $ $ $ $ s $ s s s ' $ $ $ $ v $ $ s $ =. N N N N N N N N N N N N N N N N N N N N N N N N N Jo o o o o o o o o o o o o o o o o o o o o o o o o NN N N N N N N N N N N N N N N N N N N N N N N N tt , < < < < < < < sr E sg s! E E E E E s! ! ! s ! E E s! q q q q q E E q q s N- N - N N N N C \ i O J N N N N N N N N N N N N N N N N N OO O O O O O O O O O O O O O O O O O O O O O O O -- - o o o o o o o o o o o o o o o o o o o o o o o .o o o o o o o o o o o o o o o o o o o o o o o o o o o o o ci d d c i c i d d d c i d d c i d d d d d c ; d d ci o o o @ @ $ N @ N t s I 0 O @ O @ ! ! ^ ! ! ! o + o { N O '- + 6 N - O i- N $ ; o ; o @ + o 9 q P N @ I E Y Q - - q q e qi a A i C <1 e 6' , 6 N @ I c 1r a : q I e I o@ r N N @ o N N N $ N s d t @ 3 R R I 3 h I t R oo o o o o o o r o o o o o o o o @N o @ N@ O O X oN . 9 e x -; t s o ^ : $O N - N6 Y so a . ! H ,4 . ; o 6 5V 6 6 o oo O O o 8 8 EE I OO O O O oo O O @ I8 B B 3 oo o o o $N N O A NN O O $ 66 oo o o c ; NO F ? o6 I <N - o ) : ;; N A , dl i I8 8 8 8 d c i o o :d a. oo O O O I8 E E 8 o- O O o i E Bg e o6 : @@ N O oo N O ooR b B3 R o@ q - - oo o N A <6 0 t s ;a o 6 >A ! N 6N H Pi oo o OO o o O a a & E s q9 d d Y OO O .lOF zA g; o2 o. o2 vo g oF oEoE NEo& . u2 TE -o-iOF Id o sENEo& .lOF (/ ) a o -l IFZ- d qol NE z. a ool TEod o NO o 6 a O@ F O N oQ 9 a q 66 Q o o OO ss r N } : @@ @ o \ @@ Y =: 9 9 N o ? g d, + I + + + i < l- + -: 6 N $ E: E d S S M. S s! s ! 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'. - 02 NO O O O N @ O O O N @ O O O O O O O O O O OO O N T O - O N O O O O T O N O @ N N N N r@ N @ O @ O O @ N @ @ O O N O t s O @ N r $ - (: n a? a ? q o? q cq ol q c q \ - o) Al 9 \ ol q q q oo o o o o o o 6 0 0 6 0 0 n o o o o @ o o OO r $ O O @ O @ O O O O T $ N @ O O O $ N N@ O N O O @ $ F $ O N O O O O O N $ N @ @ e? a q A t q n q q a q u ? \ a a? - \ q I n a? q ol ON T N N O $ N t { O { O O $ N N r $ $ $ $ NN N N N N N N N N N N N N N N N N N N N N 0$ @ s S O S $ o @ N @ @ O @ @ N @ N r O O O@ @ O N r F @ @ O O @ N O @ @ $ O @ O oq q n \ q '. q a ? \ n q q? q q q q c ? q \ q \ q NO @ O O S T N N o $ $ o 0 O N r N O O $ $ NN @ O @ N N N N N N N N N N N N @ N N N N oo o o o o o o o o o o o o o o o o o o o o OO O O O O O O O O OO O O O O O O OO O O U) cq q q q q q q q c c q q q c g c q q q q q z oo o o o o o o o o o o o o o o o o o o o o \o OO O O O O O O O O O O O O O O O O O O O O oo o o o o o o o o o o o o o o o o o o o o qq q q q c e q q q q q q q q q q q q c q q oo o o o o o o o o o o o o o o o o o o o o FN O N O O N T N N A $ O O @ @ $ r @ r O N N$ N @ $ @ @ N O @ N O N O @ N @ O O O O @ oq \ \ \ \ \ \ q c q \ \ \ q \ \ \ q q q q \ \ OO O O O O O O O O O O O O O O O O O O O O OO N O $ O O O O O T O O O O N O 0 O O O N $r o o o N r @ o $ o o N O o @ n r - s o @ c? \ \ q q q q o? q q o? !q u ? c ! \ - q? \ q n a a? @@ @ O O @ N @ N N @ N N @ N @ O O N N N N NT N N T N N T N I _ N N N N OO O O O O O O O O O O O O O O O O O O O O oo o o o o o o o o o o o o o o o o o o o o qq q q q q q q q q q c q q q q q q q q q q oo o o o o o o o o o o o o o o o o o o o o oo o o o o o o o o o o o o o o o o o o o o oo o o o o o o o o o o o o o o o o o o o o qq q q q q q q q q q q q q q q q q c q q q oo o o o o o o o o o o o o o o o o o o o o $r O O - O O O - @ O N 9 6 @ O O @ F @ F @ O@ N O O r @ - N O S S N @ S N T O O S @ @ oO O O r @ - O - O t o s O < N @ N N @ o o N o ; <i ; ri qi ; @ s s c i ; ; oi o < i o i c i ; OF @ O O S O N O T S N $ O O r @ O O O oQ s s s o s o o 6 0 0 0 0 < 6 < $ 3 0 @ 6 NO O O @ $ O O O O N O O O O @ O O O O O O OO O N O O O - O O @ O o N O S o O O O O O q a ? \' . =t ' . q n q q ' . q q \ e q a q q c q q NN O N r $ O N O O o O O O O N T O O O O O OO $ O O O O @ N O $ O O $ N $ @ N o ) o ) O T r@ O O N N o O N T N @ O O O O O O @ N r O \ u? - \ q q q q q q \ oq o ? q o ? oq a c\ q a a q @O N N T O @ @ @ N N @ N O O O F N O O N @ NO O O O N N N N N N N N N N N O O O N N N oo r @ o r r o o @ o o o @ o o N o o r o N o@ @ @ O O O O F O O $ S O O 6 @ O N T O O q \ \ \ \ oq \ \ q \ u? q q q \ q q u ? q \ q \ OO O O O O O O O O O O O O O O O O O ( ) O O @@ o $ @ N N N @ O O N N @ O O 0 N O @ @O N - r O @ O @ N N N O N N O O T @ N N N s? q? n a n o? o ? a ? a ? o ? o ? c? c ? e ? o ? q n n c? o ? o ? ql no o @ o o o o 0 6 6 0 0 0 0 0 0 0 0 0 0 0 r@ O r @ O N $ $ r O @ O N O O o $ N N @ N Oo @ @ @ @ 6 $ O O O N O o N O @ N S O T N q q q u ? u l q q q a u? s ? u ? u ? u 2 r | q '. 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OE>8: ,lOF Z- d e .e IFO- d eo9 v> IENOoo :eT. 9 EE g q q g c8 @@ @ @ @ i s$ t s $ 3 1 @@ @ @ @ d oo o o o 6 @@ o o o 6 r@ O N O F Ai ; - ^ i d t oo o o o N I I I P 8e q- \ q c 2 q R \ R 8 RD OO O O O O OO O O O O qq q q q q oo o o o o o@ o N @ 6 @N O S @ i 6 -N r O N o ai d a i c i c i 6 i ,o @ .N Sr r O N * NO @ @ O a c\ l s a2 '. c2 I oo o o o N @@ r $ N + @N O $ O ; Ac ! q ' : @ \ NN N o N @ NN N N N F NN @ @ @ 6 OO O N N O qa \ e l a l '_ @ o r O ! > N@ @ N N U ' oo o o o o oo o o o o OO O O O O ci c i c i o o o oo o o o o oo o o o o oo o o o o oo o o o o N@ O r S @ NO @ $ F O qc q \ g o l \ OO O F o O @@ o $ N 6 ro o s - o qa q q q o l @@ o @ o s oo o o o o oo - o - o qq c q q q oo o o o o oo o o o o oo o o o o OO O O O O oo o d c i o tN N 6 o Q N g 3 E ; n i ci N o @ o P E E 3 q E: Pi 6Eo&o! fa-Eo& I u2 TC _o o -l () F !o o *FNE .\ q *lOF oa o -l -Fz. - o ool NE Zo o N@ O 0 N O O' _ @ @ N = oo o o < e l oi o - A j ; o N@ $ O 6 @ NN N $ O P OF O o o r : NN N N N = NN N N N . . Ns r @ o Q oo o o o P i @@ N N N \ ' I dc i o o d o ol IEoa o .EOF Z- d o. o: o! o>oE o N@ N o o . ^ @o @ o @ 6 oo o o o o dr i r i r j 6 r , -N O N @ so o o $ r 66 6 6 6 F oo o o o l . o@ N @ o _o 66 6 6 6 2 $r s $ $ NN N N N OO O O O NN N N N NN N N N NN N N N N^osOLOaNX Iv oEi:ooo EE E E 9 o o o o \o oo $ o oo $ o cq q c oo o o oo o o OO O O q. q q a OO O O qq q q oo o o o@ @ o oo o o oo o o qq q c oo o o qc q q @@ @ o ** $ t f o@ @ o oo o o r6 0 0 q- = t - oo o o oo o o o( o N o $o o o ci o o c i oo o 6 oo o o qc q c oo o o oo o o oo s o qq ' : g oo o o oN 6 0 oo o o qq q q oo o o NN O O r( r o o N-oo o o NO O O *o o o qq g q oo o o oo o o oo o o qq q q oo o o NN 6 N @r O O q' : q ' : oo o o oo o o oo o o 60 0 0 od d c t O+ F O NO N O nq o ? e oo o o oo o @ oo o @ OO O - oo c t c i {@ @ @ oN o o NN F N ci d d c i oo o o oo o o OO O O dc i c i d oo o o oo o o oo o o cr o o c , NO @ O oo o o oo o o oo o o o@ o o ) (b ( b ( i i d *{ { s i NN N N oo o o NN N N NN N N NN N N oP5(LooFo-ECtu qq q oo o @@ 6 NN N qc q oo o qq g @o 6 @@ o oo o or @ N .q og ': st $ $ or ) 0 NN N oo o r@ @ ': a 2 a (O N N o6 0 NN N NO t s to @ \\ \ oo o oN o NO @ di d i ^i (0 0 0 , @r N ': q n oo o oo @ oo N qq A l oo o rO Oas c ? oo o oo @ ts + @ oi ;o o@ N @o $ qq q N$ @ NN t (| q q N@ N @N N s? ol a? oo t oo o oo o gg q oo o oo o oo o cq q oo o (o @ (r @ o o@ s Ai -- oo o NN N or O oo ( o ': o? o? 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': ' : (o ( o @ @@ o oo o ON N cq ? a oo o qq q oo o @@ o $o s oo o cq q oo o oo o oo o cq c oo o oo o ooqq q oo o oo o oo o qc q oo o oo o oo o qq q oo o OF N Nr Ocq q oo o NO O NO O qq q oo o NN N o) N o ) a? o ? o! oo o N3 0 NO O qq c oo o oo o oo o qq q oo o (o @ o NNqq o l o, o , d, or o o , oo o oo o cc q oo o @o o 60 0 cg c oo o ON o( o N oo ci o o oo o oo o oo o ci o o NO N rC l O qc c oo o N+ O qq q oo o rN s ) ?9 9 @@ @ r+ \ t $ NN N oo o NN N NN N NN N - aFo{Joo(L @0ci q@ocot+@o@Nootoaqoo0CiNoeOooc$aooNqoooqoo6cNNqoaooNoCINooqooNto@@oosqooqo@6fiNoNNN (' )o.goo(um q q q e q c q q eq q oo o o o o o o o o o @o @ @ @ @ @ @ @ @ @ oo o o o o o o o O@ N F O r @ s @ d 5 oq 0 2 a q a q c q e N q c @o o o o @ @ @ o @ @ q q q q q c c q e 88 o@ o o @ o o o o j j $$ s $ $ $ $ $ $ = = oo o o o o @ o @ d d oo a Q O a A O O d o NF @ @ N @ @ N - d d i a u. ) q q a' : q q q qq e I 3 S 3 S 3 S E s& I R I 8 I R R 3I Be q q u ? c c \ c q q ol c R & I 3 3 $ 3 3 P 8S 3 3 8 8 8 8 5I p ee cc c c q q q q u ? . q q oo o o o o o o o e o : 3 3 > P P P E E s. 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P € .' . , I OE>o o "i oq Zd g .e [t roa o o€ *> IENOoo {- } IE6& -9OEo&ec NEo& ,. t -E-o o _e () F IA o +! NEo& .lOF lD -do .e It rza ool NF Z- d ool IEoa,o *cot r Z- n o^l >E o. 9E va e N^os oeOa N: < Iv oEi:o(!o 40 CFR Part 60 Subpart JJJJ Performance Test Report Test Type: lnitial Test Date: U2A2O24 DOM: ll1l0g Source: Caterpillar G335161E Lean Burn (4 Cycle) Unit Number: Unit B Serial Number: WPT0021 5 Engine Hours: 58575.7 Location: West Water CS Grand County, Utah Prepared on Behalf of: Utah Gas Corp Test Started: 08:41 AM Test Completed: 12:46 PM #As 303 W. 3rd St (580)225-0403 Elk City , OK73644 lndex 1.0 Key Personnel.... ............. 3 2.0 Sampling System..... ....... 3 3.0 Methods Used............ ......................... 3 4.0 Test Summaries.. ............ 5 5.0 Run Summaries.. ............ 6 6.0 Volumetric Flow Rate Data.... ......-...... 7 7.0 Calculations.............. ...... 8 8.0 Oxygen Calibration... ...... I 9.0 Engine Parameter Data Sheet.. .......... 10 10.0 QA/QC Results........ ........11 11.0 D6348 Annexes...... ........ 12 12.0 Signature Page........ ....... 18 13.0 Appendices.............. ....... 19 14.0 Bottle Certs............ ......... 20 15.0 Tri Probe Certification via GD-031 ...... 26 16.0 GAS ALT 141_FT|R EpA......... ...........27 17.0 Tester Qualifications (resume)... ......... 29 18.0 RawData............. i,'il .......... 30 Table 5.1 (Run Summaries)............. ............................... 6 Table6.1(VolumetricFlowRateData)............ Table 6.2 (Stack Gas Measurements)....... ......................7 Table 8.1 (Oxygen Calibration).. ................. I Annex Table 1.2.1 (Certified Calibration Bottle Concentrations)......... 12 Annex Table 1.2.2 (Measurement System Capabilities)..................... 12 Annex Table 1 .3. 1 (Test Specific Target Analytes)............................. 1 3 Annex Table 4.1 (Measure System Capabilities) ............ 15 Figures Figure 6.1 (Location of Traverse Points per Method 1)....................... 7 Annex Figure 1 .4.1 (Sampling Train)..... ..... 13 Annex Figure 1.4.2 (Sampling Points)... ...... 14 Annex Figure 1.4.3 (Sampling Port Locations).... ............ 14 Appendices Certified Calibration Bottle Certificates............. -.....,........20 Tri Probe Certification via GD-031 ......-....... 26 GAS ALT 141_FT|R EpA............. ............... 27 Tester Qualifications (resume)... ................. 29 Raw Data..... ....... 30 1.0 Key Personnel GAS Utah Gas Corp Carlos Gamboa Derrick Timothy 2.0 Sampling System The sampling system used consisted of a Stainless steel probe, heated Teflon line, gas conditioning system, aqd a Gasmet model DX4000 FTIR analyzer. The gas conditioning system used was a Ga-smet PersonalSampling System with a Zirconium Oxide oxygen sensor. 3.0 Methods Used ASTM D6348-03 This extractive FTIR based field test method is used to quantify gas phase concentrations of multiple target analytes (CO, NOX, CH2O, & VOC's) from stationary source efflfuent. Because an FTIH analyzer is potentially capable of analyzing hundreds of compounds, this test method is not analyte or source specific. The analytes, detection levels, and data quality objectives are expected to change for any particulartesting situation. lt is the responsibility of the tester to define the target analytes, the as5ociated ileitection limits foi those analytes in the particular source effluent, and the required data quality objectives for each specific test program. Provisions are included in this test method that require the tester to determine critica! sampling system and instrument operational parameters, and for the conduct of QA/QC procedures. Testers following this test method will generate data that will allow an independent observer to verify the valid collection, identification, and quantification of the subject target analytes. EPA Method 1 & 1A The purpose of the method is to provide guidance for the selection of sampling ports and traverse points at which sampling for air pollutants will be performed pursuant to regulations set forth in this part. EPA Method2 &2C This method is applicable for the determination of the average velocity and the volumetric flow rate of a gas stream. The average gas velocity in a stack is determined from the gas density and from measurement of the average velocity head with a standard pitot tube. Velocity readings are taken from each stack at 16 separate traverse points (Table 6.1) and used to determine the engines mass emissions rate, calculated utilizing the formulas seen in section 7.0 of this report. EPA Method 3A This is a procedure for measuring oxygen (O2) and carbon dioxide (CO2) in stationary source emissions using a continuous instrumental analyzer. Quality assurance and quality control requirements are included to assure that the tester collects data of known quality. Documentation to these specific requirements for equipment, supplies, sample collection and analysis, calculations, and data analysis will be included. GAS 4.0 Test Summary Unit Unit B with a serial number of WPT00215 which is a Caterpillar G33516LE engine located at West Water CS and operated by Utah Gas Corp was tested for emissions of: Carbon Monoxide, Oxides of Nitrogen, and Volatile Organic Compounds. The test was conducted on 212212024 by Carlos Gamboa with Great Plains Analytical Services, lnc. All quality assurance and quality controltests were within acceptable tolerances. The engine is a natural gas fired Lean Burn (4 Cycle) engine rated at 1340 brake horse power (BHP) at 1400 RPM. The engine was operating at 968 BHP and 1399 RPM which is72.25o/o of maximum engine load during the test. The test HP calculation can be found on page 8. The engine was running at the maximum load available at the test site. This test will satisfy the testing requirements for 40 CFR Part 60 Subpart JJJJ. Site Verificat:on Photos I :d_ll qF. 1€. * ?* Fffi GAS 4.0 Test GAS 6 5.0 Run Summaries Table 5.1 Run Summaries GAS 6.0 Volumetric Flow Rate Data Table 6.2. Stack gas pressure rea, Aostd = Velocitv head measured bv the' standard pjtot tube, (in.) H2O.' measured with a standard tube use for Volumetric Flow Rate Stack Diameter (inches)14,00 lnches upstream trom drsturbance 26.00 lnches downstream trom dlsturbance 92.00 Pitot readings are taken for Method 2 calculations using measuring points outlined in Method 1 *The exhaust stack did not prcsont cyclonlc flow condltlons at tho sampllng locatlon due to the absence of cyclones, lnertlal demlsters, venturl scrubberB, or tangential lnlets. r Cyclonlc Flow Check (Pass/Fall): PASS Table 5.1. Data used for volumetric flow rate (Method 2) GAS 7.0 Calculations Method 2: Determination of Stack Gas Velocitv and Volumetric Flow Rate "Note- Use of this method heqates the need for anv fuel related numbers for emissions calculations Ap(avg) = Velocity head of stack gas, mm H2O (in. H2O). 3600 = Conversion Factor, sec/hr. A = Cross-sectional area of stack, m2 (ft21. Bws = Water vapor in the gas stream (from ASTM D6348) Cp(std) = Standard pitot tube coefficient; use 0.99 Kp = Velocity equation constant. Md = Molecular weight of stack gas, dry basis, g/g-mole (lb./lb.-mole). Ms = Molecular weight of stack gas, wet basis, g/g-mole (lb./lb. -mole). Ps = Absolute stack pressure (Pbar+ Pg), mm Hg (in Hg) Pstd = Standard absolute pressure, 760 mm Hg (29.92 in. Hg). Qsd - Dry volumetric stack gas flow rate corrected to standard conditions, dscm/hr. (dscf/hr.). Ts(abs) = Absolute stack temperature, oK ("R). = 460 + Ts for English units. Tstd = Standard absolute temperature, 293"K (528 'R). Vs = Average stack gas velocity, m/sec (ft./sec). Md = .aa(.059)+.32(.087)+.28(.854+0) = 29.25 LB/LB-MOLEMd = .44(o/oCO2)+.32(%O2)+.28(%N2+%CO) Ms = Md(1 -Bws)+18.o(Bws)Ms = 29.25(1 -.11217)+.18.0(.11217\= 27.988 LB/LB-MOLE vs = Kp'cp(std;-y'apavg-y'1rs1abs)(Ps'Ms))vs = 8s.49..99../.A0.y'(r TAO.OZ t(25.38'27.988)) = 101.34 FT/SEC Qsd = 3600(1 -Bws)Vs-A((Tstd'Ps)(Ts(abs)-Pstd))= 3600(1-.1 1 2)1 01.344'1.069((s28.25.38y (1 1 86.67.29.92) = 130668.38 Q - 130668.377135.315 = 3700.081 DSCM/|-|R Emission Rates (Examples use CO Run I 453.6= Conversion factor lb. to gram HP= Engines rated Horsepower A = Cross-sectional area of stack, n2 (ft2). Mfg.= N4snulrcturer Exhaust flow rate at 100% (ft3/min) BHP/HR. = Brake work of the engine, horsepower-hour (HP-HR.). 02 = Concentration of oxygen on a dry basis, percent. BTU/HP-HR. = Brake Specific FuelConsumption (HHV) ppm= Parts Per Million (CO) ER = Emission rate of (CO) in g/HP-hr. ppm@15% 02= PPM corrected lo 15'/"02 F(d )= yslurn.s of combustion components per unit of heat Qsd = Dry volumetric stack gas flow rate corrected content, scm/J (scf/million Btu). to standard conditions, dscm/hr. (DSCF/HR.). Q = Stack gas volumetric flow rate, in standard cubic meters Run Time = Run Time in Minutes per hour, dry basis Tpy= Tons per year LB/HR.= Emission rate of (CO) in LB/HR. Vs = Average stack gas velocity, m/sec (ft./sec). Mol wt.= MolWeight of CO (28.01) ppm @ 15olo 02 = PPM'((20 .9-15o/oo2)l(20.9-O2))ppm @ 15% 02 = .359'(20.9-15)l(20.9-8.7'/.)) = .174 PPM @ 15% 02 g/hp-hr = (PPM-(1 . I 64.1 0^-3).Q.(Run Time/60))lBH P/HR (.359.(1.164'10^-3).3700.081'(Run Time/60))1999.138 = .002 G/HP-HR lb/hr = ER'1 /453.6-8HP-HR LB/HR = .002' l/453.6'999.1 38 = .003 LB/HR TPY = .003'4.38 =.013 TPY BHP/llR = Available HP - ((MFP @1OO/o - Actual MFP inHG) @1OO/"'MFP @75V"\ I 999= 1339.04 - ((70-55) I ((70-55.2) I 25'/.))). 1339.04) ppm wet'(1(1-H2O) = ppm dry .36 = .318s',(1/(1-.1 1)) GAS 8.0 Oxygen Calibration 9 8.1 Calibration error test; how do I confirm my analyzer calibration is correct? After the tester has assembled, prepared and calibrated the sampling system and analyzet, they conduct a 3-point analyzer calibration error test before lhe first run and again after any failed system bias test or failed drift test. They then introduce the low-, mid-, and high-level calibration gases sequentially in direct calibration mode. At each calibration gas level (low, mid, and high) the calibration error must be within I 2.0 percent of the calibration span. 8.2 lnitial system bias and system calibration error checks. Before sampling begins, it is determined whether the high- level or mid-level calibration gas best approximates the emissions and it is used as the upscale gas. The upscale gas is introduced at the probe upstream of all sample- conditioning components in system calibration mode. (1) Next, zero gas is introduced as described above. The response must be within 0.5 percent ofthe upscale gas concentration. (2) Low-level gas reading is observed until it has reached a final, stable value and the results are recorded. The measurement system will be operated at the normal sampling rate during all system bias checks. (3) lf the initial system bias specification is not met, corrective action is laken. The applicable calibration error test from Section 8.2.3 of EPA Method 7E is repeated along with the initial system bias check until acceptable results are achieved, after which sampling will begin. The pre- and poslrun system bias must be within t 5.0 percent of the calibration span for the low-level and upscale calibration gases. 8.3 Post-run system bias check and drift assessment - confirming that each sample collected is valid. Sampling may be performed for mulliple runs before performing the post-run bias or system calibration error check provided this test is passed at the conclusion of the group of runs. A failed final test in this case will invalidate all runs subsequent to the last passed test. (1) lf the post-run system bias check is not passed, then the run is invalid. The problem is then diagnosed and fixed, lhen another calibration error test and system bias is passed before repeating the run. (2) After each run, the low-level and upscale drift is calculated, using Equation 7E-4 in Section 12.5 from EPA Method 7E. lf the poslrun low- and upscale bias checks are passed, but the low-or upscale drift exceeds the specification in Section 13.3, the run data are valid, but a 3-point calibration error test and a system bias check must be performed and passed prior to additional testing. Table 8.1 Oxygen Calibration Method 7E 3.4 To the extent practicable, the measured emissions should be between 20 to 100 percent of the selected calibration span. This may not be practicable in some cases of low concentration measurements or testing for compliance with an emission limit when emissions are substantially less than the limit. EPA Method 3A QA Worksheet Certified Gas Concentralon I Certifled Gas Concentraion I Cortified Gas Co Low-Level (%) I Mid-Level l%l I Hloh-Levc 0.00%19.12Yo121.029 ncentralon 7E 8.5: Note: that you may risk sampling for multiple runs before performing the post-run bias provided you pass this test at the conclusion of the group of runs (DIRECT) Analyzer Calibration Error (S 2%) Check Certified Concentration Value (06) Direct Calibration Response (9 Absolute Analyzer Calibration *rot (o/o) Zero Gas o/o 0.00%0.000/o 0.0070 0.00% Mid-Level Gas % High-Level Gas o/o 9.120/o 21.02o/o 9.14o/o z'.t.o20/o 0.02o/o 0.00olo 0.110/o 0.00% (SYSTEM) Calibration Bias Checks (S 5%) and Drift Checks (S 3%)Upscale Gas 9.12o/o Zero Offset 0.00% Bias Pre lnitisl Velue Bias Post lnital Values Span 21.02 Analyzer Calibration Response (%) Zero Gas 0.000/o System Calibrations Response Pre (o/o) System Bias (o/ of Span) Pre System Calibration Response Post (%") System Bias (ol of Span) Post Drift (% of Span) 0.000/o 0.00o/o 0.00o/o 0.00%0.0070 Upscale Gas 9.14o/o 9.090/o O.27o/o 9.09%0.27o/o 0.007o (SYSTEM, Calibration Bias Checks (S 5%) and Drift Checks (S 3%) Avo. Gas Concentration (Run 1 8.640/o Effluent Gas (Coas) Run 1 8.67% Avg. Gas Concentration (Run 2)8.68% Effluent Gas (Cgas) Run 2 8.71o/o Avg. Gas Concentration (Run 3)8.72o/o Effluent Gas (Cgas) Run 3 8.75o/o EPA Method 3A CIA Worksheet Zero Gas 100% Nitrogen Mid-Level Gas 9.12o/o High-Level Gas 21.O2o/o Zero Gaso/o Mid-Level Gas 7o zero cas % l-;ii;-l upscate used upscate cat t ,ng% I gj}o/o GAS 10 9.0 Engine Parameter Data Sheet AS fi,nfifu,tiffiI $PadgG, rn Comoanv Utah Gas Corp Facility WeSt Water CS Date 2t22t2024 Site Elevation (ft)5048 Unit lD Unit B Make Caterpillar MOOet G33516LE Serial Number wPT00215 Technician Carlos Gamboa Run 1 Run 2 Run 3 Completed Run Start Times U6:4] AM U9:5/ AM l1:t I AM l2:46 PM Enqine Hours 5A5t:z.t 58573.7 5U5/4. /5A5t5.t Enqine Parameter Data Run 1 Run 2 RUN 3 Averaqe Ensine Speed (RPM)1399.0 1398.0 'r rr99.u 1398.7 lntake Manilold Pressure (psi)27.0 26.0 26.0 26.3 Intake Manifold Temp'F 120.2 123.8 123.4 122.6 EnEine Load (EHP)999.1 9s2.4 953.1 968.2 Ambient Temp "F 3t.o 43.0 46.0 42.O HumidatY 7o 65.O 50.0 44.0 53.0 Dew Point "F 27.O 26.0 25.0 za.u AFR Manufacturer/Type Caterpillar I Caterpillar CaterDillar Caterpillar suction Pressure 125.t 19.3 19.3 121.4 DischarEe Pressure 324.O 312.0 312.U 316.0 catalvst (Yes or No Yes Catalyst Manufacturer EmeriChem Emerichem EmeriChem EmeriChem # of Catalyst lnstalled 1 Catalvst lnlet Temp "F 808.0 797.O 797.O 800.7 Catalvst Outlet Temp 'F 831.0 819.O 819.O 823.O Catalvst Pressure Drop H2O 199.0 3.9 3.9 68.9 GAS 11 10.0 QA/QC Results me System Response Time 45 seconds Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Oxygen Average:0.00 Average:0.00 Average:0.00 Average:0.69 Average:0.00 CTS Bottle Concentration CTS Compound Concentration Avg Tolerance Ditference between measured and expected Value:99.40 2.00/o 0.60% Carbon monoxide CO Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Oxygen Average:0.34 Average:0.40 Average:0.00 Average:0.40 Average:0.33 Average:0.00 Mechanical Response Time CTS Bottle Concentration CTS Compound Concentration Avg Tolerance Ditference between measured and expected Value: 100.00 Value:99.65 5.00% 0.3s% Equilibration Besponse Time Spike Reported Spike Expected 45 seconds Value: 251.07 Value: 251.00 Gas, lnc. 12 11.0 D6348 Annexes 1€ The test quality objectives completed for the emissions test are demonstrated throughout Annexes 1,2,3, 4, 5, 6, 7 & 8 as layed out per ASTM D6348-03. Al! reference methods, pre-test and post test procedures were within acceptable limits. Data generated during the pre-test and post-test procedures are summarized below in order of the distinctive Annex. Three 60 minute test runs were performed. The final analyte concentrations are the average of each test run. Data was taken at 60 second intervals. Each 60 second measurement was the average of 600 scans. Propane is used as the surrogate compound for the Annex 5 Spiking Technique due to Propane being the VOC that is most commonly found in the combustion process of natural gas. Additionally, the molecular weight of Propane coincides with with motecular weight of VOC's per the EPA. Annex Table 1.2.1 Certified Calibration Bottle Concentrations Bottle Exoirataon NO2 Ethvlene sF6 02 ("/ol cG419750 5t8t2026 99.10 9.120/0 cc1 17503 8t15t2031 100.00 4LM020982 11t28t2030 21.O2Y" Cylinder # CC142828 Expiration: 12-06-2030 Propane co NO SF6 tsotfle value 251.00 501 .40 252.40 v. /u Analyzer System Response 251.Ot 494.61 245.33 9.t4 Percent urnerence O.O37o 1.35o/o 2.8O"/o u. t ir-lo Annex T able 1.2.2 Measu rement System Capabil ities GAS Annex Table 1.3.1 Test Specific Target Analytes and Data Quality Objectives Compounds Infrared Analysis Region (cm-l) Expected Concentration Range IUleasuremenl System Achievable Minimum Detectable Concentrations nequtreq Measurement System Accuracy and Precision for Test Aoolication CO 2000-2200 0-1200 ppm 0.16267 pom 4 Dom NO 1875-2134 0-'1000 Dpm 0.4007 DDm 2 Dom N02 2700-2950 0-100 oom 0.4899 oom 2 oom VOC 2600-3200 0-100 ppm 1.8520 ppm Total VOC's 1 ppm perVOC91 0-1 1 50 2550-2950 CH2O 2550-2850 0-100 ppm u./6/6 ()()m 1 ppm lnterfering Compounds . CO is analyzed in a separate analysis region than CO2 and H2O c02 926-1 1 50 0-10%OVo nla Water Vapor 3200-3401 O-22o/o O.2Oo/o nla . VOCs compiled of Acetaldehyde, Ethylene, Hexane, and Propane. 1.4 PROBE STACK PAIIIEt GASMET FTR FLOITV ITTR. Figure Annex 1.4.1 Sampling Train The testing instrumentation is housed in an enclosed vehicle which is located approximately 45 feet from the source. A heated sample line (sixty feet in length) is attached to the inlet of analyzer system and the source effluent discharges through the FTIR outlet. l ry GAS *# GAS 14 G.ull-ul-sotof(', TRLPROBE SAf\IPLE POI NT LOCATIONS AS PERCENTAGE OF STACK DIAMETER Figure Annex 1.4.2 Sampling Points lnterior Stack Diameter (inches): lnches Upstream: 26 lnches Downstream: 92 SAMPLE PORT LOCATION DfiERMINED BY DISTAI{CE FROM DISIURBANCE Figure Annex 1.4.3 Sample Port Location Sampling Point Locations in lnches 16-7o/"2.338 o/o /.UUU 83.3%11.662G,t!Ful =o EIorft GAS Annex 2. Deteimination of FTIR Measurement Tarqet Analvte Results (ppm) CO O.162t NO 0.4001 NO2 0.489( Etnvlene 0.378t HroDane u.455r Hexane U.ZZ3i Acetaldehvde 0.8152 FOrmaloenvoe u. /6 lt NEA TfI :r'rrt s RET" TII :t'}}ls- MDC#I : [t ,.1" (rve,tT),lnLi:1 N EA 7tl t'rnls -rPl Lrerl R I: t: ttt rTTIS Le:e,tt ualrbratron I ransler Standaro Exoected Measured Path Lenqth Validated Ethylene 100 99.4 4.97 PaSSEd D6348 Annex 4;.,,,Required Pre-Test Procedures .,', Annex Table 1.2.2 Measurement System Capabilities raramerer Measured Gas concentratron (pom)Path Length EquilrDralron Time Dilution Factor % Recovery Path Lenqth ttnvlene 99.397 t.9 tu Spike Direct Propane 249 441 t' SF6 9.677 CO 499.857 NO 248.603 Mechanical Response Time Ethylene 99.652 1 7 seconds Analyzer Response Propane 251.0ti9 41 secondsSF69.743 CO 494.614 NO 245.333 Analyte Spike Recovery Propane & SF6 U.JU"/o 9B.BB% I . 19"/o 99.08% 7.75o/o 91.45"/o Svstem Zero Nitroqen 1 7 seconds Post Spike System Hropane 251.196 CO 493.380 NO 245.573 SF6 9.747 GAS Parameter Gas Concentration Measured 70 Difference Soecilicatlon Validated Spike Direct Propane 251.000 249.481 0.610/o +l-2/o Pass SF6 9. /30 9.6t I U.54-/o +l- 2"/o Pass CO 5UI.4UU 499.85/U.3l "/o *.l- 2"/o PASS NO ZSZ.CUV 248.603 l.5U7o tl'2o/o PASS spike Run I vla the system Source Output Spike Averaqe Dilution Factor Expected 70 Recoverv Specification Propane 9.605 29.563 29.898 98.880%7O-'l3Oo/" SF6 0.000 o.803 4.296"/o <1Q"/" Spike Bun 2 via the Svstem Source Outpul Spike Average Dilution Factor Expected 7" Recoverv Specification Propane 9.768 28.536 ZU.UU I 99.060%/O-13tJ"/o SF6 0.000 o.t54 l.lVZ"/o (l U-lo Spike Run 3 via the System source output spike AveraEe Dilution Factor Expected 70 Recovery Specification Propane 10.o22 28.'t99 28.938 97.45O"/o 7O-13OYo SF6 0.000 0.750 l.l5U"/o <1Qo/o Noise Equivalent Absorbance (NEA) RMS High. 0.000969 RMS Mid 0.000934 RMS Low 0.000994 Line Position 2092 2069 2046 2A23 1999 1976 1953 1930 1907 1884 1861 1837 1814 0.20 0.15 0.10 0.05 0.00 -0.05 0.20 0.'t 5 0.10 0.05 0.00 -0.05 @ o.oo% Pass GAS The Gasmet GICCOR (Genzel lnterferometer with Cube Corner Retroreflectors) interferometer is specially designed for maximum optical throughput and maximum signal to noise ratio of 7.72 (cm-1) remaining stable with any vibration and temperature changes. spectrometerlne Gasmet Dx4000 ts a setting and the detector li a low resoluuon spectrometer wnere me apenure rs IrXe, linearity was tested with an alternate approach. A three apertu point linerarity of the CTS gas was performed and validated. Linearity 't57.8867 148.8867 139.8867 130.8867 't21.8867 1',t2.8867 103.8867 94.8867 85.8867 76.8867 157.8867 148.8867 139.8867 130.8867 121.8867 112.8867 103.8867 94.8867 85.8867 76.8867633 625 618 610 602695 687 679 672 664 656 648 641 5.02798793 Pass The analytical accuracy of the quantification algorithm is satisfied via the results from Annex 5 per Annex 7.6 POST GIli lJrraf,em GreCK: u ls Honle uoncenlra0on:100.00 u ls samDle uoncentranon Averaqe:100.36 Dtfterence bewveen measured and exDecteo:0.35% lolerance:5.OO% Run Data Valldatlon - Automated vs Menual Beadlng Valldatsd Gommentg HUn 'l l,OInIS'l d. Z On UU/l\U/HrODane All wlthln 2070 Passed uemonslrates no tntenerences oDserveo. HUn Z HOTnIS 't & Z On UU/r\U/FrOpane All wtthln 2O7o Passed Demonstrates no rntenerences oDserveo. HUn i, Hornts 't & z on uu/r\u/rropane All withrn 2O7o PASSEd uemonstrates no rntenerences oDserveo. GAS 18 12.0 Signature Page Job/File Name: Utah Gas Corp;West Water CS; Unit B;JJJJ We certify that based on review of test data, knowledge of those individuals directly responsible for conducting this test, we believe the submitted information to be accurate and complete. #AS Company: G.A.S. lnc. Print Name'. Travis Hartley Date:212212024 Title: Director of Stack Testing Signature: Phone Number: 580-225-0403 Company: Print Name: Title: G.A.S. lnc. Carlos Gamboa Emissions Specialist Date:212212024 Company: Utah Gas CorPoration print Name. Taryn Weiner 4t11t2024lJate: Signature: Ti,e: Manager, Air and Sustainability Phone Number: 970-307-5032 GAS Appendices GAS Airgas an Air Liquidg c@paoy Spike (5 Gas) Alrgas Specialty Gres Airgs USA LLC 12722 S. WentworthAve. Chi@go, IL 60628 Airga-6m CERTIFICATE OF ANALYSIS Grade of Product: EPA PROTOCOL STANDARI) Part Number: Cylinder Number: Laboratory: PGVP Number: Gas Code: E05Nl94E1 54C014 cc142828 124 - Chicago (SAP) - lL 812022 CO,C02,NO,NOX,PPN,BALN Reference Number: 54-402601324-1 Cylinder Volume: 147.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 660 Certification Date: Dec 06, 2022 Date: Cedifi€tion pedomed in a@odan@ with 'EPA Tmceability Prcb@l for Asgy and Certili€tion of Gaseous Calibrauon Standards (May 2012)- documant EPA 600/R-12/531, using the assay pocedur6s listed. Analyti€l Methodology does nol require corectron for analytical interferen@. This cylinder has a total analyti€l un@iainty as stated below with a @nfiden6 level of 95%. Ther6 are rc signili€nt impuriues which affect lhe use of this €libration mixture. All @n@nhations are on a mle/mle basis unless otheNise noted. The results relata only to lhe items tested. The report shall not be reprcduced ex@pt in Iull without approval ofthe laboratory. Do Triad Data Available Upon Request PERMANENT NOTES:Mixture contains nominal 'loppm Sultur Hexafluoride as a tracer component. Aclual lested value included within the original Certificate of Analysis. Contacl the Airgas laboratory if a reprinl is required NOTES:Mixture contains nominal loppm Sulfur Hexafluoride as a tracer component. Aclual tested value included within the original Certilicate of Analysis. Contact the Airgas laboratory if a reprint is required. SFO Results: JMR137-9.73:PPM L- il I ! Approved for Release Page 1 of I Componenl ANALYTICAL RESULTS Requested Actual Protocol Total Relative Concentration Concentration Method Uncertaintv Assay Dates NOX 250.0 PPM 253.0 PPM G1 +/- '1.2% NIST Traeable 11ngn122, 12106D022 NITRIC OXIDE 250.0 PPM 252.4PPM Gl +/- 1.0% NIST Traceabls 1112812022,'l2n6no22 PROPANE 250.0 PPM 251.0 PPM G1 +/- 0.7% NIST Tra€able 1'll30n022 CARBON MONOXIDE 500.0 PPI\il 501.4 PPM Gl +/- 0.6% NIST Traeable 11ngnl22 CARBONDIOXIDE 5.000% 5.025V" G1 +/-1.4%NlsTTra@able 1128D022 NITROGEN Balane CALIBRATION STANDARDS fype Lot lD Cylinder No Concentration Uncertainty Expiration Date od29,2026 Feb 20,2O2O Feb 18, 2023 Mat 17,2027 Ju!03,2024 May 14,2025 NTRM 200603-31 880113125 250.3 ppM NtTRtC OXTDENTTROGEN +l-0.80/o PRM 12386 D68s025 S.gt PPM NTTROGEN D|OX|DE/AIR +l-2.0o/o Gl\fls 401423838104 CC505590 4.373 PPM NITROGEN D|OX|DE/N|TROGEN +t-2.0"h NTRM 200602-13 6162697Y 243.3 PPM PROPANE/AIR +l-O.5o/o NTRM '130'10109 KA1003925 495.4 PPM CARBON MONOXIDENITROGEN +l-0.60/o NTRM 13060423 CC413685 7.489 % CARBON DIOXIDE/NITROGEN +l-0.6% The SRM, NTRM, PRM, or RGM not6d abov6 is only in reference to the GMIS used in the assay and not Dad ofthe analysis. ANALYTICALEQUIPMENT lnstrumenuMake/Model Analvtical Principle Last Multipoint Calibration Ni@let iS50 AUP20'10242 CGl SIEMENS ULTRAMAT 6E N1J57OO Ni@let iS50 AUP2010242 Ni@let iS50 AUP2010242 Ni@let iS50 AUP2110277 FTIR NDIR FTIR FTIR FTIR Nov 07, 2022 Nov 28,2022 Dec05.2022 Dec05,2022 Nov 07. 2022 GAS 9o/o O2|NO2 nllp"*$ Airgs Specialty Gses Airgas USALLC 525 North Industrial lrop Road Tooele, UT 84074 Air86.@m CERTIFICATE OF ANIALYSIS Grade of Product: EPA PROTOCOL STANDARI) Part Number: E03N190E15W0003 CylinderNumber: CC419750 Laboratory: 124 - Tooele (SAP) - UT PGVP Number: 872023 Gas Code: NO2,O2,BALN Reference Number: 153-402732424-1 CylinderVolume: 145.0CF Cylinder Pressure: 2015 PSIG Valve Outlet: 660 Certification Date: May 08, 2023 Expiration Date: Mav 08.2026 Cedill6tion perfomed in aeordance with "EPA Tra@ability Prcto@llor Asey and Ceiifi€tio of Gasus Calibration Standards (May 2012)' document EPA 600/R-12/531, usinO the assay procedures lisled. Analytial Methodology does not require @slion for analyti€l interferen@. This cylinder has a total anal,,ti€l uncedainty as stated below with a 6nfiden@ level of95%. There are rc signifienl impurilies which aflectthe usg ofthis calibretion mixture. All @n@ntrations are on a mle/mle basis unless otheMise noted. The €sults Elate only to th6 itemstosted. The report shall nol be reprcduced ex@pl in full without approval ofthe laboratory. Do Triad Data Availablo Upon Requost Approved for Release Page I ol I Component .ANALYTICALR-ESULTS Requested Actual Protocol Total Relative Concentration Concentration Method Uncertainty Assay Dates NITROGENDIOXIDE 100.0PPM 99.10PPM G1 +/-2.0%N|STTra@able OSI01DO23.O5n8l2o23 OXYGEN 9.000 % 9.119 o/o G1 +/- 0.6% NIST Tra@able 0510212023 NITROGEN Balan@ CALIBRATION STANDARDS Type Lot lD Cylinder No Concentration Uncertainty Expiration Dato PRt\' 12389 NTRtVt 14060629 Oec 17,2024 Feb 19,2020 od29.2025 GMIS 1534012021601 CC502090 100.5 PPM NITROGEN DIOXIDE/NITROGEN 1.1o/o The SRM, NTRlvl, PRM, or RGM noted abde is only in retorence to th6 GMIS 6sd ih the asay and not pad ofthe anavsis. D685O5O 99.0 PPM NITROGEN DIOXIDE/NITROGEN 1,OYO CC436987 4.794 % OXYGEN/NITROGEN 0.4o/o ANALYTICALEQUIPMENT Analytical PrinciDlelnstrumenUMake/Model Last Multipoint Calibration MKS FT|R NO2 0t8143349 Horiba MPA-s10 U/603MM58 02 FTIR 02 Paramaonetic (DIXON) May 03, 2023 Apr 06, 2023 GAS Airgas e Air Lhuida @rpary Ethylene Only Airgas Specialty Gas€c Airg6 USA LLC uZ2 S. Wentmrth Are. Chicago, IL 60628 Arry6.6B CERTIFICATE OFANALYSB Grade of Product: PRIMARY STA\IDARD GREAT PLAINS ANALYTICAL SERVICE,Customer: Part Number: Cylinder Number Laboratory: Analysis Date: Lot Number: x02Nt99P1sACVH8 cc'fi7503 124 - Chicago (SAP) - lL Aug 1 5, 2023 54402811378-'.1 Expiration Date: Aug 15,2031 Referenc€ Number: 54402811378-1 CylinderVolume: 144.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 350 Primary Standard Gas Mixtures are traceable to N.I.S.T. weights and/or N.LS,T, Gas Mixture reference materials. Component ANALYTICALRESI.'LTS Req Conc Actual Concentration (Mole o/o) Analytical Uncertainty ETHYLENE NITROGEN 100.0 PPM Balance '100.0 PPM +l- 1o/o Notes:GREAT PLAINS ANALYTICAL, CERTIFIED BY FTIR Approved for Release Pagc I of 'l GAS Airga$. e Ar ljquftJo cspany BIP AirgN Mid Soutb region Airgm USA LLC 9741 E. 56th St. North Tulsa, OK74u7 Airya.6h CBRTIFICATE OF BATCH ANALYSIS Part Number: Cylinder Analyzed Laboratory: Analysis Date: Grade ofProduct: Nl BlP300 T\ /05-867349 106 - Tulsa Fast Fill (SAP) - OK Feb 10,20'16 BIP-BUILT IN PURIFIER Reference Number: 29400672389-1 Cylinder Volume: 304.0 CF Cylinder Pressure: 2640 PSIG Valve Outlet: 580 Component ANALYTICAL REST'LTS Requested Purity Certified Concentration NITROGEN OXYGEN WATER TOTAL HYDROCARBONS CARBON DIOXIDE CARBON MONOXIDE 99.999 % 1 PPM 1 PPM 0.1 PPM 0.5 PPM 0.5 PPM 99.999 % 0.94 PPM 0.058 PPM 0.1 PPM 0.235 PPM 0.235 PPM Permanent Note3:This c€rt includes values from the "filf side and is not representative of the "use" side purity. Contact an Airgas Sales Representative for this information. Cylinde13 ln Batch: 4263617Y, T1 O4671107, T\ 0S831574, TW0$.865966, T\ i0S867349, TW0ffi67538, TW05-867578, Tl /0$881687, Tt 0$88'1820, T\ /0S920689, T\4,0S920760, T\ 105848694, T\ /05862141, Tt4,O5897265, T\ 05897512, T\ 05920678, TW05920686, T\ 05920695, T\ 05920781, Tr O5920874 lmpurities verifled against analytical standards traceable lo NIST by weight and/or analysis. Approved for Relea3e P.gc I ot t GAS Airgas 21o/o 02 Airgas Specialty G6es Airgas USA LLC 525 North Indstrial taop Road Tooele, lrT 84074 Airgas.om CERTIFICATE OF ANALYSIS Grade of Product: EPA PROTOCOL STANDARD Part Number: E02N179E15A0081 CylinderNumber: 41M020982Laboratory: 124 -fooele (SAP) - UT PGVP Number: 872022 Gas Code: O2,BALN Reference Number: 153-402603461-1 CylinderVolume: 146.0CF Cylinder Pressure: 2015 PSIG Valve Outlet: 590 Certification Date: Nov 28,2022 Date: Certili€tion p€rfomed in a@ordan@ with 'EPA Traceability Prcto@l for Assay and Ce^ili@tion of Ga@us Celibration Standads (May 2012)" document EPA 6OO/R-'12531. usinO the assay prccoduros listed. Analytidl Methodology does not requke @fl*tion foranalyti€l intederene. This cylinder has a total analr{i€l unc€dainty as stated below with a @nfiden@ l6vel of95%- There are no signifient ampurilies which affectthe use ofthis calibration mixture. All @n@nhations are on a mle/mle basis unless otheMise notad. The results relate only to the items tasted. The rcpod shall not be repaoduced er@pt in full without approval of the labo.atory. Do Triad Data Available Upon Request Approved for Release Page I of I Component Requested Concentmtion ANALYTICAL RESULTS Actual Protocol Concentration Method Total Relative Uncertainty Assay Dates OXYGEN 21.00% 21.O2o/o NITROGEN Balan@ Gf +/-1.0%NlsTTc@able 11n82022 CALIBRATION STANDARDS Type Lot lD Cylinder No Concentration Uncertainty Expiration Date NTRM 09061434 CC282492 22.53 % OXYGEN/NITROGEN O.4Yo May 13,2025 lnstrumenUMake/Model ANALYTICAL EQUIPMENT Analytical Principle Last Multipoint Calibration Horiba MPA-s10 V!603MM58 02 02 Pammagnetic (Mason)NoY 17,2022 GAS Airgas. Acetaldehyde & SF6 Airg8 Specialty Grues Airgas USA LLC 9810 BAY AREA BLVD Pasadena, TX z7so7 Airt6.@m CERTIFICATE OF ANALYSIS Grade of Product: PRIMARY STANDARJ) GREAT PLAINS ANALYTICAL SERVICE, x03Nl99P1 sACD42 cc334560 124 - Pasadena (SG06) - IX Sep 29, 2023 163402847128-1 Expiration Date: Sep 29,2024 Primary Standard Gas Mixtures are traceable to N.I.S.T. weights and/or N.I.S.T. Gas Mixture reference materials. ANALYTICAL RESULTS Customer: Part Number: Cylinder Number: Laboratory: Analysis Date: Lot Number: Reference Number: 163402847128-1 Cylinder Volume: '140.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 350SS Gomponent Req Conc Actual Concentration (Mole %) Analytical Uncertainty SULFUR HEMFLUORIDE ACETALDEHYDE NITROGEN 10.00 PPM 100.0 PPM Balance 10.00 PPM 99.62 PPM + l- 1o/o +l- 1o/o Sidnrfirra 6n file Approved for Release Page I ot I GAS #as Part Number: Laboratory: Analysis Date: LOT Number: SN: CERTTFICATE OF ANALYSIS Grade of Product: CERTIFIED STAI{DARD-PROBE Measured Flow Measured Flow Measured Flow Mean Pmbe Port A (Vml Port I (Vm) Port C (Vm) Port Srmpled lDelta o1l lDelta o2l lDelta oil Flow lllm) Great Plalns Analytlcal Servlces 303 w 3'd st Elk City, OK, 73644 (58 0) 2 25-0403 F ax: (580)225 -Z6tZ Tri Probe Certification 145 GAS INC. 3t3t2022 A 224145 Reference 22 Number: Stack Diameter: 14" Target Flow 3Umin Rate: Numberof 3 Points: Product performance verified by direct comparison to calibration standards traceable to N.I.S.T. *The probe listed on this form meets the multipoint traverse requirement of EPA Method 7e, section 8.4 as shown in the accompanying data. Method 7e, section 8.4 states that the multipoint traverse requirement can be satisfied by sampling via "a multi-hole probe designed to sample at the prescribed,points with a flow {- l0 percent of mean flow rate". ANALYTICAL RESULTS Total Flow (r/m) Run I Ru2 2 LPM 4 LPM 0.720 (8.00a) l.4l (7.oea) 0.660 (-r.00a) l.3l (4.51A) 0.620 (-7.00a) 1.23 (-6.58A) *Calibration conducted in accordance with Emission Measurement Center Guideline Document - f,MC GD.03l 3/3/2022 DateApproved for Release Probe size: 14S a,oH'.,,-- LYJ UNITED STATES ENVIRONMENTAL PROTECTION AGENCY BESEARCH TRIANGLE PARK, NC 27711 March 15,2021 I rS, l..l r 'r ,\ ll.r { rl ,4{ I I 'r' t,t AlJtr lli r. , Al,,t.' 1, I Ahi r&irl.,! Mr. Jordan Williamson CEO GAS Inc. 303 W. 3ra Street Elk City, OK73644 Dear Mr. Williamson: We are writing in response to your letter received on September 17, 2020,in which you request the approval of alternative testing procedures. The EPA's Office of Air Quality Planning and Standards (OAQPS) is the delegated authority for consideration of major alternatives to test methods and procedures as set forth in 40 CFR parts 60 and 63 under which your request must be addressed. GAS Inc. is requesting a change to one of the test methods, ASTM D6348-03, used for conducting performance tests to determine compliance under 40 CFR part 60, Subpart JJJJ - Standards of Performance for Stationary Spark Ignition Intemal Combustion Engines (Subpart JJJJ) and 40 CFR part 63, Subpart ZZZZ - National Emissions Standards for Hazardous Air Pollutants for Performance for Stationary Reciprocating Internal Combustion Engines (Subpart ZZZZ). The change being requested will be used to check detector linearity of the Fourier Transform Infrared (FTIR) instrumentation used to conduct this method. Specifically, you are requesting that the procedures of section 8.3.3 of Method 320 (40 CFR part 60, Appendix A), another FTIR-based method allowed under Subparts JJJJ and ZZZZ, be used in lieu of section A6.4.1of ASTM D6348-03 when conducting testing using ASTM D6348-03 under 40 CFR part 60, Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. In your request, you state that this altemative linearity check procedure will produce consistent results when utilizing either Method 320 or ASTM D6348-03. Additionally, some FTIR instrumentation does not allow for reducing the size of the aperture in the instrument and, thus, it would not be feasible to properly conduct the entirety of the ASTM D6348-03 method in its current form using such an instrument. Based on our understanding of FTIR instrument principles and recognition that the requested alternative determination of detector linearity is both technically sound and contained within Method 320, we are approving the requested change. We believe that this alternative is acceptable for use for use in testing all engines subject to 40 CFR part 60 Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. Also, we will post this letter as ALT-l4l on EPA's website (atwww.epa.gov/emc/broadly-applicable-approved-alternative- testmethods) to announce that our approval of this alternative test method is broadly applicable to engines for the purposes of meeting Subparts JJJJ and ZZZZ. If you should have any questions or require further information regarding this approval, please contact David Nash of my staffat 919-541-9425 or email at nash.dave@ppa.gov. Sincerely, STEFFAN DlCtrilf dStcd bI STEFAilJO$6(}{ cc: JOH Steffan M. Johnson, Group Leader Measurement Teehnology Group Sara Ayers, EPA/OECA/OC/IvIAMPD, (ayres.sara@epa.gov) Melanie King, EPA/OAR/OAQPS/SPPD, (king.melanie@epa.gov) James Leather, EPA Region 6, (leatherjames@epa.gov) David Nash, EPA/OAR/OAQPS/AQAD, (nash.dave @epa.gov) hnsrort.oaltrlJds{tw Carlos Gamboa GAS 580-225-0403 info@gasinc.us Type of Sources Tested: Stationary lnternal Combustion Engines. 4 Stroke Rich Burn Engines. 2 Stroke & 4 Stroke Lean Burn Engines Stationary Natural Gas Fired Generators Stationary Propane Fired Generators Gas Fired Boilers Types of Analyzers:. Gasmet DX4000 FTIR. Gasmet Portable Sampling Unit with Zirconium Oxide 02 Sensory. Testo 350. Flame lonization Detector Qualifications: Trained, sludied, and fully demonstrates compliance for emissions testing via data collection outlined in the following Reference Methods:. EPA Method 1 & 1A - Sampling & Traverse Points. EPA Method 2 &2C - Velocity & Volumetric Flow Rate of a Gas Stream. EPA Method 3A - Oxygen. EPA Method 7E - NOX. EPA Method 10 - Carbon Monoxide. EPA Method 25A- Volatile Organic Compounds. ASTM D6348 - Extractive Fourier Transform lnfrared Spectroscopy Conducts emissions testing on a weekly basis including, but not limited to, the following test types: lnitial Compliance, Biennial Compliance, SemiannualCompliance & Quarterly Compliance. Alltests performed are in accordance to any and all Federal & State requirements as applicable (i.e. JJJJ, ZZZZ, 106.51 2, 117, PEA, etc.). Pefformed testing in Colorado, Utah, Wyoming, North Dakota, Montana, Kansas, New Mexico, Oklahoma, Texas, Louisiana (land and off-shore), Arkansas, Ohio, Pennsylvania, West Mrginia, New York, Kentucky, & Mississippi. . Quarterly Performance- Reviews covering ongoing changes with Federal Regulations, State Compliance guidelines, & site-specific safety certifications. GAS oo o NN N cq c oo o qq e ON N @( o ( o oo @ oo o oonq \ Nr or ) 6 NN N oo o @N N r@ o No i c i NN N ON@@ @ qq q oo r o @o @ @o N nq - NN N ao oo o oo o qq q oo o oo o aq o? a? oo o ) NN N o@o( o * @o ri s + oo rO ( , oo $ dc i c t qa q oo o 6@ O@@ o sN @ qq c oo o n( o o N9 0 q' : ' . NN N @N @ rO N qn l oN o o$ o q' : q oo o o$ o u? q u ? NO @ -N ( ) qg c l o+ s i oo o oo o qg g oo o 6r s i (O N N ': q o ? NO @ NN N oN ( ) NN N (? \ q or @ r oo o $t 6 rt O@o + NN N++ + ro < t oo o qg q oo o @o o 99 9 NN N oo o NN N oo o NN N NN N NN N NN N oo.=oo.YCL U) oo o oo o oo o oo o oo o oN o OF O o' j o N- O *N O q' : c oo o oo N $oqq q oo o oo o oo o oo o ci o o @@ o , o( o @ qo ? o ? rO O oo o oo o qe q oo o $+ 6 Al o l ol oo o qq c oo o @@ o o$ $ 6t o t oi c9 q N@ @ @@ @ oo @ oo o qq c oo o @n N qu ? a N@ o ) oo r o , oo o oo o oo o oc i o oo o oo o oo o oo c i oo o oo o qq q oo o -@ @ oN o u? c q Or 6N O os t ol o o Nd o ; oo o ) oo N oo N qq o ? oo o oo o oo o qq c oo o oo o oo o oo o oc r o N ox o a5 a o- i O o( ) { 99 9 NN N oo o NN N oo o NN N NN N NN . N NN N ooLi5(\ Iop(\ Ioz qq q oo o o@ @ Or n qq c NN N cq q 6@ O o@ @ @6 0 s@ o , qo ? 6 . | rO O oo o oo o do o r0 A ON N qq q oo o or N @r qc l a ? oo o oo o oo o oc i o oo o @$ o qc ' : oo o O, N O @o o oc i o NN @ ro @qq c oo o oo o oo o qq q oo o N+ C ) $oNr O do o @F @ ON N oF + -- O o( o 6 $o o oo o od o oo o oo o aa q oo o oo o oo o aa e oo o oo o oo o qq e oo o oo o oo o 60 0 oo c i $o o o$ o aq q oo o oo o oo o cq g oo o 60 N oo o oo o oo c i o@ @ Y? Y ? II ? @@ @ oo o NN N oo o NN N NN N NN N NN N oo.=oNo-c .9 )T rO O rC , O qq c oo o o( o NO O c! - ' : oo o qq q oo o oo @ (o * c6 ) c ? oo o cq q $$ N NN N o@ 6 OO N a? a ? ol (o 6 0 @o @ ro @ Or ci c t o $N e oo o qq q oo o oo o oo o qq 9 oo o oo o Nr O qq q oo o oo o oo o cc q oo o r) o @ SN N a? u ? a? oo o o) o o , oo o oo o qq q oo o oo o oo o qq q oo o oo o oo o qc q oo o oo o oo o qq 9 oo o @o o oo o cq q oo o Or O oo @ q. ' : oo o oo o oo o oo o oo o !t o @ orqq c oo o NO O qq c oo o oo o {? { ? Y? @@ @ oo o NN N oo o NN N NN N NN N NN N o$ @ oo o qq q oo o ooi5U'o cq q oo o o@ @ oo o qq q oo o cq q oo r ) NN N @@ @ oo o cq q oo o q\ \ oo o oo o oo o qg q oo o ON N o( o d) q ' : ooo o oo o cq q oo o oo o oo o gq q oo o oo o oo o cq q oo o Or O Or O q' : q oo o oo o oo o qq g oo o oo o oo o cc c oo o rN O@( o s t q9 q oo r@nq \ oo o oo o oo o oo o ct o o oo o oo o ee q oo o oo o oo o cq c oo o oo o oo o cq q oo o oo o oo o oo o oo o oo o oo o qq q oo o o0 t oo o qq q oo o NO \ t q{ $ $ t @@ @ oo o NN N oo o NN N NN N NN N NN N ooi5oL:=oo(UctU'oFo(L oogo qo@oo?NqoN@@o-NNAloNooN:oooqo\t6qNNNU?ooqNNq?No(ooAloots.too6oNoNNNN oqNeqoO)cooooo\NN8qooqoqo Eb(ua _qEE T o. o v FESa >o \ xvo .e ' g F €, P E oe OE ,g e x>OE zd g .BLt r (/ , E eoe $> IEsl o () o -Foto& o!NEo8xi u2 TE -a o -eOF IA o +! NEo8 .iot r u, -do a? -Fz- d ooi NF Z- d ool It roa q -lOF z6 - a ^t -C oa o: oa o *i -EEEGl ^os ovOa I5 (E+, (ro==oot=t oEFo(!o U)w oo.caooooo(ELoo=.E=r L_( u '6ooo t!J(o lo(o (r )o roc{ooF(L= id Io= Etto= o'l tEzTU 't roo oLoooo(, -c(U:) aoLo(U=ao)= dI .=cf troo -o.Eoo oltEz.=cf qc c q q q q c oo o o o o o o o@ @ o @ @ o o ac ) N o o N @N @ @ @ O @ @ Ni i x N N s N qq q c c q c q NN F t s N N N N 66 6 0 0 0 0 0 @@ @ o @ @ o @ N@ O O O O O O \o q q q \ q \ \ o( ) ( ) 6 ( ) 0 6 0 @( ) O O r r @ r $ Al o l . : ' : o l c ' : n @N @ @ O O O O ) NN N N N @ O N oo o o o o o o oo o o o o o o qq q q q q q q oo o o o o o o ON $ r @ O O N oo N 0 0 N @ N ': q o ? q 0 q d l q q TN N N N N O O ON O - O + @ O NO N T O T O O , qq q q q q o l o ) TN N N N N OC ) r { - - @ N F O oN 6 0 0 0 @ o tN N @ @ $ t { No t o t o t o o o i o ; ts r N N O N N OO r O . + O O O nq q ? c \ ] \ A l ': o l oN @ o @ @ @ N ON N N N N N N oo o o o o o o 88 8 8 8 8 8 8 y) oo o c r o o c i o < \ o oo o o o o o o oo o o o o o o qq q q q c q q oo o o o o o o OS r @ n e N N o+ N O r @ N O cA l o l a ? a q a ? q ? oo o o o o o o oN o o o o o $ oo N o o o @ @ q? o q \ a a q a ? A l o( . ) ( f ) o o o o c ) o* @ N $ o o o N@ { N * s f O O c? q q ' : q g q C TO O O O O O O oo o o o o o o oo o o o o o o oo o o o o o o oo d o o d c i c ; N$ F O T N F N o@ ( o N o ( o @ $ a? ' : a q ' : o q s ! \ oo o o o N N o NN O r ) O ( ' ) O O (o o o @ o o @ @ ON D O O O T @ ON $ n O r N O @o r O r @ @ O c, d d r j N N N N NN F O O @ O O @o o c ) @ : f o o a? o ? q c ! q a a o q NF o O T N N T n( o @ @ @ @ ( o @ oo o o o o $ o oO O O O O T O qq q q q q q q oo o o o o o o o @ O . O O r @ O @o N N @ O @ O ' @@ o o @ o @ @ +d d d d ( i d d -o @ @ o N @ N }- . @ @ r F o O O ud ? q ' : q r y a ? n JO -N O { D @ N @ is Y n n s s s oo @ @ @ 6 @ o oo o o o o o o $$ $ + * $ t t NN N N N N N N oo o o o o o o NN N N N N N N NN N N N N N N NN N N N N N N NN N N N N N N .EEoqoPJ.=Eo(f , Ic)0c qq q @@ @ oo o oo o od d cq q oo o o6 0 @o @ NO ) ( f ) o? A l .. oo o oN @ =t ': ol oo o@$ o oo o qg q oo o @N O *o o o ct o o rO@@ o qq q oo o ON NS 0 qq c oo o oo o $o @ cq q oo o oo $ ooqq q oc ) o oo o oo o oo o oc i o +r @ $@ N qq c oo o oo o o6 @ cq c l oo o N@ O oodo o @@ o NO N qq g oo o co o o , NO O ': q o J oo o oo o oo o oo o od c i ON N or @ a- o l oo o or ) ( o NO ) @ NNoo d oo o oo o qq g oo o OO N oo o qq q oo o @@ o ) NN N NN N oo o NN N oo o NN N NN N NN N NN N oE't roooCLootr .C :P _ =Eooaocoo(Um qq q oo o @@ @ NN N qq q oo o qq c @t s N 60 0 @@ @ $o c? u ? \ oc ) r ) o6 0 NN N @o ( o oo o ++ < o \t * $ NN N o@ @ o@ N NN N do i o t ON o@ o ne q NN N NO O FO O oq a q Or O o0 e NN N oo $ (o r ) o ': q \ 00 @ $o r o $o o NN N oo d o( o o oo o qc \ q oo o 6@ O ON O q? ': u? oo o oo o oo o dc i d ON N @o o t$ d Ai 6 i - oo c o oo r J ': q o q oo o (o o o 0@ r q? u ? q @o N !+ o $ oq q ? q \t ( ) c ) oo o oo o q9 q oo o or ) ( 9 oo @ qq a ? ss i @ :i $ $ NN N NO @ oo @ N@ O dc i + oo o N@ @ @o o NN @++ + NO r ) oo o qq c oo o os i ' * $t $ l 9! NN N oo o NN N oo o NN N NN N NN NNN N oEtroooo- CI 'oNE=Eoaaol<CLa cg q oo o @o @ qq q o@ o o( ) ( ) @@ o oN o q '. Al oo o oN @ qu ? q oo o oo o oo o qg g oo o NO O oo ( o qc q oo o oN @ N( O O OO r dc i c i NN N qq ' : oo o oo o oo o qq c oo o oo o oo o qc q oo o oo o oo o sq q oo o FN . + oo o qc q oo o oo o oo o oo o oo o oo o oo o qq q oo o oo N oo o Nr N od d NO N (o o N qo l n l oo o rO O OF \ t \o ? o q oo o oc ' r N oN o qa e oo o oo ) o N$ O o$ @ or O oi d o i $$ o rO @ qq ' : oo o ea a qq q oo o On r 90 0 oo$t $ t $t FN N oo o NN N oo o NN N NN N NN N NN N oE't rooCoo.ooE.C '= EoaaNop=oloz qc q oo o @6 @ o$ o e? q? 02 oo o qq q 6$ O @o ( o @@ @ NN 6 an q @@ N @o @ oo o cq q oo o oo o rO O qq q oo o @@ o ON N ': ' : Al oo o oN $ rN ( 0 qq q oo o oo o oo o eq q oo o oo r o $N O qq q oo o ON N OF O qq g oo o oo o oo o qq q oo o 66 S : o@ = soot o i e oo = o@ o oo o Or O cj - o Or o t s N( 0 m q' : ' : oo o oo o C, F O qg e oo o oo o oo o qq q oo o oo o oo o q9 c oo o oo o oo o qq q oo o oo o oo o oo o oo o oo N rO O cq g oo o (o o N qq q oo o (o @ o NN N oo o NN N oo o NN N NN N NN N NN N oEtroocoooot. -c '=Eo(r , U)aFo qq c oo o @@ @ qq c *: f \ t @@ @ oo o oo o qc q oo o N@ N u2 ': Al oo o FO @ ol o { q oo o o rO O oo o oo o NO O $N N oooc i c i N( ) N @o o oo o oo c i $o o 00 0 ac c oo o oo @ ooqq q oo o o@ N Or O oo o oo o oo c ) ooqc q oo o oo o oo o oo o ci o c i $o o u? ': ' : oo o oN o sN @ nq ? a oo o ON N OF o oo o ci o o oo o oo o cq c oo o oo o oo o oo o oo o oo o , oo N o? q q oo o tO N r N$ O \- qoo o NO O oo o qq q oo o oo N o ce q oo o NO O (r t s oo o \i \ t $ NN N oo o NN NNN . & NN N NN N o 6E ^ o. o \ , Fc9c ' xvo6d € €p € &4 5ol OE>o o> x>og oE@> rE(/ ) a o oa {>TE NqOo *e F> IE@XOo - o!oEo&@3 NEo& 9 u2 YE -o q -Eot r IA o *!NEoH *EOF u, -do .l IEza eol NF Z- d o oe tt roag -eOF z. - d ot o:zega o: oE d o Eooao.s6@(dm N^8ERs oEtrooo qq q q q :O O O O O :o o o @ @ rN o o @ o .( o N o (o N :N N N N N :Q q q q q :N N N N N :o o o o o :@ @ @ @ @ :O - O - N i@ O N N N 'c i d c i c i < ; Nr qO@NqN :0 :@:c i o :o:q '@ N :o:o:6 o ::'N,o qo ;N No?No@qoNNqNoO ,q oo 'o eoo ,c ? N a:Oro.N.^ i ro :O.c i :. O rq o@n;@NnOu?OO@ r N @ o S :N @ N N q :q \ o? ry '. 3 c, 3 h 3 3 3 IP E o N o o o X^ O @ N r O : V O N N 9( O c t d o o o r\ ,o OP O @ O S N o- @ @ o o @ \= c q o q q c q o q oL o o o o o oF o N N o @ O= N r O o @ o( J O N T N cj C ) ; - - - - .: * m o o r N o rN N N N 'o o o o o o o. o ,r o o o o o V vv v '= d = & d N N N L4 O J O O O O O :C I r S rr S S S S S -N N N N N N :N N N N N N Q! ? O o ON O a o r O N $ o N O $ N O @ @ @ oq og q q q q o o o @ o @ @ @ @ @ @ @ o o o 0 6 o o o o o o 6 r i d d d ri d d 6 6 ri rj o ri d d d @- @ @ O O r o o O O $ O o o 0 O O $ N N N a ! S a $ N o O F F N $ N N O O r o N $ o @ N( ? V O O N N N N N N N N N N N N N N N N NN N O ;; -- - ; ;- -- ; ;- - -- - ; -; - ;I - - = OO - N O $ O @ N @ O O N O $ O @ N @ O O - a I q? c? Y? I Y ? p r. t g? rI ? I I I I I Q I I 9 : . : . 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E E E q E E NN N N . - N N N & N N N NN N N N N N N N N N qq a gq q q q q q q q q g q q q q c qq qq OO O O O O O O O O O O O O O O O O O O O O O @ @ @ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ a O O 0 $ $ @ @ @ O r @ r N N r N $ O @ O @ Fl : q( 9 qq q q q q q \ q\ \\ \ \ \ \ qq q \6 NN N N N N N NN N N N N N N N N N N N N N N q q q q q q q q q c q q q q q q q q q c c q8 N N N N N N N N N N N N N N N N N N N N N N T ' o o o o o o o o o o o o o 6 n o o o 0 0 0 0 l : @ @ @ @ @ @ @ @ o @ o o o o o o 6 6 6 @ @ @ u $ o N OO @ $ oo O O O O O - O $ O O @ $ O t cq \ og \ \ oq q q q q oq q q q q , . q , . .. q q q x O O O o o o o o O @ O n O @ @ @ @ @ @ @ O @ r i O N A O N Q N O O N r OO A O Q r N N O O O R ] - q n q c q q o q \ q e ? q q n n \ a? 'Q q a q q c ? t s -N $ N rN OO r @N o o $ $ O O O @ @ O @ ; @o o o o 6 N N6 N N NN N N N N N N N N N K O O O O O O O O O O O O O O O O O O O O O OO OO O O O O O O O O O O O O O O O O O O O OO ' cq qq q q q q q q a gc q q q q q q q q q q . oo o o o o o o o o o o o o o o o o o o o oo @r O @ O $ N @ N O O $ @ @ O O N O A @ N $ - : $ r o@ N N O N o N S $ @t S r @N @ O O O U . q - q q 1' . ' . ' : ' : q q C c. ! -' . ' . ' . '' .. q .. q : oo o o o o o o o o o oo o o o o o o o o oo :: -O r @ @ r N A @ N V @ N O N @ N O O N T $ - : NN @ O @ O o o - @O N VO O @ @ N O O a 6 : q q q q q o? q q q q q q ot q q q ol q ot q q q q : NN N - O $ $ N $ - O O N @ N O O . + $ N @ O O $ O No @S O@ O $ @O O - O @ O O @ O N N N O $ No I a q a u? q q q q oq q q q a q q \ q 0 9 0 q \ cq q o o o o o o o o o o o o o o o o o o o o i o f o t o O@ O r @ O r O O $ N r N @ $ O O N O N N O @ O O N @ O - @ $ N O N N @ O - O S O N N Oc t c2 c ? q a ? \ \ c? c q () n q q a? q, . q c! o o s o @ @ @ @ @ @ o o o o o o o o o o o o o o d og i NN N N N N N N N N N O N O O O N O N N N N O O O o O o O O O o O o O O o O o o o O o oQ o o o o o o o o o o o o o o o o o o o o g g 8 qq q q q q q q q q q q q q q q q q q O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O O Q OO O O O O O O O OO O O O O O O O O O O O O q q q c q q q q q q q c c q q q q q q q c c q O O O O O O O O O O O OO O O O O O O O O O O O r @O O @ @ N @O @ @ $ $ @ O N O O r N @N @r @o $ N r @@ o o o s r - o o v N $ N o@ c? n c' l A l o ? n o? o1 c ? e ? c ? a c' , 1 Al n q I c? q? c! c ! c ! ll o o o o o o o o o o o o o o o o o o o ci o o o N @ O N O N O t s O O O @ @ @ O @ O O @ O $ S t O oO @ $ $ O O N o N O o S O $ O O r @ @ $ c? . At q \ \ q q o q q c c o q q q q q q q , . c q q \q OO O O N N N NN N N N N N N N N N O N N N N OO O O O O O O O O O O O O O O O O O O O O o o o o o o o o o o o o o o o o o o o o o o @ c? g q q q c q q q q q q q q Q c c Q o o o -9 o o o o o o o o o o o o o o a a o o o c i o c i o O O O O OO O O O O O OO O O O O O O O O O O Q O O O O O O O O O O O O O O O O O O O O O Q OO O O O O O O O O O O O O O O O O O O O O O o d c i c i o d o o d c i c i d o o o o o o o c i o d o @N N O @ Al n a a a ? NO N O N NN N N N NO O O O OO O O O '. q q q q oo o o o OO O O @o N o o ,. - c . l ,. q OO O O O O@ O - @r r O O ac q \ a a ? @o o @ o NN N N N : EE E E T a := : = = <o rO O O o O to o o o o 'q q q q q OO O O O @N @ - @ '_ O O oq q? ol o ? Al OO O O O NO N N @ SN V r O \\ a o q r | NN N N N oo o o o OO O O O qq q q q OO O O O OO O O O oo o o o cq q q q oo o o o OO $ F @ N$ O @ c2 q q a ? c . l @N @ $ @ oo $ $ $ @o o o @ NO $ N N O@ V F N O@ N N N ri N C i N c t NN r O@ $ OO N O r NO O @ @ O - N@ r NN S F NN @N O @ $ N@ O O O @ O O @ @ N O @ i N r O @ O O N N O O O @O A N O @ $ @ N $ No ? d rj oj cj s s c t 6 @ d s - d r i @ + - s r j + + o j I oo o o o o o o oo o $ o s $ < v $ $ $ s $ e j @@ @ @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ @ @ @ NN ON @ O $ n r O r Or N O@ @ r No - sE @O O N O O o O $ $ N N $O $ OO @ rO o N9 g q q G l . r q q l ! I \ ot q \ q (| a a q $ - $Y @o o o o o @ N o N N @ @ @ @ @ @ @ N N d NN NO NN N O N NN @O N S O O O N O r OO O @ q) o o N N o @ o 6 N @ N o o o I o o @ @ o o q q q n q q 1 c. t \ 9 , . , . c? a q c q \ - n o (. o @: O O $ O N O r O N o O N @ N N @ N N o o i c j d P @@ @ @ @ o @ (o @ o @ 0 6 0 e o o 0 0 0 (o a O$ N O O O @ @ F S 9 @ @ T T O O A N O a! ? N N @O N N @ O @ OO O O O N @ @ @ N @ + q c. : c\ l n a? a l ": Al , . ol q , . c l q a, . , . c! - A! -: oo o o o o o o o o o o o o o o o o o o o o NO O 6 0 NN O @ $ qq q q q @N @ . ^ O oo r : 1 q ': q B '. 39 9 o i 9 qqoooo NSNFcc NNoo@@ N@qqoo q q q g q q q q q q q q q q e q q q q o o o o o o oo o oo oo o o o o o o o oo o o o o o o o c i c; d d d o o .; @o @@ @ @ @ @ @ 6 @ @@ @ 66 @ @ @ @ 6 4 6 d6 6 d 6 6 6 i6 6S NN r $ o r ON O N s O@ $ $ @ O o O No o s9 o > > \ \ \ \ q \ a { - c e q a e a e q q q q < q aE E E NN N N N N N N N N N N N N N N N N N N N N N N * I t s ' O _o6 Er ' : (- ) .o y Fc8, a xvo 3f r 8 E^ ' E ., EOE>o o:"l ot r g .e IEoaeo9 IENOog :c IFE* NO ,o.d d :o o :o o OO :q q :o o OO :@ 6 ,a i d q c q c q q q q q q q q q q q q q q q q q q q q c8 8 q \ N N N N N N N N N N N N N N N N N N N N N N N N . - . . A A oo 6 o @ o n 6 o e o o o o o o oo o 6 6 k ) i . ! > r i1 @ @ o qi q i o @ @ @ o @ oi @ @ @ qt o qi @ 6 6 U U U U U St s U @ r O N $ r N o Q N N O @ O O @ 0 A r N @ O $ N N - ts . o N A i . ! : N; o t F b N 6 o 6 ( o oi o o S 3 I $ E S FE \ @ c t @ @ d d @ @ o c , c t @ rj r i d d d @ o o o 6 o o o d; , J -; - q q E + E € N s E q i f f N E g E E 6 N E c I 5 s e FE :i o o o o o r o o r g o - o o N a N s - I; ; ; : ; = BB 3 N @ @ N @ N N N N N N @ @ @ o 6 @ @ @ @ @ oi o o i y b x : , :: Q a Q O - o o O O O o o O O O O O o O O O O O o O o o Q o o o o o o Q a a o o o o - o - O 6 - - - - - - d 6 : :o q q C q q q o o o o - o O o - 6 - o o - - 6 - 5 - 6 5 , .5 o o o o o o c i c i d o o c i d c t o o o o c i c i d o d c i c t d c t c; 1: -@ F N N O @ O N T O O O $ $ O O O O ri d ci c i ri c i c i r i d c i r i r i r i c t r i ri r i c , c t c i e i ci a i r i ^i ct c i c; $Q N @ O o r $ N n 6 @ N T N T o N N O O N - @ O O 6 $ : r Q Q O r O o q) N @ o o @ @ N N N 6 o O N d l < 6 6 .@ qq o q q qq q q q o ? a qq q q c q q c e a ci c qa q q c N N N N N N N F - lo N 5 R B R E B 3 3 o ? r @ r o N $ o o q- , N r @ @ - 9- E NN - - O ; E ( Y X @ > . @ $ N r N o s O O @ @ O o o E - O ;; o J E o : ' yo y N N N o 6 N N N N @ o 6 ( i ( j : . 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Q' : ? - 6 o o N N N N o o N N N o N N N N o N N o o o o o o o o ri a i d$ E E E E E E E E E g E E E E E E E g 3 E E E E E E E E EE oo o o a o a o o o o o o o o o o o o d o o o o o o dc i o oo o o o o o o o a e o o o o o o Q e > o o o oo Q o o o Q - - 6 - - - -6 6 - - - 6 - 6. 6 O O 6 - - o O a Q a a P q q q q q q q a q q q a c q Q q c c c q c q c 9I ? ? ? : OO O O O O O O O O O O O O O O O OO O O OO O O O O O 9 o!OE () &ol NEo8 ; u) rc_o o -l (J F IO o s3 NEo& .lOF@- d o -l IEz. A ooi NE Zn o P E H } g E 3 E q + E P S F H F H H R $ S R H g R N E Eq * 6 .: i j ; @ ; d - ; - d o d d oj ^i d d Ai a a .9 t- \ d r, d ri S 'o di N c5 6 . 1 6 6 6. i o o $ < 6 < + < o n @ o o @ rD (9 a a A A d @ qi q i c6 o @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ @ + S U B E X B B U R + d @ $ o o r (e o @ @ @ @ @ N o - os q q c? '. \ o? c2 q q or cq q "c E N I 5 q 5 3 I 3 3 S q b i € q oi N N N N d I N N N N N N N N N N N T N - N r H H $ H P $ $ $ H 8 P S H S R E E R E E B 3 E fi H H E q. 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' . 8 : T fr f r E fi E I i $ t { g s + I I ff E s fr ff fr f r E q E E s I s I9 y -o o o O O O O O O O O O O O O O O O O O o O O O T T < a E$ $ v $ $ $ r $ $ $ < 9 $ s s s $ s $ $ v s . s s $ $ + s $ s 5 = N N N N N d r c n d r d N N N N N cn N cn N N N N N N N N N N N N N E J d d c j c j d c j 6 ci - cj - o o o o o o o o o o o a Q o o o Q a Q rr 'N { { { { { { { A { S { S S s! s t E E dr N N N N N Ar N N N N N N N N N N NN N N N N N N NN N O N N N N N N N N N N N N N{ N N N S S S S S S S * s s s s s s * S S S $ * S S S S S NN N N N I OO O O O O O O O O O O O O O O O O O O O O O O O O O O O o c j o c j - ci cj d o d c t d d d c i c i d o c j c j o o o o o o o f o o , @@ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ o o N o o ' NN O @ @ O - N @ N O @ O N $ @ O O N - S N S N @ N O @ O I \ \ \ \ \ \ 0q \ \ oq o q o q q q \ \ \ 09 \ q o q q o q \ q o q q c q q , NN N N N N N N N N N N N N N N N N N N N N N N N N N N N qq q q c q q q q Q c c q q c q c q c q q q q q q q q q q NN N @ @ N @ N @ N N @ N N t s N N N N N N N N t s N N N N N 60 0 0 0 0 a o o o o 0 0 n o 0 0 0 0 0 0 0 0 0 @ o o o o @@ @ @ @ @ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ o @ o o @ @ o Oo N r O @ @ @ O o @ O O @ @ O @ O O $ N o o o i o N r @ '. . q q cl q q ' . 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N N s $ ss - s " s s N N N N N N N N N & N & N S S S S S S S S S S S S S S S S _o6 E , i o. o y tE3, : ; xvo .E sF oo oEr e ., 8OE>a :"lOF Z- d e€ o> LE <t , -ogo9 s> -ENOog {a IEEe ooqO :O 'O.c t :o:Oto:c t , oo :O:d ::o 'o:c oo@C\ ]oqoNci o3 oEo&o!T' NEo& ! u2 TE _o q -l () F !o o *FNE (' ) & *lOF oa o -i IFZ- d ool Nt s Z- d o oood: : .o.O,o : o .: :N : a0 '6 - NC i5 0 d( o \ :o o#O- og .E (o L50 .' t o C r ) oo < Yl := r mo(/ ) s ( : (U 3 f MS (r N:N oEtrooo ol IEoa o .EOF Z- d o^to; o: oE 'c @ :o o :o ::O:d:o:o:' : :Oloro C;ooqOoqOo@qo N^os ovOa N> S ,q q q q q q q q q q q q q q q q q q q q q q q q q q OO O O O O O O O O O O O O O O O O O O O O O O O O -@ @ @ @ @ @ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ oo o R oN @ q\ q NN N oo N OO O N N T qq \ \ \ q \ \ NN N N N N N N NO $ O O N - N q\ q u ' ? q \ \ \ \ NN N N N N N N N .O O O O O O O O O O O O O O O O O O O O O O O O O O NN N N N N N N N N N N N N N N N N N N N N N N N l \ o o o 0 0 0 0 0 0 0 0 0 0 0 @ 0 0 .o o o 0 0 0 0 @ @@ @ @ o @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ o @ @ @ @ @ oo o o N o 6 @ o o o o N O o N a $ @ o @ o N N N $ q q q q \ \ o? q q q \ oq q c og \ q \ \ oq q q q o q c q r@ o o o e o o @ s @ @ o @ @ o a o o @ o o o @ @ o NF oT N O O O O $ O @ - $ @ r 0 - O N O O O n T N N O a \ q q q c ? 0 2 u) '. q n \ q a ? '. cq n q \ oq - cq '. (q '. c2 @N O O O O O $ O N N O @ F N @ O N O N O @ $ 6 $ O N@ @ @ @ @ N N N N @ @ N @ N N @ N N N N N N N N N @r o o r o N O r O O O O O N O O - O O O O O O O O @O O O O O O O O O O O O O O O O O O O O O O O O O '. g q q q q c g q q c q q q q q g q q q q c q c q q OO O O O O O O O O O O O O O O O O O O O O O O O O Or N @ N @ N $ O N N T O $ $ $ r N o O N o @ O @ $ NN O T O O N @ - S N @ O @ @ r N @ O @ r O - $ C ) @ q q q q o q a q o q q q g q ' . q q q q q q q o g q q ol g q NO O O N N N N O N O O O N N N N N N O N N N N O N . NO O O O @ O N F N @ N O F @ O O r O $ $ N N O N @ I OO O o N O @ T O O N O O O N N O O T O - N @ O @ O : qq q q q q q c q g q q c q q c q q a q q q q q q o ) NN N N N N N N N N N N N N N N N N N T Po s o o @ @ s o o o o @ r o N @ s o r e N N @ N r . 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() F -6 . o *!NEo& .lOE@- d g o5 IEz- d ool NF Z- d o oo + + @ F b b N E {B 3 3 s s sE oo 6 0 ol -Eo6 . a @N O N O ' N 3I 5 3 EE P = P P 9T E P h P 5 E or o s - ' ' ! 3 3 b h E E r@ O NE€ q E E E oo o o 8E Z- d -9 OE ze go9oe q $N O O 6 6 @@ o o 6 N @@ @ @ o @ d ri d d dd OO r O NN O N 6 O Ni jj;; rN o t R NN N N D < ' NN N N i < -o $r f $ $ 3 NN N N T oo o o NN N N NN N N NN N N NN N N N^os ovOa NX Iv 0,EFooo 40 CFR Part 60 Subpart JJJJ Performance Test Report Test Type: lnitial Test Date: A2A2O24 DOM:111109 Source: Caterpillar G3516LE Lean Burn (4 Cycle) Unit Number: Unit C Seria! Number: WPT00209 Engine Hours: 6031.3 Location: West Water CS Grand County, Utah Prepared on Behalf of: Utah Gas Corp Test Started: 01:10 PM Test Completed: 05:23 PM ffiAs 303 W. 3rd St (580) 225-0403 Elk City , OK73644 lndex 1.0 Key Personnel.... ............. 3 2.0 Sampling System..... ....... 3 3.0 Methods Used........,... ......................... 3 4.0 Test Summaries.. ............ 5 5.0 Run Summaries.. ............ 6 6.0 Volumetric Flow Rate Data.... ............. 7 7.0 Calculations.............. ...... 8 8.0 Oxygen Calibration... ...... I 9.0 Engine Parameter Data Sheet.. .......... 10 10.0 QA/QC Results........ ........ 11 11.0 D6348 Annexes...... ........ 12 12.0 Signature Page........ ....... 18 13.0 Appendices.............. ....... 19 14.0 Bottle Certs............ ......... 20 15.0 TriProbe Certification via GD-031 ...... 26 16.0 GAS ALT 141_FT|R EPA......... ..,........27 17.0 Tester Qualifications (resume)... ......... 29 18.0 RawData........ .. i;t;; .......... 30 Table 5.1 (Run Summaries)............. ........... 6 Table 6.1 (Volumetric Flow Rate Data)........... ................ 7 Table 6.2 (Stack Gas Measurements)......... ....................7 Table 8.1 (Oxygen Calibration).. ................. I Annex Table 1.2.1 (Certified Calibration Bottle Concentrations)......... 12 Annex Table 1.2.2 (Measurement System Capabilities)..................... 12 Annex Table 1.3.1 (Test Specific Target Analytes)............................. 13 Annex Table 4.1 (Measure System Capabilities) ............ 15 Figures Figure 6.1 (Location of Traverse Points per Method 1).......................7 Annex Figure 1.4.1 (Sampling Train)..... ..... 13 Annex Figure 1.4.2 (Sampling Points)... ...... 14 Annex Figure 1.4.3 (Sampling Port Locations).... ............ 14 Appendices Certified Calibration Bottle Certificates-............ Tri Probe Certification via GD-031... GAS ALT 141-FTIR EPA............. Tester Qualifi cations (resume)... Raw Data..... 20 26 27 29 30 1.0 Key Personnel GAS Utah Gas Corp Carlos Gamboa Derrick Timothy 2.0 Sampling System The sampling systern used consisted of a Stainless steel probe, heated Teflon line, gas conditioning system, and a Gasmet model DX4000 FTIR analyzer. The gas conditioning system used was a Gasmet Personal Sampling System with a Zirconium Oxide oxygen sensor. 3.0 Methods Used ASTM D6348.03 This extractive FTIR based field test method is used to quantify gas phase concentrations of multiple target analytes (CO, NOX, CH2O, & VOC's)from stationary source effluent. Because an FTIR analyzer is potentially capable of analyzing hundreds of compounds, this test method is not analyte or source specific. The analytes, detection levels, and data quality objectives are expected to change for any particular testing situation. lt is the responsibility of the tester to define the target analytes, the associated detection limits for those analytes in the particular source effluent, and the required data quality objectives for each specific test program. Provisions are included in this test method that require the tester to determine critical sampling system and instrument operational parameters, and for the conduct of QA/QC procedures. Testers following this test method will generate data that will allow an independent observer to verify the valid collection, identification, and quantification of the subject target analytes. EPAMethodl &1A The purpose of the method is to provide guidance for the selection of sampling ports and traverse points at which sampling for air pollutants will be performed pursuant to regulations set forth in this part. EPAMethod2&2C This method is applicable for the determination of the average velocity and the volumetric flow rate of a gas stream. The average gas velocity in a stack is determined from the gas density and from measurement of the average velocity head with a standard pitot tube. Velocity readings are taken from each stack at 16 separate traverse points (Table 6.1) and used to determine the engines mass emissions rate, calculated utilizing the formulas seen in section 7.0 of this report. EPA Method 3A This is a procedure for measuring oxygen (O2) and carbon dioxide (CO2) in stationary source emissions using a continuous instrumental analyzer. Quality assurance and quality control requirements are included to assure that the tester collects data of known quality. Documentation to these specific requirements for equipment, supplies, sample collection and analysis, calculations, and data analysis will be included. GAS 4.0 Test Summary Unit Unit C with a serial number of WPT00209 which is a Caterpillar G3516LE engine located at West Water CS and operated by Utah Gas Corp was tested for emissions of: Carbon Monoxide, Oxides of Nitrogen, and Volatile Organic Compounds. The test was conducted on 212212024 by Carlos Gamboa with Great Plains Analytical Services, lnc. All quality assurance and quality control tests were within acceptable tolerances. The engine is a natural gas fired Lean Burn (4 Cycle) engine rated at 1340 brake horse power (BHP) at 1400 RPM. The engine was operating at 1029 BHP and 1398 RPM which is 76.80% of maximum engine load during the test. The test HP calculation can be found on page 8. The engine was running at the maximum load available at the test site. This test will satisfy the testing requirements for 40 CFR Part 60 Subpart JJJJ. Site Verification Photos GAS 4.0 Test GAS 6 5.0 Run Summaries Table 5.1 Run Summaries GAS 6.0 Volumetric Flow Rate Data Table 6.2. Stack gas pressure measured with a standard tube use for Aostd = Velocitv head measured bv the' standard pitot tube, (in.) H2O.' uamole aner EacK Huroe.o.77 Within 5% of Last Apstd readinq:Yes Figure 6.1 16 Traverse Points Were UsedStack Dlameter (inches)26.00 lnches upstream from disturbance 14.00 lnches downstream from disturbance 92.00 Pitot readings are taken for Method 2 calculations using measuring points outlined in Method 1 *The exhaust stack dld not present cyclonlc flow condltlons at the sampllng locatlon due to the absence of cyclones, lnsrtlal demisterE, venturi scrubberc, or tangentlal lnlets. * Cyclonlc Flow Check (PasslFall): PASS Table 6.1. Data used for volumetric flow rate (Method 2) GAS 7.0 Calculations Method 2: Determination of Stack Gas Velocitv and Volumetric Flow Rate *Note- Use of this method neqates the need for anv fuel related numbers for emissions calculations Ap(avg) = Velocity head of stack gas, mm H2O (in. H2O). 3600 = Conversion Factor, sec/hr. A = Cross-sectional area of stack, m2 (ft2). Bws = Water vapor in the gas stream (from ASTM D6348) Cp(std) = Standard pitot tube coefficient; use 0.99 Kp = Velocity equation constant. Md = Molecular weight of stack gas, dry basis, g/g-mole (lb./lb.-mole). Ms = Molecular weight of stack gas, wet basis, g/g-mole (lb./lb. -mole). Ps = Absolute stack pressure (Pbar+ Pg), mm Hg (in Hg) Pstd = Standard absolute pressure, 760 mm Hg (29.92 in. Hg). Qsd = Dry volumetric stack gas flow rate corrected to standard conditions, dscm/hr. (dscf/hr.). Ts(abs) = Absolute stack temperature, oK ("R). = 460 + Ts for English units. Tstd = Standard absolute temperature, 293'K (528 "R). Vs = Average stack gas velocity, m/sec (ft./sec). Md = .44(.055)+. 32(.096)+. 28(.849+0) = 29.227 LB A_B-MOLE Ms = Md(1 -Bws)+18.0(Bws)Ms = 29.227 ('t -. 1 0664)+. 1 8.0(. 1 0664) = 28.03 LB/LB-MOLE vs = Kp-cp(stdl-y'apavg.Vffs(abs)(Ps-Ms))vs = 85.49-.99""/.At"l1',t tZS.AZ 425.32.28.03)) = 84.65 FTISEC Qsd = 3600(1 -Bws)Vs-A((Tstd.Ps)(Ts(abs).Pstd))Osd = 3600(1-.107)84.65'3.687((s28'25.3211 (1173.67'29.92)) = 382190.87 DSCF/HR Q = Qsd135.315 Q = 382190.87/35.315 = 10822.338 DSCM/HR Emission Rates (Examples use CO Run 1 453.6= Conversion factor lb. to gram HP= Engines rated Horsepower A = Cross-sectional area of stack, m2 (ftz). Mfg.= yqnul.cturer Exhaust flow rate at 100o/o (ft3/min) BHP/HR. = Brake work of the engine, horsepower-hour (HP-HR.). 02 = Concentration of oxygen on a dry basis, percent. BTU/HP-HR. = Brake Specific FuelConsumption (HHV) ppm= Parts Per Million (CO) ER = Emission rate of (CO) in g/HP-hr. ppm@15% 02= PPM corrected lo 15/o02 F(d )= yslumrs of combustion components per unit of heat Qsd = Dry volumetric stack gas flow rate corrected content, scm/J (scf/million Btu). to standard conditions, dscm/hr. (DSCF/HR.). Q = Stack gas volumetric flow rate, in standard cubic meters Run Time = Run Time in Minutes per hour, dry basis Tpy= Tons per year LB/HR.= Emission rate of (CO) in LB/HR. Vs = Average stack gas velocity, m/sec (ft./sec). Mol M.= Mol Weight of CO (28.01) ppm @ 15% 02 = PPM'((20.9-1so/o02)l(2o.9-O2))ppm @ 15% 02 = 1.29s-(20.9-15y(20.9-9.6oh)) = .676 PPM @ 15% 02 g/hp-hr = (PPM'(1.1 64.1 0r3)-Q-(Run Time/60))/BHP/HR (1.295.(1 .164'1043f 10822.338.(Run Time/60))/1 183.349 = .014 G/1-lP-HR lb/hr = ER'1 /453.6'BHP-HR LB/HR =.014'1/453.6-1 183.349 = .036 LB/HR TPY = .036'4.38 = .158 TPY = Available HP - ((MFP @100o/o - Actual MFP inHG) / ((MFP @1000/" - MFP @75olJ l25o/"\\\ - Available HP 1183= 1339.04 - ((70-63) I ((70-55.2) I 25o/o))). 1339.04) ppm wet - (1(1-H2O) - ppm dry 1.29 = 1.1 565'(1(1 -.1 1 )) GAS 8.0 oxygen calibration 9 8.'l Calibration error test; how do I confirm my analyzer calibration is correct? After the tester has assembled, prepared and calibrated the sampling system and analyzer, they conduct a 3-point analyzer calibration error test before the first run and again afier any failed system bias test or failed drift test. They then introduce the low-, mid-, and high-level calibration gases sequentially in direcl calibration mode. At each calibration gas level (low, mid, and high) the calibration error must be within i 2.0 percent of the calibration span. 8.2 lnitial system bias and system calibration error checks. Before sampling begins, it is determined whether the high- level or mid-level calibration gas best approximates the emissions and it is used as the upscale gas. The upscale gas is introduced at the probe upstream of all sample- conditioning components in system calibration mode. (1) Next, zero gas is introduced as described above. The response must be within 0.5 percent ofthe upscale gas concentration. (2) Low-level gas reading is observed until it has reached a final, stable value and the results are recorded. The measurement system will be operated al the normal sampling rate during all system bias checks. (3) lf the initial system bias specification is not met, corrective action is taken. The applicable calibration error test from Section 8.2.3 of EPA Method 7E is repeated along with the initial system bias check until acceptable results are achieved, after which sampling will begin. The pre- and poslrun system bias must be within t 5.0 percent of the calibration span for the low-level and upscale calibration gases. 8.3 Post-run system bias check and drift assessment - confirming that each sample collected is valid. Sampling may be performed for multiple runs before performing the poslrun bias or system calibration error check provided this test is passed at the conclusion of the group of runs. A failed final test in this case will invalidate all runs subsequent to the last passed test. (1) lfthe post-run system bias check is not passed, then lhe run is invalid. The problem is then diagnosed and fixed, then another calibration error test and system bias is passed before repeating the run. (2) After each run, the low-level and upscale drift is calculated, using Equation 7E-4 in Section '12.5 from EPA Method 7E. lf the post-run low- and upscale bias checks are passed, but the low-or upscale drift exceeds the specification in Section 13.3, the run data are valid, but a 3-point calibration error test and a system bias check must be performed and passed prior to additional testing. Table 8.1 Oxygen Calibration Method 7E 3.4 To the extent practicable, the measured emissions should be between 20 to 100 percent of the selected calibration span. This may not be practicable in some cases of low concentration measurements or testing for compliance with an emission limit when emissions are substantially less than the limit. EPA Method 3A QA Worksheet Certified Gas Concentraion I Certifled Gas Concentraion I Certifiod GaB Co Low-Level (%l I Mld-Level (%l I Hiqh-Leve 0.000/o I 9.12o/o I 21.020, ncentraion 7E B.5: Note: that you may risk sampling for multiple runs before performing the post-run bias provided you pass this test at the conclusion of the group of rUNS (DIRECT) Analyzer Calibration Error (< 2%) Linearitv Check Certified Concentration Value (%) Direct Calibration Response (9 Absolute )ifference (o/o) Analyzer Calibration Error (%) Zero Gas o/o 0.00o/o 0.00%0.0070 0.00% Mid-Level Gas % High-Level Gas o/o 9.120/o 21.020/o 9.14o/o 21.O2o/o 0.02o/o 0.00% 0.11o/o 0.00o/o (SYSTEM) Calibration Bias Checks (S 5%) and Drift Checks (s 3%)Upscale Gas 9.12o/o Zero Offset 0.00% Bias Pre lnitial Value Bias Post lnital Values Span 21.02 Analyzer Calibration Response (o/o) Zero Gas 0.000/o System Calibrations Response Pre (Yo) System Bias (? of Span) Pre System Calibration Response Posl (o/o) System Bias (ol of Span) Post Drift (Yo of Span) 0-00o/o 0.000/o 0.00o/o 0.0070 0.00% Upscale Gas 9.14o/o 9.09o/o 0.27o/o 9.06%0.390/o 0.00% (SYSTEM) Calibration Bias Checks (s 5%) and Drift Checks (s 3%) Avo. Gas Concentration (Run 1)9.55Yo Effluent Gas (Coas) Run 1 9.607o Avg. Gas Concentration (Run 2)9.11o/o Eflluent Gas (Cgas) Run 2 9.16Yo Avg. Gas Concenfation (Run 3)9.050/o Effluent Gas (Cgas) Run 3 9.090/o EPA Method 3A QA Worksheet Zero Gas 100% Nitrogen Mid-Level Gas 9.12o/o High-Level Gas 21.O2o/o Zerc Gas o/o Mid-Level Gas o/o GAS 10 9.0 Engine Parameter Data Sheet AS Anitk*ifi I &rr*qcras, Irta Company Utah Gas Corp Facility WESI WATET CS Date 2t22t2024 Site Elevation (ft)5077 unit lD Unit C Mal(e Caterpillar Model G3516LE Serial Number wPT00209 Technician Carlos Gamboa Run I Run 2 Run 3 Completed Run Start Times 01:10 PM 02:4E ]'M 04:04 PM 05:23 PM Engine Hours 6028.3 6029.3 6030.3 OUJI.U EnEine Parameter Data RUn 1 Run 2 RUn 3 Averaqe Engane speed (RPM)1399.0 1398.O 1397.0 1398.0 lntake Manifold Pressure (psil 3I.U 26.0 26.O zt.t lntal(e Manafold Temp "F 127.4 125.6 tzz.u 125.O ENEINE LOAd (EHP)183.3 95:z.4 951.7 1UZV.2 Ambient Temp "F 51.0 52.0 52.O 51.7 Humidity 70 31.O 30.0 30.0 30.3 Dew Poant "F 22.O 21 .O 22.O 21.t AFR Manulacturer/Type Caterpillar I CaterDillar Caterpillar I Caterpillar suction Pressure 117.4 117.2 1U2.2 112.4 Dascharqe Pressure 302.0 3UZ.U 306.0 303.3 Gatalvst (Yes or Nc Yes Catalyst Manufacturer EmeriChem EmeriChem EmeriChem EmeriChem # of Catalvst lnstalled 1 1 1 Catalvst lnlet Temp 'F 882.0 9't2.0 91 1.0 vut Catalvst Outlet Temp "F E6E,O 899.0 E95.0 447.3 Catalvst Pressure DroD H2O 2.9 3.2 3.4 3.2 GAS 11 10.0 QA/QC Results System Zero Response Time System Response Time 45 SeCOnoS 45 seconds Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Oxygen Average:0.00 Average:0.00 Average:0.00 Average:0.69 Average:0.00 CTS Compound Concentration Avg Tolerance Difference between measured and expected Value:99.40 2.O0o/o 0.60% Nitrogen monoxide NO Nitrogen dioxide NO2 NOx voc Average:0.40 Average:0.00 Average:0.40 Average:0.33 Average:0.00 CTS Bottle Concentration CTS Compound Concentration Avg Value: 100.00 Value:99.65 5.00% 0.3s%Ditference between measured and expected Equilibration Response Time Spike Reported Spike Expected 45 seconds Value: 251.O7 Value: 251.00 Gas, lnc. 12 11.0 D63/t8 Annexes 1€ 1.2 The test quality objectives completed for the emissions test are demonstrated throughout Annexes 1,2,3, 4,5,6,7 & 8 as layed out per ASTM D6348-03. All reference methods, pre-test and post test procedures were within acceptable limits. Data generated during the pre-test and post-test procedures are summarized below in order of the distinctive Annex. Three 60 minute test runs were performed. The final analyte concentrations are the average of each test run. Data was taken at 60 second intervals. Each 60 second measurement was the average of 600 scans. Propane is used as the surrogate compound for the Annex 5 Spiking Technique due to Propane being the VOC that is most commonly found in the combustion process of natural gas. Additionally, the molecular wei$ht of Propane coincides with with molecular weight of VOC's per the EPA. Annex Table 1.2.1 Certified Calibration Bottle Concentrations Botue Expiration NO2 Ethvlene sF6 02 ("/ol cc41s750 5t8t2026 9S_10 9.12o/o cc1 17503 8t15t203'l 100.00 ALM020982 11128t2030 21.027, Cylinder # CC142828 Expiration: 12-06-2030 Propane GO NO sF6 tsotfle value 251.OO 501 .40 252.40 v. /u Analyzer system Hesponse 251.O7 494.61 245.33 9.14 Percent Difference O.O37o 1.35"h 2.EO"/o O-13o/o Annex Table 1.2.2 Measurement System Capabilities GAS Annex Table 1.3.1 Test Specific Target Analytes and Data Quality Objectives Compounds Infrared Analysis Region (cm-l) Expected Concentration Range Measuremenr System Achievable Minimum Detectable Concentrations Hequrreq Measurement System Accuracy and Precision lor Test Application CO 2000-2200 0-1200 ppm 0.1626/ ppm 4 ppm NO 1 875-21 38 o-1000 00m 0.4007 ppm 2 ppm NO2 2700-2950 0-100 ppm o.4899 ppm 2 ppm VOC 2600-3200 0-100 ppm 1.8520 ppm Tota VOC'S 1 ppm perVOC91 0-1 1 50 2550-2950 CHzQ 2550-2850 0-100 oom 0.7878 DDm 1 Dpm lnterlering Compounds - CO is analyzed in a separate analysis region than CO2 and H2O coz 926-1 1 50 0-10%Oo/"nla water vapor 3200-3401 O'22"/o O.2O"/o nla * VOCs compiled of Acetaldehyde, Ethylene, Hexane, and Propane. nex 1.4 PROEE GASMET FTIR PAtlEt FLCI\' i[IR. Figure Annex 1.4.1 Sampling Train The testing instrumentation is housed in an enclosed vehicle which is located approximately 45 feet from the source. A heated sample line (sixty feet in length) is attached to the inlet of analyzer system and the source effluent discharges through the FTIR outlet. l ru cils 02 SENSR -1*f*lr STACK GAS 14 Sampting Point Locations in lnches 16.7o/"4.342 l"h 13. 83.3%21 .65 TRI.PROBE SA[',PLE POI NT LOCATIONS AS PERCENTAGE OF STACK DIAMETER Figure Annex 1.4.2 Sampling Points lnterior Stack Diameter (inches): lnches Upstream: 14 lnches Downstream: 92 SAMPLE PORT LOCATION DETERMINED BY DISIANCE FROM USruRBANCE Figure Annex 1.4.3 Sample Port Location GAS 15 um Detectable s N Ti A 7I''' : r"trr.5 REF 7II : r?71s' MDC#I: F \, "1" (w e ,tT), f,rr / 'i : L ttlN E Al-r,ts' c.*l L."t -* It E l-' ttt rttls Lre'lt Target Analyte Results (ppm) CO 0.162', NO 0.4007 NO2 U.4UY! tthVlene u.3t62 Hro0ane u.455r Hexane u.2z3i Acetaldehvde u.ut 52 Formaldehvde o.787f nce Calibration Transfer Standard ExDected Measured Path Lenoth Validated Ethylene 100 99.4 4.97 PaSSed , Hequ Annex Table 1.2.2 Measurement System Capabilities rarameler Measured Gas concentratron {nnm}Path Length EquilrDraron Time Dilution Factor % Recovery Path Lenqth ttnvlene 99.39 /4.970 Spike Direct Propane 249 481 :: SF6 9.677 CO 499.857 NO 248.603 Mechanical Response Time Ethylene 99,652 17 seconds Analyzer Response Propane 251.0ti9 41 secondsSF69.743 CO 494.614 NO 245.333 Analyte Spike Recovery Propane & SF6 /.utj"/o 1 10.10% 1.92"/o 92.88% 8.66%90.90% SVSTEM ZETO Nitroqen 1 7 seconds Post Spike System Hro0ane 250.999 ,: CO 494.651 NO 244.549 SF6 9.733 GAS Parameter Gas Goncentration Measured o/o Difference SDecilication Valldated Spike Direct Propane 251.000 249.481 0.61%+l'2o/o Hass SF6 9.730 9.O/O.54"/o +l- 2o/"PaSS CO 501 .400 4YY.65/0.31"/o +l- 2/"HASS NO 252.400 246.OU;J 1.50%+l-2/o PASS Spike Bun 1 via the Svstsm Source Output Spike Averaqe Dilution Factor Expected 70 Becovery specification Propane 26.208 48.629 44.166 1 'l O.1 OOo/o 7O-13Oo/o SF6 0.001 0.763 7.885/o :11Oo/o Spike Run 2 via the System source output spike Average Dilution Factor Expected 7o Recoverv Specilication Propane 14.591 JI 1t1 33.560 92.880%7O-130o/" SF6 o.ooo u. /bb 1.91b"/o <1O/" Spike Run 3 via the Svstem Source Output Spike Averaqe Dilution Factor Expected 70 Recovery specification Propane 14.744 32.244 35.472 90.900%7O-13O7o SF6 0.000 0.838 U.OOUTo (1U-/o Noise Equivalent Absorbance (NEA) RMS High 0.000969 RMS Mid 0.000934 RMS Low 0.000994 ng Line Position 0.20 0.15 0.10 0.05 0.20 0.15 0.10 0.05 0.00 ar--- -i.-:\ /,'0.00 r'- -='-/ '\,/ -0.0s 2092 2069 2046 2023 1999 1976 1953 1930 1907 't884 1861 1837 1814 Pass GAS -0 05 0.00o/o Pass The Gasmet GICCOR (Genzel lnterferometer with Cube Corner Retroreflectors) interferometer is specially designed for maximum optical throughput and maximum signal to noise ratio of 7.72 (cm-1) remaining stable with any vibration and temperature changes. setting and the detector linearity was tested with an alternate approach. A three point linerarity of the CTS gas was performed and validated. Linearity 157.8867 148.8867 139.8867 130.8867 121.8867 112.8867 103.8867 94.8867 85.8867 76.8867 695 687 679 5.02798793 The analytical accuracy of the quantification algorithm is satisfied via the results from Annex 5 per Annex 7.6 157.8867 148.8867 139.8867 130.8867 121.8867 112.8867 103.8867 94.8867 85.8867 76.8867672 664 656 648 641 633 625 618 610 602 POSTCTSSScm Chocl(: u tu tsonte uoncenlralron:100.oo u lu sample uoncentralron Averaqe:100.59 Difference between measured and expected:U-59"/o toterance:5.OO70 Eun Data Valldatl0n - Aut0ftat6d VA ManuAl B6adlnq Valldatod Commonts Hun 1 Potnts 1 & 20n U9/NU/ProDane All within 20olo Passed uemonstrates no tnlenerences ooserveo. Run 2 Points'l & 2 on L;O/NO/Prooane All within 20olo Passed uemonstrates no rnlenerences ooserveo. Hun 3 Points 1 & 2 on UO/NO/ProDane All within 20olo Passed Demonstrates no rnlenerences oDserveo. GAS 18 12.0 Signature Page Job/File Name: Utah Gas Corp;West Water CS; Unit C;JJJJ ffi&re We certify that based on review of test data, knowledge of those individuals directly responsible for conducting this test, we believe the submitted information to be accurate and complete. Company: G.A.S. lnc. Print Name: Travis Hartley Dale:212212024 Title: Director of Stack Testing Signature: PhoneNumber: 580-225-0403 Company: Print Name: Title: G.A.S. lnc. Carlos Gamboa Emissions Specialist Dale:212212024 Company: Utah Gas CorP print Name, Taryn Weiner Date: 4t10t2024 Signature: Ti,e: Manager, Air and Sustainability phone Number: 970-307-5032 GAS Appendices GAS Aitgas an Air Liquido cmpany Spike (5 Gas) Airgas Specialty Gas€s Airgas USA LLC 12722 S. Wentworth Ave. Chicago, IL 60628 Air8tr.sm CERTIFICATE OF ANALYSIS Grade of Product: BPA PROTOCOL STANDARI) Part Number: Cylinder Number: Laboratory: PGVP Number: Gas Code: E05Nt94E1 5AC014 cc142828 124 - Chicago (SAP) - lL 812022 CO,CO2,NO,NOX,PPN,BALN Reference Number Cylinder Volume: Cylinder Pressure: Valve Outlet: Certification Date: 54-402601324-1 147.0 CF 2015 PSIG 660 Dec 06,2022 Date:2030 Certifi€tion performed in accordance with "EPA Thceability Prctocol for Assy and Ceililietion of Gaseous Calibration Standards (May 2012)'document EPA 600/R-12/531, using the assay procodures listed. Analyti€l Methodology do6 not require corstion for analytical interferen@. This cylinder has a total analyti€l uncedainty as strated below wjth a confiden@ level of95o/o. There are no signifl@nt impurities which affecl the use ot this €libration mixture. All @nentrations are on a mle/mle basis unless otheMise notod- The results relate only to the items tested. The report shall not b6 roproduced ex@pt in full without approval of the laboratory. Do Triad Data Available Upon Request PERMANENT NOTES:Mixture contains nominal 1 oppm Sulfur Hexafluoride as a tracer component. Actual tested value included within the original Certificale of Analysis. Contact lhe Airgas laboratory if a reprint is required NOTES:Mixture contains nominal 10ppm Sulfur Hexafluoride as a tracer component. Actual tested value included within the original Certificate of Analysis. Contact the Airgas laboratory if a reprint is required. SFG Results: JMR'137-9.73rPPMr r I l ri Approved for Release Pag€ 1 ot I Componenl ANALYTICALRESULTS Requested Actual Protocol Total Relative Concentration Concentration Method Uncertainty Assay Dates NOX 250.0 PPM 253.0 PPM G1 +/- 1.2olo NIST Traceable 11D8D022,1U06D022 NITRICOXIDE 250.0PPM 252.4PPM G1 +/-1.0%NlsTTraceable 11D8D022,1200D022 PROPANE 250.0 PPM 251.0 PPM Gl +/- 0.7% NIST Traceable 11130D022 CARBON MONOXIDE 500.0 PPM 501.4 PPM G1 +/- 0.6% NIST Traeable 11129D022 CARBONDIOXIDE 5.000% 5.025o/o Gl +/-1.4%NlslTraeable 11D8D022 NITROGEN Balan@ CALIBRATION STANDARDSType Lot lD Cylinder No Concentration Uncertainty Expiration Date od29,2026 Feb 20, 2020 Feb 18. 2023 Mar 17.2027 Jul 03, 2024 May 14,2025 NTRM 200603-31 PRM 12386 EB0113125 250.3 PPM NITRIC OXIDE/NITROGEN D685025 9.91 PP[il NITROGEN DIOXIDE/AIR +l- O.8o/o +l- 2.Oo/o GMIS 401423838104 CC50s590 4.373 PPM NTTROGEN D|OX|DE/NITROGEN +l-2.0% 6,I6269ry 243.3 PPM PROPANE/AIR +l- 0.5'/o KA1003925 435.4 PPM CARBON I\TONOXIDE/NITROGEN +l- 0.60/o cc413685 7.489 0/o CARBON O|OX|DE/N|TROGEN NTRM 200602-13 NTRM 130't0'109 NTRM 13060423 +l- O 6o/6 The SRM, NTRM, PRM, or RGl, noted abde is onv in refeEn@ to the GMIS ussd in the assay and not part ofthe analysis ANALYTICAL EQUIPMENT lnstrumonUMake/Model Analytical Principle Last MultipointCalibration Nov 07.2022 Nov 28,2022 Oec 05,2022 Oec05,2022 Nov 07,2022 Ni@let iS50 AUP2010242 CGl SIEMENS ULTRAMAT 6E N1J57OO Nicolet iS50 AUP2010242 Ni@let iS50 AUP2010242 Ni@let iS50 AUP2110277 FTIR NDIR FTIR FTIR FTIR GAS Airgas m Atr Laquira c@pany 90/ o2tNo2 Airgas Specialty Grces Airgas USA LLC 525 North Industrial hop Road Tooele, t T 84074 Airg6-@D CERTIFICATE OF AIYALYSIS Grade of Product: EPA PROTOCOL STAMARD Part Number: Cylinder Number: Laboratory: PGVP Number: Gas Code: E03Nt90E1sW0003 cc41 9750 '124 - Tooele (SAP) - UT 872023 N02,02,BALN Reference Number: Cylinder Volume: Cylinder Pressure: Valve Outlet: Certification Date: 153-402732424-1 145.0 CF 2015 PSIG 660 May 08, 2023 Ex Date:2026 Certifi€tion perfom€d in a@rdance with 'EPA tor Assy and Cenification of Gaseous Calibration Sbndards (May 2012)" documenl EPA 600/R-12531, using the assay prccedures lisled. Anal,'ti€l d6 not require mn4iion tor analytiBl inte.feren@. This cylinder has a total analyli€l uncertainty as stated below with a confiden@ level of95%. Ther6 a6 rc signif€nt impurities which afiectthe uso ofihis calibr6tion mixluE. All @ncentrations are on a rcle/rcle basis unless olheMise noted. The results relate only to the itom tesbd. The report shall not be roproduced ex€pt in full without approval ofthe laboratory. Oo Triad Oata Availablo Upon Request Approved for Release Pago I of I Component ANALYTICAL REST'LTS Requested Actual Protocol Total Relative Concentration Concentration Method Uncertainty Assay Dates NITROGEN DlOxlDE 100.0 PPM 99.10 PPM G1 +/- 2.070 NIST TEeable 0510112023,05lO8Do23 OXYGEN 9.000 % 9.1'19 o/o G1 +/- 0.6% NIST Tra@able 05102D023 NITROGEN Balane CALIBRATION STANDARDS TvDe Lot lD Cvlinder No Concentration Uncertaintv Expiration Date GM|S 15340'1202'1601 PRM 12389 NTRM '14060629 ftc SRM mM PRM 6r RGM CC5O2O9O ,100.5 PPM NITROGEN DIOXIDE/NITROGEN 1.1YO D685050 99.0 PPM NITROGEN DIOXIDE/NITROGEN 1.Oo/o CC436987 4.794 % OXYGENNITROGEN 0.4o/o ue is onk in rafamnce to the GMIS used in lhe asav end not @rt otlhe analvsis. Oec 17,2024 Feb 19, 2020 od29,2025 lnstrumenUMakerModel ANALYTICALEQUIPMENT Analytical Principle Last Multipoint Calibration FTIR 02 Paramagnetic (DIXON) May 03, 2023 4pt06,2023 MKS FT|R NO2 018143349 Horiba MPA-s'10 U/603MM58 02 GAS Aitgas. s /& Ljquira cmpdry Ethylene Only Airgu Sprccialty Guec Airgm USA LLC 12722 S. WentmrthAYe. Chiego, IL 60628 AiBs.@m CERTIFICATE OF AIVALYSIS Grade of Product: PRIMARY STANDARD GREAT PLAINS ANALYTICAL SERVICE,Customer: Part Number: Cylinder Number: Laboratory: Analysis Date: Lot Number: x02Nl99Pl sACVH8 cc't 't7503 124 - Chicago (SAP) - lL Aug 15, 2023 54402811378-',1 Expiration Date: Aug 15,2031 Reference Number: 54402811378-1 Cylinder Volume: 144.0 CF Cyllnder Pressure: 2015 PSIG Valve Outlet: 350 Primary Standard Gas Mixtures are traceable to N.I.S.T, weights and/or N.I.S.T. Gas Mixture reference materials. Component ANALYTICAL RESULTS Req Conc Actual Concentration (Mote %) Analytical Uncertainty ETHYLENE NITROGEN 100.0 PPM Balance 100.0 PPM +l- 1o/o Note3:GREAT PLAINS ANALYTICAL, CERTIFIED BY FTIR Sldnrftrr.6n fila Approved for Release Page I of 1 GAS Airuas. 0 Arr t&uirc coparry BIP Airgrs MidSouth regi@ Airgs USA LLC 9741 E. S6th St. North Tulsa, OK 741y Ai196.@m CERTIFICATE OF BATCH ANALYSIS Grade of Product: BIP-BUfLT IN PURIFIER Part Number: Nl BlP300 Cylinder Analyzed: TW05-867349Laboratory: 106 - Tulsa Fast Fill (SAP) - OK Analysis Date: Feb 10, 2016LotNumber: 29400672389-1 ReferenceNumber: 29400672389-1 Cylinder Volume: 304.0 CF Cylinder Pressure: 2640 PSIG Valve Outlet: 580 Component ANALYTICAL RESULTS Requested Purity Certified Concentration NITROGEN OXYGEN WATER TOTAL HYDROCARBONS CARBON DIOXIDE CARBON MONOXIDE 99.999 % 1 PPM 1 PPM 0.1 PPM 0.5 PPM 0.5 PPM 99.999 % 0.94 PPM 0.058 PPM O.,I PPM 0.235 PPM 0.235 PPM Permanent Notes:This cert includes values from the Till' side and is not representative of the "use" side purity. Contact an Airgas Sales Representative for this information. Cylinde13 ln Batch: 4263617Y, T\ /04671107, T\ i0ffi31574, TW0S,865966, TVl/05467349, T\4Ofi67538, TW5-867578, Tr /05-881687, T\ 0$,881820, T\ 0S920689, T\ Ot920760, T\ O5848694, T\ O5867441, T\ /05897265, T\ O5897512, T\ /05920678, TW05920686, TW05920695, TW)5920781, T\ O5920874 lmpurities verified against analytical standards traceable to NIST by weight and/or analysis. Approved for Release Page I of I GAS Airgas e A[ Liquido cmpaiy 21o/o 02 Airgas Specialty Gases Airgas USA LLC 525 North Industrial hop Road Tooele, Ll'I 84074 Airgas.conr CERTIFICATE OF ANALYSIS Grade of Product: EPA PROTOCOL STANDARI) Part Number. Cylinder Number: Laboratory: PGVP Number: Gas Code: E02N179E1 5A0081 41M020982 124 - Tooele (SAP) - UT 872022 O2,BALN Reference Number: 153-402603461-1 Cylinder Volume: '146.0 CF Cylinder Pressure: 2015 PSIG Valve Outlet: 590 Certification Date: Nov 28.2022 Expiration Date: Nov 28.2030 Cedifi€tion perfomed in a@o.dance with 'EPA Traceability Prctoml for Assy and Cedification of Gaseous Calibration Standards (May 2012)' document EPA 600/R-12/531, using the assay procedures listed. AnalyU€l Methodology do€s not require coiiection for analytical inted6r6n@. This cylinder has a total analyli€l uncetuinty as stated belowwith a @nfiden@ levelof 95o/o. There are no signili€nt impurities which affectthe use of this €libration mixfure. All@n@ntEtions are on a mle/rcle basis unless otheMise noted. The resulls relate only to the items tested. The repod shall not be reproduced ex@pt in full without approval of the laboralory. Do Triad Data Available Upon Request Approved for Release Page I of I Not Use This Cylinder bel@ 100 psig. i.€ Componenl Requested Concsntration ANALYTICAL RESULTS Actual Protocol Goncentration Method Total Relative Uncertainty Assay Oat6s oxYGEN 21.00 % 21.02 vo NITROGEN Balane G1 +/- 1.0% NIST TEceable 11nal2o22 . CALIBRATIONSTANDARDS Type Lot lD Cylinder No Concentration Uncortainty Expiration Date NTR|\ll 09061434 CC2A2492 22.53 % OXYGEN/N|TROGEN 0.40/o May 13,2025 ANALYTICAL EQUIPMENT lnstrumenuMakerModel Analytical Principle Last Multipoint Calibration Horiba MPA-510 V!603MM58 02 02 Paramaonetic (Mason)Nov 17.2022 GAS AirUa$. Acetaldehyde & SF6 AirgB Slrecialty GueE Airgas USALLC 9810 MYAREABLVD Psadem,TxzsoT Airta.@m CERTIFICATE OF AI\IALYSIS Grade of Product: PRIMARY STAMARI) GREAT PLAINS ANALYTICAL SERVICE,Customer: Parl Number: Cylinder Number: Laboratory: Analysis Date: Lot Number: x03Nl99P1sACD42 cc334560 124 - Pasadena (SG06) - TX Sep 29, 2023 1634028/.7',t28-',1 Expiration Date: Sop 29, 2024 ReferenceNumber: 163402847128-1 Cylinder Volume: 140.0 CF Cylinder Pressure: 2015 PSIG Valve Outet: 350SS Primary Standard Gas Mixtures are traceable to N.I.S.T. weights and/or N.I.S.T. Gas Mixture reference materials. Component Req Conc AI\iALYTICAL REST'LTS Actual Concentration (Mole %l Analytical Uncertainty SULFUR HEXAFLUORIDE ACETALDEHYDE NITROGEN 10.00 PPM 100.0 PPM Balance 10.00 PPM 99.62 PPM +l-'lo/o +l- 1o/o Approved for Release P.ge I of I GAS y.rto:;tr*iflu LY; UNITED STATES ENVIRONMENTAL PROTECTION AGENCY BESEARCH TRIANGLE PARK, NC 27711 March 15,2021 {J[ I t{-l ,,r Air fitrAt IIY Irt Ai,ilftllir-r Alrt, sl,tt{t.tAl{t'1 Mr. Jordan Williamson CEO GAS Inc. 303 W. 3ra Street Elk City, OK73644 Dear Mr. Williamson: We are writing in response to your letter received on September 17, 2020, in which you request the approval of alternative testing procedures. The EPA's Office of Air Quality Planning and Standards (OAQPS) is the delegated authority for consideration of major alternatives to test methods and procedures as set forth in 40 CFR parts 60 and 63 under which your request must be addressed. GAS Inc. is requesting a change to one of the test methods, ASTM D6348-03, used for conducting performance tests to determine compliance under 40 CFR part 60, Subpart JJJJ - Standards of Performance for Stationary Spark Ignition Internal Combustion Engines (Subpart JJJJ) and 40 CFR part 63, Subpart ZZZZ - National Emissions Standards for Hazardous Air Pollutants for Performance for Stationary Reciprocating Internal Combustion Engines (Subpart ZZZZ). The change being requested will be used to check detector linearity of the Fourier Transform Infrared (FTIR) instrumentation used to conduct this method. Specifically, you are requesting that the procedures of section 8.3.3 of Method 320 (40 CFR part 60, Appendix A), another FTIR-based method allowed under Subparts JJJJ and ZZZZ, be used in lieu of section A6.4.1of ASTM D6348-03 when conducting testing using ASTM D6348-03 under 40 CFR part 60, Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. In your request, you state that this alternative linearity check procedure will produce consistent results when utilizing either Method 320 or ASTM D6348-03. Additionally, some FTIR instrumentation does not allow for reducing the size of the aperture in the instrument and, thus, it would not be feasible to properly conduct the entirety of the ASTM D6348-03 method in its current form using such an instrument. Based on our understanding of FTIR instrument principles and recognition that the requested alternative determination of detector linearity is both technically sound and contained within Method 320, we are approving the requested change. We believe that this alternative is acceptable for use for use in testing all engines subject to 40 CFR part 60 Subpart JJJJ and 40 CFR part 63, Subpart ZZZZ. Also, we will post this letter as ALT-l4l on EPA's website (atwww.epa.gov/emc/broadly-applicable-approved-alternative- testmethods) to announce that our approval of this alternative test method is broadly applicable to engines for the purposes of meeting Subparts JJJJ and ZZZZ. If you should have any questions or require further information regarding this approval, please contact David Nash of my staffat 919-541-9425 or email at nash.dqe@pa.gov. Sincerely, cc: STEFFAN I#H,ffiH,JoHNsgr{ffi' Steffan M. Johnson, Group Leader Measurement Technology Group Sara Ayem, EPA/OECA/OCA{AMPD, (ayres.sara@epa.gov) Melanie King, EPA/OAR/OAQPS/SPPD, (king.melanie@epa.gov) James Leather, EPA Region 6, (leatherjames@epa.gov) David Nash, EPA/OAR/OAQPS/AQAD, (nash.dave@epa.gov) Carlos Gamboa GAS 580-225-0403 info@gasinc.us Type of Sources Tested: Stationary lnternal Combustion Engines. 4 Stroke Rich Burn Engines. 2 Stroke & 4 Stroke Lean Burn Engines Stationary Natural Gas Fired Generators Stationary Propane Fired Generators Gas Fired Boilers Types of Analyzers:. Gasmet DX4000 FTIR. Gasmet Portable Sampling Unit with Zirconium Oxide 02 Sensory. Testo 350. Flame lonization Detector Qualifications: Trained, studied, and fully demonstrates compliance for emissions testing via data collection outlined in the following Reference Methods:. EPA Method 1 & 1A - Sampling & Traverse Points. EPA Method 2 &2C - Velocity & Volumetric Flow Rate of a Gas Stream. EPA Method 3A - Oxygen. EPA Method 7E - NOX. EPA Method 10 - Carbon Monoxide. EPA Method 25A- Volatile Organic Compounds. ASTM D6348 - Extractive Fourier Transform lnfrared Spectroscopy Conducts emissions testing on a weekly basis including, but not limited to, the following test types: lnitial Compliance, Biennial Compliance, Semiannual Compliance & Quarterly Complianc,e. {lltgqts performed are in accordance to any and all Federal & State requirements as applicable (i.e. JJJJ,72ZZ, 106.512, 117, PEA, etc.). Performed t-esting in Colorado, Utah, Wyoming, North Dakota, Montana, Kansas, New Mexico, Oklahomi, Texas, Louisianalland and off-shore), Arkansas, Ohio, Pennsylvania, West Virginia, New York, Kentucky, & Mississippi. . Quarterly Performance Reviews covering ongoing changes with Federal Regulations, State Compliance guidelines, & site-specific safety certifications. GAS qq q oo o @o @ oo o NN N qc c oo o cq q ON N (o ( o @ @@ @ oo o ooao q \ Nroo o NN N oo o @t s t s ': q o ? NO @ NN N ON r o( o o qq q oo r o @o @ @o r F ac ! - NN N ao oo o oo o oo o oo o o, r o o oq c ? a? o, o o, NN N oooo r i @o ri + + Or e rO C i oo t oo o @o o +N @ cq q oo o @N @ ro Nqn a oN o o* o q' : c oo o o( ( ) 0 N$ O OrNA i s i O\ t O u? ( ? q N( r @ rN O qq o l (r $ * oo o oo o qc c oo o Or \ t @N N r@ O io i d i NN N oN r ) ts N N u? \ o { o@o) o o $$ o F$ o @o { NN N $+ + r( o \ t oo o oo o oo o oo o 99 9 NN N oo o NN N oo o NN N NN N NN N NN N oo.=oo j'aa oo o qc q oo o cq q oo o @o @ 6* s i oo i o , cq q N@ @ @( o @ @@ @ @n N qu ? a N@ O oo r o , oo o oo o oo o oc i o oo o oo o qq c oo o oo o oo o gc q oo o F@ O oN o u? q q oroN 6 r) \ t \ i qq c NO O ) oo o oo N oo N oo o do o oo o oo o cq q oo o oo o oo o cq q oo o N ox o q6 a 9o q o( r + c9 9 NN N oo o NN N oo o NN N NN N NN N NN N oo o oo d qq q oo o o@ o oN o Or @ o- c i Nr O $N O Or O do o oo N $oqc q oo o oo o oo o qc q oo o @o o o@ @ go ? o ? rC , O oo o oo o cq q oo o $s o o! A l 01 oo o oo-=oC\ Iop$loz qq q oo o @o o Or O qq q NN N cq q @o o @@ @ @o @ $@ o a2 o? 01 rO O oo o qq c oo o -O o C] N N cq c oo o Or N @r qq a ? oo o oo o cq c ot o o @$ o qq - oo o oN o @o o ': ' : q oo o NN @ FO @ ce q oo o oo o oo o qg c oo o Ni o $on' . 9 oo o Or @ ON N a? a * q o o@ o go o qq q oo o oo o oo o qq q oo o oo o oo o qq q oo o oo o oo o qq q oo o oo o oo o oo o do o $o o o$ o qq q oo o oo o oo o cq q oo o 60 N oo o oo o oo o @@ ( o 5? { 2 Y? @@ @ oo o NN N oo o NN N NN N NN N NN N C)o.=o$to.C.9I rO O rC , O eq c oo o o@NO O Nr oo o o{ o oo o qq q oo o oo o oo o qq c oo o r) o @ $N N c? q e ? oo ) d , oo o oo o oo o cc c oo o oo o oo o ec q oo o oo o oo o oo o do o qq q oo o o@ o (o $ oo o oo o qq q $* N NN N @@ @ o@ N o? q? ol @@ @ @@ @ FO ( o OFci o o $N O oo o qc q oo o oo o oo o qq q oo o or o o Nr O oo o ci o o oo o oo o oo o ci c i o @o o oo o oo o ci d o OF o oo @ q. . ' : oo o oo o oo o oo o oc i O $o o C, T cq q oo o NO O qq q oo o oo o {? Y? s? @@ @ oo o NN N oo o NN N NN N NN N NN N ()oLi5ct )o cc e oo o @o o oo o qq c oo o cq q oo o NN N o@ o OF \ i q\ \ oo o oo o cc c oo o oo o oo o 9C C oo o ON N o( o ol C a c, r oo o oo o qq c oo o oo o oo o cq q oo o oo o oo o qq q oo o Or O Or O q' : q oo o oo o oo o qc q oo o oo o oo o oo o . oc t c i rN O (o o s qq ? q co o -@a( ? \ oo 6 oo o oo o qc q oo o oo o oo o qq e oo o oo o oo o cq q oo o oo o oo o oo o ci o o oo o oo o qq < 2 oo o oo o oo o oo o do o oo $ oo o qg c oo o NO $ NN N (b 6 6 oo o NN N oo o NN N NN N NN N NN N ()Ei5o.EoU) (u tr l yooFoo- Nol o,NoONci qo@o, o?NcoN@(ou?Nooqo6qNooqooqoooqO\NNI;ooqoNNq?oIciNN@q?No,@oloo,Naoo6o\tNoNNNN aoqoooqo\too?N :=5oa _o6E ^ o. o v FcS= ' xvoEr ? h €g € fo 5 ol OE>o oe x>oc zd o .l LEU' A o OE $> IENO () o+e IE6E fEOEo&@= NEo&*! -E-o o _e (J F IA o oE NEo& -lOEO- n e .i -tz- d qol NF Z- d o *e IEoa o -EOF Z- d oI o:oI PE vo e (E {J(go==ooE=E Naos ovRS Iv U)w oEFo6o oocnoo3oooLoo=s=r -o '6Looo lr J -l(o lo (f )o o)oNooFo-= oJ(E= ::otto= ottEzEoU' oLoC)c,oo-cof aoo) (E=o0,= ocD troo tro(Eoo o.c t IzE= qc q q c q q q oo o o o o o o @o @ @ @ @ @ o $O F O N S o O r+ v o { N @ o NN i N N N ( @ cq c q q q q q N( O ( o @ @ @ @ @ 6n o o o o o ( ) @@ @ @ @ o o o ^o o $ s N o N :q a ( ? ' : a ' : a ? :6 0 0 0 @ o N rN r N oo @ @ N N o - -c ! o ? o q q q - x NN O N O N O . ; @r N O r O O i A TN N N N T oo o o < f o o o oo o o o o o o qq q c q q c q oo o o o o o o So O O @ O @ r ON O - O O N * qq q q o q o q u ? q Fo o o N o N o o@ o o N N @N N t s r * @ O qo ? o ? o g \ 9 9 4 ? C, r r \ t r t Nr o o * : @ = NO O $ O : l N H os N o o - @o , o ; o t o t Y o P @@ N O O @ O O NN O N N T N ( , \q s ? a \ q q o ? *N N O $ O O ( O OO O O O T $ N EE E E E E E E g oo d c i c i c i o o * \ o oo o o o o o o oo o o o o o o oo o o o o o o od c i d o o o o OO O r * o ) @ Y oN F O O O N ! ? qq u ? - o q \ s s ? 6o @ N N o ; P rN N O O @ N o @o o o o o r o , @O O O O T O O @o o O O r O O ro o o o r c , r oo o o o o c i c i o@ o N 6 @ ON O @ O N F O FO S @ S 0 $ O cr o o o o d d d N$ @ O S @ l: O O r @ N N O 50 ? q g q q 9 n di N N O O @ N O NO O O O O O O oo o o o o o o c. t q q c q q q q oo o o o o o o oo $ @ $ @ o - oN s ( O ( o O r l ; qq \ - u ? o q q F 5 N$ 6 N N @ n N n( o @ ( o @ N s oo v o @ o @ - NF o O o O o q T s$ @ N o @ $ m +c i + d t s c i dr n j L i ) < e 6 o E oo o o o N $ @ oo @ o o o o o qq q ' : o l o? q \ oO r o o o @O N @ O N e T ro - o O O O $ qq q o l q o ? o l \ $6 @ O @ O O 6 -t o N o @ o N =N O S + 6 6 6 :; a a ? c ? a ? - - o ? @= = = : : = 9 Or N O $ O @ t s ci d " , c i c i a i ci c i ci ss s s s s s s NN N N N N N N oo o o o o o o NN N N N N N N NN N N N N N N NN N N N N N N NN N N N N N N .cEo(oof.sEc) (f ) I l-ft qq q Or O OO O oo o cq q oo o qq q oo o or ) r ) oo o NO O q? q - oN o n' : s l oo o (o $ o oo o oo o oo o @N O $o o ': - C FC , (0 @ o qq q ON NS O qq q oo o oo o $o @ cg g oo o oo t + oc , r qc q oo o oo o oo o oo o ci o o $r @ s@ N qq q oo o oo o oo @ cq o l oo o N@ O o( , r ct c t c i @@ o Nr ) N qq q oo o@o o NO C ) ': q s l oo o oo o oo o cq q oo o ON N Or r @ 1- o i oo o r) ( ) ( 9 NO @ ol o ! ': oo o oo o oo o qq q oo o o( o N oo o cq q oo o oo o NN N NN N oo o !+ $ s i NN N oo o NN N NN N NN N NN N oEFooCoo.o'oE.C'=EoU'ao.goo(Ud] qq q oo o oo o qq c @N N () a ( ) oo o *o , o? ( ? \ oo o 60 n NN N @6 @ 6? q a ? {* @NN N r) o ( o (, ( o N \\ \ oo o ONo( o o aq q NN N oo o oo o qq q oo o NO ( , F( ) o oq a q Or O oo o NN N oo $ @a u ) ': q \ 00 @ $o o *o r ) qq q oo o o@ o oo o qq q oo o 6( O ( o oN o c? ' : a oo @ o6 0 ': q q oo o QN N@o r o aa a NN NN N qq a oo o@o N so s @o 6 +d c i @o D o( o au ? u ? oo o oo o qq q oo o o6 r ) o6 @ qq a ? $$ @ *\ i \ i NN N NO @ o) @ ( o N@ @ ri c i + oo o $$ $ N@ O @o o \\ o q NO O oo c ) qq q oo o o$ * $t $ r $l NN N oo o $$ s f NN N oo o NN N NN N NN N NN N oEtroooo-oo(f l-E=EooaolzCL U) qc q oo o @o @ NN N qq ' : oo o qq q o) @ @ 60 0 @6 0 oN 6 Al ': ol oo o ot s @ qu ? q oo o oo o oo o qq q oo o NO O oo @ gq q oo o oN ( o N( O O cq ' : oo o oo o oo o q9 q oo o oo o oo o oo o oo c i rN { oo o qq q oo o oo o oo o oo o ci d o oo o oo o qq c oo o oo o oo o oN o od c i oo N oo o q' : a l oo o NO N @o N NN N oo o ro O C, F $ \o ) o q oo o or o ) N oN o qa q or @ o oo o N* O os @ q' : q NO N {$ o rO @ qq ' : oo o oo o oo o oo o oo o QN !2 0 0 90 0 of o o oo NN N NN N oo o NN N oo o NN N NN N NN N oEtro(tcoo. al ,oE, .C.==EoU'aNoE=GIoz cq c oo o @o @ o. t o oo o qq e 6V ( f ] @( o @ @@ @ NN O $+ o o( o N @@ @ oo o qq c oo o oo o -O O cq q oo o @@ o ON N N ci c i o oN $ FN @qq q oo o oo o oo o qq c oo o oo o *N O q? g q oo o ON N C, r O qe q oo o oo o oo o qq q oo o 6n 9 2 o@ : l do i P oo : o@ o oo o q' : q oF O oo N N( O O q' : - oo o OO O C, r O oo o oc r c , oo o oo o cq c oo o oo o oo o qq q oo o oo o oo o oo o oc i o oo o oo o qq q oo o oo N -O o 9q q oo o oo N gq q oo o @@ @ NN N oo o NN N oo o NN N NN N NN N NN N oEtroocoo(t ,otr !'=EoaU)ao cc q o' o o @@ @ oo o qq < 2 oo o qq q @@ ( o @@ @ N@ N s? r o l oo o ro @ o? 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IE@: () E qc eq q q q q q q q qq q c q q q cq q q E , @ @ @ @ @ @ @ @ @ @ @ o @ o @ @ @ @ @ @ @ o , ; o o 6 0 0 0 0 0 @ o o o o o 0 0 0 0 0 0 0 0 i x @@ @ @ @ @ @ @ @ @ @ @o @ @ @ @ @ @ @ @ @ 6 a oq \ Al ' : cl \ a c? q \ c\ l q q q a ? q o l s ? c ? , . \ \ ii j N O NN @N @@ O O O O O N N ON O S F - $; N N NN N O O O $ $ O O ( ) O S O @ @ O O S @A : $O N N O T @ @ @ N N N O O T $ $ - N O 0 O lq q ot q a q \ \ q q? c? \ c2 ' : a ? n \ n \ q c2 q & oN $ @N N O@ N N O O @ O $ @ O O O @ O @; s $ $ v $ N N N N O O O N O O $ N O O $ O $ i { . OO O O O N N T O O N O N - O O N o $ O $ F OO O O OO O OO O O OO O O O O O O O O O O qq q q q q q q q q q q q q gq q c q q q q q oo o o o o o o o o o oo o o o o o o o o o o Oo @ @ s @ 0 @ o O N @ @ O O N @ O r @ N O NO O @ O @ r NO @ @ Oo @ O @ n N@ O O o + a q o ? a c? q q q q q q q c ? - : q q a q q q q o2 9 oo o o o o $ $ oo v v $ s o N o $ $ N N o o O$ O O @ @ O r ON N OO O O @ N r N OO NO N- O@ N N O N @O N O r 0 N OO r @ S @ rO c\ l q c! c! 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Igoa o 8E Z- d qi o> zt r d o ^?UEg NN O O ) 6 N NN N O 6 b \ \ \ \ r\ 66 6 6 a r i @r @ N o@ $ r + o o OO o O @ r P e e e 33 @O O r . * q a r r P 5 ' NN N N E < -6 c $$ $ * f NN N N T oo o o NN N N NN N N NN N N NN N N N^os ovOaNX oEFooo cq q oo o oo o oo o qc c oo o cc q @o ( o r) 0 r ) @o @ oo @ q? u 2 a oo o oo 0 qq c l oo o oo N oo o qc c oo o oo @ 60 N qi o l oo o o( o oN o qq q oo o .E s6 o ai o E^ ' EogOE ,E*eOE zd gc@> tL t r o- d go€ s> -ENO () o+E ICEE U)o o@ $ NO N -' : o l oo o o@ o c? c ' i e NN oo o oo o oo o oo o qq c oo o oo N {o oeq ' : oo o oo o @o 0 gq ' : oo o oo o oo o Al qq oo o NO O Or O oo d -FOEo& o! NEo3 i u2 TE o ,?OE -a o !' =NEo&*lOF@- d a -l T. t r z- d qol NE Z- d o oo o oo o ': q q oo o rO O OO @ aq q oo o @o @ -O O ol qa oo o o@ o NO N \\ qoo o ol -9oa a .ioi : z6 - oe o2 o RE vo g _o3E 0 c9c ' o ON N rOqq c oo o @( o s t oo o cq c oo o (o ( o @ $! $ t n NN N $+ $ NN N oo o NN N NN N NN N N. - N Naos C) v OaNX Iv (,Ei= 511124, 12:00 PM State of Utah Mail - Compliance Advisory Response Letters - Westwater Compressor Station & San Anoyo Plant Kyle Greenberg <kgreenberg@utah.gov> Comptiance Advisory Response Lefters - Westwater Gompressor Station & San Arroyo Plant Taryn Weiner <tweiner@utahgascorp.com>Wed, May 1,2024 at8:44AM To: Kyle Greenberg <kgreenberg@utah.gov> Cc: Ken Secrest <ksecrest@utahgascorp.com>, April Mestas <amestas@utahgascorp.com>, Ronald Plummer <rplummer@utahgascorp.com>, Chris Forster <chris.forster@utahgascorp.com>, Rik Ombach <rombach@utah.gov> Good morning Kyle, We have confirmed that all units have the same stack diameter of 14 inches, Unit C has a clerical errors. Let me know if you would like me to have the reports modified to reflect the correct stack diameter and to include the lb/hr. Thank! [Quoted text hidden] https://mail.google.com/mail/u/O/?ik=83bbfeb418&view=pt&search=all&permmsgid=msg-t 1797861885074783516&simpl=msg-t1797861885074783516 1l'l