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Home My WebLink AboutDAQ-2024-0104531 DAQC-968-24 Site ID 10414 (B4) MEMORANDUM TO: STACK TEST FILE – CENTRAL VALLEY WATER RECLAMATION THROUGH: Harold Burge, Major Source Compliance Section Manager FROM: Paul Morris, Environmental Scientist DATE: September 25, 2024 SUBJECT: Source: Jenbacher Engine 1 and 3 Contact: Brian Mansell: (801) 973-9100 Location: 800 West Central Valley Road, Salt Lake City, UT Test Contractor: Alliance Technical Group, LLC FRS ID#: UT0000004903500191 Permit#: 3500191001, dated March 16, 2020, Last Revised September 9, 2021 Action Code: TR Subject: Review of Stack Test Report Received September 23, 2024 On September 23, 2024 (Email), DAQ received a test report for Central Valley Water Reclamation facility’s Jenbacher Engine 1 and 3. Testing was performed on September 4-6, 2024, to determine compliance with permit condition II.B.2.c. The DAQ-calculated test results are: Source Test Date Test Method Pollutant Result Limit Jenbacher 1 9/4-5/2024 RM 320 NOx 0.52 g/hp-hr 0.55 g/hp-hr CO 2.19 g/hp-hr 2.50 g/hp-hr VOC 0.1 g/hp-hr 1.0 g/hp-hr NMHC 0.3 g/hp-hr 0.3 g/hp-hr Jenbacher 3 9/5-6/2024 RM 320 NOx 0.46 g/hp-hr 0.55 g/hp-hr CO 2.19 g/hp-hr 2.50 g/hp-hr VOC 0.1 g/hp-hr 1.0 g/hp-hr NMHC 0.2 g/hp-hr 0.3 g/hp-hr DEVIATIONS: None reported. CONCLUSION: The test report appears to be acceptable. 6 , 3 2 RECOMMENDATION: Central Valley Water Reclamation facility’s Jenbacher Engine 1 and 3 should be considered to have been in compliance with the applicable limits at the time of the test. HPV: No ATTACHMENTS: Test report dated September 23, 2024, and DAQ Spreadsheets TEST REPORT SUMMARY CORPORATE OFFICE 255 Grant St. SE, Suite 600 Decatur, AL 35601 256.351.0121 www.alliancetechnicalgroup.com Client Information / Test Location Source Information Central Valley Water Reclamation Facility Engine/Unit ID: Jenbacher #1 Wastewater Treatment Plant 800 W Central Valley Road Salt Lake City, UT 84119-3379 Engine Manufacturer GE Jenbacher Engine Make/Model: JMS 612-F28F02 Engine Serial Number: 1322399 Engine Type: Spark Ignition 4SLB Engine Date of Manufacture: 1/1/2017 Engine Rating: 2,509 HP Regulatory Applicability Project No. 40 CFR 60, Subpart JJJJ AST-2024-3767 DAQE-AN104140015-21 Run No. Run 1 Run 2 Run 3 Average Date 9/4/24 9/5/24 9/5/24 -- Engine Load, % * 94 94 94 94 Nitrogen Oxides Data Emission Factor, g/bHP-hr 0.52 0.52 0.52 0.52 Emission Limit, g/bHP-hr -- -- -- 0.55 Percent of Limit, % -- -- -- 95 Carbon Monoxide Data Emission Factor, g/bHP-hr 2.4 2.4 2.4 2.4 Emission Limit, g/bHP-hr -- -- -- 2.5 Percent of Limit, % -- -- -- 97 Volatile Organic Compounds Data ** Emission Factor, g/bHP-hr 0.12 0.11 0.11 0.11 Emission Limit, g/bHP-hr -- -- -- 1.0 Percent of Limit, % -- -- -- 11 Non-Methane Hydrocarbons Data Emission Factor, g/bHP-hr 0.28 0.27 0.26 0.27 Emission Limit, g/bHP-hr -- -- -- 0.3 Percent of Limit, % -- -- -- 90 Methane Data Emission Factor, g/bHP-hr 5.7 5.7 5.7 5.7 Ethane Data Emission Factor, g/bHP-hr 0.11 0.11 0.11 0.11 Formaldehyde Data Emission Factor, g/bHP-hr 0.35 0.35 0.35 0.35 *Performance testing was conducted while the engine was operating at the highest achievable load at current site conditions. **VOC excludes Formaldehyde, methane, and ethane. NMHC value adds ethane back to VOC. TEST REPORT SUMMARY CORPORATE OFFICE 255 Grant St. SE, Suite 600 Decatur, AL 35601 256.351.0121 www.alliancetechnicalgroup.com Client Information / Test Location Source Information Central Valley Water Reclamation Facility Engine/Unit ID: Jenbacher #3 Wastewater Treatment Plant 800 W Central Valley Road Salt Lake City, UT 84119-3379 Engine Manufacturer GE Jenbacher Engine Make/Model: JMS 612-F28F02 Engine Serial Number: 1322432 Engine Type: Spark Ignition 4SLB Engine Date of Manufacture: 1/1/2018 Engine Rating: 2,509 HP Regulatory Applicability Project No. 40 CFR 60, Subpart JJJJ AST-2024-3767 DAQE-AN104140015-21 Run No. Run 1 Run 2 Run 3 Average Date 9/5/24 9/6/24 9/6/24 -- Engine Load, % * 94 94 94 94 Nitrogen Oxides Data Emission Factor, g/bHP-hr 0.47 0.44 0.46 0.46 Emission Limit, g/bHP-hr -- -- -- 0.55 Percent of Limit, % -- -- -- 83 Carbon Monoxide Data Emission Factor, g/bHP-hr 2.4 2.4 2.5 2.4 Emission Limit, g/bHP-hr -- -- -- 2.5 Percent of Limit, % -- -- -- 97 Volatile Organic Compounds Data ** Emission Factor, g/bHP-hr 0.11 0.10 0.10 0.11 Emission Limit, g/bHP-hr -- -- -- 1.0 Percent of Limit, % -- -- -- 11 Non-Methane Hydrocarbons Data Emission Factor, g/bHP-hr 0.29 0.21 0.21 0.24 Emission Limit, g/bHP-hr -- -- -- 0.3 Percent of Limit, % -- -- -- 79 Methane Data Emission Factor, g/bHP-hr 5.4 5.8 6.0 5.7 Ethane Data Emission Factor, g/bHP-hr 0.12 0.069 0.073 0.088 Formaldehyde Data Emission Factor, g/bHP-hr 0.28 0.30 0.31 0.30 * Performance testing was conducted while the engine was operating at the highest achievable load at current site conditions. **VOC excludes Formaldehyde, methane, and ethane. NMHC value adds ethane back to VOC. Source Test Report Central Valley Water Reclamation Facility 800 W Central Valley Road Salt Lake City, UT 84119-3379 Sources Tested: Jenbacher #1 & #3 Test Dates: September 4 – 6, 2024 Project No. AST-2024-3767 Prepared By Alliance Technical Group, LLC 3683 W 2270 S, Suite E West Valley City, UT 84120 . Source Test Report Source & Contact Information AST-2024-3767 Central Valley – Salt Lake City, UT Page i Regulatory Information Permit No. DAQE-AN104140015-21 Regulatory Citation 40 CFR 60, Subpart JJJJ Source Information Source Name Source ID Target Parameters GE Jenbacher Model JMS 612- F28F02 Generator Engine Jenbacher #1 NOx, CO, VOC, NMHC GE Jenbacher Model JMS 612- F28F02 Generator Engine Jenbacher #3 Contact Information Test Location Test Company Central Valley Water Reclamation Facility Wastewater Treatment Plant 800 W Central Valley Road Salt Lake City, UT 84119-3379 Facility Contact Bryan Mansell mansellb@cvwrf.org (801) 973-9100 Alliance Technical Group, LLC 3683 W 2270 S, Suite E West Valley City, UT 84120 Project Manager Charles Horton charles.horton@alliancetg.com (352) 663-7568 Field Team Leader Alan Jensen alan.jensen@alliancetg.com (847) 220-3949 QA/QC Manager Kathleen Shonk katie.shonk@alliancetg.com (812) 452-4785 Report Coordinator Delaine Spangler delaine.spangler@alliancetg.com Report Reviewer Sarah Perry sarah.perry@alliancetg.com 2 of 99 Source Test Report Certification Statement AST-2024-3767 Central Valley – Salt Lake City, UT Page ii Alliance Technical Group, LLC (Alliance) has completed the source testing as described in this report. Results apply only to the source(s) tested and operating condition(s) for the specific test date(s) and time(s) identified within this report. All results are intended to be considered in their entirety, and Alliance is not responsible for use of less than the complete test report without written consent. This report shall not be reproduced in full or in part without written approval from the customer. To the best of my knowledge and abilities, all information, facts and test data are correct. Data presented in this report has been checked for completeness and is accurate, error-free and legible. Onsite testing was conducted in accordance with approved internal Standard Operating Procedures. Any deviations or test program notes are detailed in the relevant sections on the test report. This report is only considered valid once an authorized representative of Alliance has signed in the space provided below; any other version is considered draft. This document was prepared in portable document format (.pdf) and contains pages as identified in the bottom footer of this document. Charles Horton, QSTI Alliance Technical Group, LLC Date 3 of 99 9/23/2024 Source Test Report Table of Contents AST-2024-3767 Central Valley – Salt Lake City, UT Page iii TABLE OF CONTENTS 1.0 Introduction ................................................................................................................................................. 1-1 1.1 Facility and Process Description ................................................................................................................. 1-1 1.2 Project Team ............................................................................................................................................... 1-1 1.3 Instrument Information................................................................................................................................ 1-1 1.4 Site Specific Test Plan/Test Protocol & Notification .................................................................................. 1-1 2.0 Testing Methodology .................................................................................................................................. 2-1 2.1 U.S. EPA Reference Test Methods 1 and 2 – Sampling/Traverse Points and Volumetric Flow Rate ........ 2-1 2.2 U.S. EPA Reference Test Method 3A – Oxygen/Carbon Dioxide .............................................................. 2-1 2.3 U.S. EPA Reference Test Method 320 – H2O, NOx, CO, VOC, NMHC, CH4 and H2CO ......................... 2-1 2.4 U.S. EPA Reference Test Method 205 – Gas Dilution System Certification .............................................. 2-2 2.5 Quality Assurance/Quality Control – U.S. EPA Reference Test Method 3A.............................................. 2-2 2.6 Quality Assurance/Quality Control – U.S. EPA Reference Method 320 .................................................... 2-3 LIST OF TABLES Table 1-1: Project Team ........................................................................................................................................... 1-1 Table 1-2: Instrument Information ............................................................................. Error! Bookmark not defined. Table 2-1: Source Testing Methodology .................................................................................................................. 2-1 APPENDICES Appendix A Sample Calculations Appendix B Field Data Appendix C Quality Assurance/Quality Control Data Appendix D Engine Operating Data Appendix E Site Specific Test Plan 4 of 99 Introduction 5 of 99 Source Test Report Introduction AST-2024-3767 Central Valley – Salt Lake City, UT Page 1-1 1.0 Introduction Alliance Technical Group, LLC (Alliance) was retained by Central Valley Wastewater Reclamation Facility (Central Valley) to conduct compliance testing at the Wastewater Treatment Plant in Salt Lake City, Utah. Portions of the facility are subject to provisions of the 40 CFR 60, Subpart JJJJ and the Utah Department of Environmental Quality, Division of Air Quality (UDAQ) Approval Order (AO) DAQE-AN104140015-21. Testing was conducted to determine the emission rates of nitrogen oxides (NOx), carbon monoxide (CO), volatile organic compounds (VOC) minus formaldehyde, and non-methane hydrocarbons (NMHC) from the exhausts of two (2) GE Jenbacher Model JSM 612-F28F02 engines designated as Jenbacher #1 and Jenbacher #3. 1.1 Facility and Process Description Central Valley operates two (2) GE Jenbacher Model JMS 612-F28F02 generator engines. Each engine is rated at 2,509 horsepower (hp) each. The engines can be fired on natural gas or digester gas. Jenbacher #1 and #3 are the subject of this test program and will be fired on a mixed gas of blended digester gas and natural gas. 1.2 Project Team Personnel involved in this project are identified in the following table. Table 1-1: Project Team Central Valley Personnel Zack VanWormer Alliance Personnel Alan Jensen Jesse Hall Supilani Mailei 1.3 Instrument Information The instruments used to conduct the compliance testing are summarized in the following table. Table 1-2: Instrument Information Pollutant Manufacturer Model Serial Number O2 Servomex 1400 14200/3279 CO2 Servomex 1400 1415C-2 H2O / CO2 / NOx / CO / VOC / NMHC / CH4 / H2CO MKS -- -- 1.4 Site Specific Test Plan/Test Protocol & Notification Testing was conducted in accordance with the Site Specific Test Plan (SSTP) submitted to UDAQ by Central Valley. 6 of 99 Testing Methodology 7 of 99 Source Test Report Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-1 2.0 Testing Methodology The emissions testing program was conducted in accordance with the U.S. EPA Reference Test Methods listed in Table 2-1. Method descriptions are provided below while quality assurance/quality control data is provided in Appendix C. Table 2-1: Source Testing Methodology Parameter U.S. EPA Reference Test Methods Notes/Remarks Volumetric Flow Rate 1 & 2 Full Velocity Traverses Oxygen / Carbon Dioxide 3A Instrumental Analysis Moisture Content / Nitrogen Oxides / Carbon Monoxide / Volatile Organic Compounds / Non-Methane Hydrocarbons / Methane / Ethane / Formaldehyde 320 FTIR – Continuous Sampling Gas Dilution System Certification 205 --- 2.1 U.S. EPA Reference Test Methods 1 and 2 – Sampling/Traverse Points and Volumetric Flow Rate The sampling location and number of traverse (sampling) points were selected in accordance with U.S. EPA Reference Test Method 1. To determine the minimum number of traverse points, the upstream and downstream distances were equated into equivalent diameters and compared to Figure 1-2 in U.S. EPA Reference Test Method 1. Full velocity traverses were conducted in accordance with U.S. EPA Reference Test Method 2 to determine the average stack gas velocity pressure, static pressure and temperature. The velocity and static pressure measurement system consisted of a pitot tube and inclined manometer. The stack gas temperature was measured with a K-type thermocouple and pyrometer. Stack gas velocity pressure and temperature readings were recorded during each test run. The data collected was utilized to calculate the volumetric flow rate in accordance with U.S. EPA Reference Test Method 2. 2.2 U.S. EPA Reference Test Method 3A – Oxygen/Carbon Dioxide The oxygen (O2) and carbon dioxide (CO2) testing was conducted in accordance with U.S. EPA Reference Test Method 3A. Data was collected online and reported in one-minute averages. The sampling system consisted of a stainless-steel probe, Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas conditioning system was a non-contact condenser used to remove moisture from the stack gas. If an unheated Teflon sample line was used, then a portable non-contact condenser was placed in the system directly after the probe. Otherwise, a heated Teflon sample line was used. The quality control measures are described in Section 2.5. 2.3 U.S. EPA Reference Test Method 320 – BWS, NOx, CO, VOC, NMHC, CH4, C2H6 and H2CO The concentrations of concentrations of moisture content (BWS), nitrogen oxides (NOx), carbon monoxide (CO), volatile organic compounds (VOC), non-methane hydrocarbons (NMHC), methane (CH4), ethane (C2H6) and formaldehyde (H2CO) were determined in accordance with U.S. EPA Reference Test Method 320. Each source gas stream was extracted at a constant rate through a heated probe, heated filter and heated sample line and analyzed with a MKS MultiGas 2030 FTIR operated by a portable computer. The computer has FTIR spectra of calibration gases stored on the hard drive. These single component calibration spectra are used to analyze the measured sample spectra. The gas 8 of 99 Source Test Report Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-2 components to be measured were selected from the spectra library and incorporated into the analytical method. The signal amplitude, linearity, and signal to noise ratio were measured and recorded to document analyzer performance. A leak check was performed on the sample cell. The instrument path length was verified using ethylene as the Calibration Transfer Standard. Dynamic spiking was performed using a certified standard of the target compound or appropriate surrogate in nitrogen with sulfur hexafluoride blended as a tracer to calculate the dilution factor. All test spectra, interferograms, and analytical method information are recorded and stored with the calculated analytical results. The quality control measures are described in Section 2.6. 2.4 U.S. EPA Reference Test Method 205 – Gas Dilution System Certification A calibration gas dilution system field check was conducted in accordance with U.S. EPA Reference Method 205. An initial three (3) point calibration was conducted, using individual Protocol 1 gases, on the analyzer used to complete the dilution system field check. Multiple dilution rates and total gas flow rates were utilized to force the dilution system to perform two dilutions on each mass flow controller. The diluted calibration gases was sent directly to the analyzer, and the analyzer response recorded in an electronic field data sheet. A mid-level supply gas, with a cylinder concentration within 10% of one of the gas divider settings described above, was introduced directly to the analyzer, and the analyzer response recorded in an electronic field data sheet. The cylinder concentration and the analyzer response agreed within 2%. These steps were repeated three (3) times. The average analyzer response agreed within 2% of the predicted gas concentration. No single injection differed more than 2% from the average instrument response for that dilution. Copies of the Method 205 data can be found in the Quality Assurance/Quality Control Appendix. 2.5 Quality Assurance/Quality Control – U.S. EPA Reference Test Method 3A Cylinder calibration gases used met EPA Protocol 1 (+/- 2%) standards. Copies of all calibration gas certificates can be found in the Quality Assurance/Quality Control Appendix. Low Level gas was introduced directly to the analyzer. After adjusting the analyzer to the Low-Level gas concentration and once the analyzer reading was stable, the analyzer value was recorded. This process was repeated for the High-Level gas. For the Calibration Error Test, Low, Mid, and High Level calibration gases were sequentially introduced directly to the analyzer. All values were within 2.0 percent of the Calibration Span or 0.5% absolute difference. High or Mid Level gas (whichever was closer to the stack gas concentration) was introduced at the probe and the time required for the analyzer reading to reach 95 percent or 0.5% (whichever was less restrictive) of the gas concentration was recorded. The analyzer reading was observed until it reached a stable value, and this value was recorded. Next, Low Level gas was introduced at the probe and the time required for the analyzer reading to decrease to a value within 5.0 percent or 0.5% (whichever was less restrictive) was recorded. If the Low -Level gas was zero gas, the response was 0.5% or 5.0 percent of the upscale gas concentration (whichever was less restrictive). The analyzer reading was observed until it reached a stable value and this value was recorded. The measurement system response time and initial system bias were determined from these data. The System Bias was within 5.0 percent of the Calibration Span or 0.5% absolute difference. High or Mid Level gas (whichever was closer to the stack gas concentration) was introduced at the probe. After the analyzer response was stable, the value was recorded. Next, Low Level gas was introduced at the probe, and the analyzer value recorded once it reached a stable response. The System Bias was within 5.0 percent of the 9 of 99 Source Test Report Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-3 Calibration Span or 0.5% absolute difference or the data was invalidated and the Calibration Error Test and System Bias were repeated. Drift between pre- and post-run System Bias was within 3 percent of the Calibration Span or 0.5% absolute difference. If the drift exceeded 3 percent or 0.5%, the Calibration Error Test and System Bias were repeated. To determine the number of sampling points, a gas stratification check was conducted prior to initiating testing. The pollutant concentrations were measured at twelve traverse points (as described in Method 1). Each traverse point was sampled for a minimum of twice the system response time. If the diluent concentration at each traverse point did not differ more than 5 percent or 0.3% (whichever was less restrictive) of the average pollutant concentration, then single point sampling was conducted during the test runs. If the pollutant concentration did not meet these specifications but differed less than 10 percent or 0.5% from the average concentration, then three (3) point sampling was conducted (stacks less than 7.8 feet in diameter - 16.7, 50.0 and 83.3 percent of the measurement line; stacks greater than 7.8 feet in diameter – 0.4, 1.0, and 2.0 meters from the stack wall). If the pollutant concentration differed by more than 10 percent or 0.5% from the average concentration, then sampling was conducted at a minimum of twelve (12) traverse points. Copies of stratification check data can be found in the Quality Assurance/Quality Control Appendix. A Data Acquisition System with battery backup was used to record the instrument response in one (1) minute averages. The data was continuously stored as a *.CSV file in Excel format on the hard drive of a computer. At the completion of testing, the data was also saved to the Alliance server. All data was reviewed by the Field Team Leader before leaving the facility. Once arriving at Alliance’s office, all written and electronic data was relinquished to the report coordinator and then a final review was performed by the Project Manager. 2.6 Quality Assurance/Quality Control – U.S. EPA Reference Method 320 EPA Protocol 1 Calibration Gases – Cylinder calibration gases used met EPA Protocol 1 (+/- 2%) standards. Copies of all calibration gas certificates can be found in the Quality Assurance/Quality Control Appendix. After providing ample time for the FTIR to reach the desired temperature and to stabilize, zero gas (nitrogen) was introduced directly to the instrument sample port. While flowing nitrogen the signal amplitude was recorded, a background spectra was taken, a linearity check was performed and recorded, the peak to peak noise and the root mean square in the spectral region of interest was measured and a screenshot was recorded. Following the zero gas checks, room air was pulled through the sample chamber and the line width and resolution was verified to be at 1879 cm-1, the peak position was entered and the FWHH was recorded (screenshot). Following these checks, another background spectra was recorded and the calibration transfer standard (CTS) was introduced directly to the instrument sample port. The CTS instrument recovery was recorded and the instrument mechanical response time was measured. Next, stack gas was introduced to the FTIR through the sampling system and several scans were taken until a stable reading was achieved. The native concentration of our surrogate spiking analyte (acetaldehyde) was recorded. Spike gas was introduced to the sampling system at a constant flow rate ≤ 10% of the total sample flow rate and a 10 of 99 Source Test Report Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-4 corresponding dilution ratio was calculated along with a system response time. Matrix spike recovery spectra were recorded and were within the ± 30% of the calculated value of the spike concentration that the method requires. The matrix spike recovery was conducted once at the beginning of the testing and the CTS recovery procedures were repeated following each test run. The corresponding values were recorded. 11 of 99 Appendix A 12 of 99 Example Calculations Location Source Project No. Run No. Parameter(s) Absolute Stack Gas Pressure (Ps), in. Hg where, Pb 25.61 = barometric pressure, in. Hg Pg 3.50 = static pressure, in. H2O Ps 25.87 = in. Hg Molecular Weight (DRY) (Md), lb/lb-mole where, CO2 8.5 = carbon dioxide concentration, % O2 10.5 = oxygen concentration, % Md 29.78 = lb/lb mol Molecular Weight (WET) (Ms), lb/lb-mole where, Md 29.78 = molecular weight (DRY), lb/lb mol BWS 0.103 = moisture fraction, dimensionless Ms 28.57 = lb/lb mol Average Velocity (Vs), ft/sec where, Cp 0.84 = pitot tube coefficient Δ P1/2 1.158 = average pre/post test velocity head of stack gas, (in. H2O)1/2 Ts 747.9 = average pre/post test absolute stack temperature, °R Ps 25.87 = absolute stack gas pressure, in. Hg Ms 28.57 = molecular weight of stack gas, lb/lb mol Vs 83.7 = ft/sec Average Stack Gas Flow at Stack Conditions (Qa), acfm where, Vs 83.7 = stack gas velocity, ft/sec As 2.18 = cross-sectional area of stack, ft 2 Qa 10,954 = acfm Average Stack Gas Flow at Standard Conditions (Qs), dscfm Ps Ts where, Qa 10,954 = average stack gas flow at stack conditions, acfm BWS 0.103 = moisture fraction, dimensionless Ps 25.87 = absolute stack gas pressure, in. Hg Ts 747.9 = average pre/post test absolute stack temperature, °R Qs 5,993 = dscfm Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 1 VFR Qsd = 17.636 x Qa x (1 - BWS) x Ms ൌ Md ሺ1 െ BWSሻ ൅ 18.015 ሺBWSሻ Md ൌ ሺ0.44 ൈ % COଶ ሻ ൅ ሺ0.32 ൈ % O2ሻ ൅ ሺ0.28 ሺ100 െ % COଶ െ % O2ሻሻ Ps ൌ Pb ൅ Pg 13 6 Vs ൌ 85.49 ൈ Cp ൈ ሺΔ P ଵ/ଶ ሻ avg ൈ Ts Ps x Ms Qa ൌ 60 ൈ Vs ൈ As 13 of 99 Location: Source: Project No.: Run No. /Method O₂ - Outlet Concentration (C O₂), % dry CMA ( CM - C0 ) where, Cobs 10.4 = average analyzer value during test, % dry Co 0.0 = average of pretest & posttest zero responses, % dry CMA 11.0 = actual concentration of calibration gas, % dry CM 10.9 = average of pretest & posttest calibration responses, % dry CO₂10.54 = O₂ Concentration, % dry Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 3A CO₂ = ( Cobs - C0 ) x CO₂ - Outlet Concentration (C CO₂), % dry C M A ( CM - C 0 ) where, Cobs 8.6 Co 0.0 CMA 11.0 CM 11.1 CCO₂8.49 = average analyzer value during test, % dry = average of pretest & posttest zero responses, % dry = actual concentration of calibration gas, % dry = average of pretest & posttest calibration responses, % dry = CO₂ Concentration, % dry CCO₂ = ( Cobs - C0 ) x Example Calculations 14 of 99 Example Calculations Location: Source: Project No.: Run No. /Method CO - Outlet Concentration (C CO), ppmvd CCOw 1 - BWS where, CCOw 421.6 = CO - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CCO 470.10 = ppmvd CO - Outlet Concentration (C COc15), ppmvd @ 15% O₂ 20.9 - 15 20.9 - O₂ where, CCO 470.1 = CO - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % CCOc15 267.85 = ppmvd @15% O₂ CO - Outlet Emission Rate (ER CO), lb/hr where, CCO 470.1 = CO - Outlet Concentration, ppmvd MW 28.01 = CO molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ERCO 12.3 = lb/hr CO - Outlet Emission Rate (ER COTPY), ton/yr ERCO x 8,760 2,000 where, ERCO 12.3 = CO - Outlet Emission Rate, lb/hr ERCOTPY 53.9 = ton/yr CO - Outlet Emission Factor (EFCO), g/hp-hr ERCO x 454 EBW where, ERCO 12.3 = CO - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EFCO 2.4 = g/hp-hr ERCOTPY = EFCO = ERCO =CCO x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 CCOc15 = CCO x CCO = Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 15 of 99 Example Calculations Location: Source: Project No.: Run No. /Method NOx - Outlet Concentration (C NOx), ppmvd CNOxw 1 - BWS where, CNOxw 55.0 = NOx - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CNOx 61.32 = ppmvd NOx - Outlet Concentration (C NOxc15), ppmvd @ 15% O₂ 20.9 - 15 20.9 - O₂ where, CNOx 61.3 = NOx - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % CNOxc15 34.94 = ppmvd @15% O₂ NOx - Outlet Emission Rate (ERNOx), lb/hr where, CNOx 61.3 = NOx - Outlet Concentration, ppmvd MW 46.0055 = NOx molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ERNOx 2.6 = lb/hr NOx - Outlet Emission Rate (ERNOxTPY), ton/yr ERNOx x 8,760 2,000 where, ERNOx 2.6 = NOx - Outlet Emission Rate, lb/hr ERNOxTPY 11.5 = ton/yr NOx - Outlet Emission Factor (EFNOx), g/hp-hr ERNOx x 454 EBW where, ERNOx 2.6 = NOx - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EFNOx 0.52 = g/hp-hr ERNOxTPY = EFNOx = ERNOx =CNOx x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 CNOxc15 = CNOx x CNOx = Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 16 of 99 Example Calculations Location: Source: Project No.: Run No. /Method VOC - Outlet Concentration (C VOC), ppmvd CVOCw 1 - BWS where, CVOCw 13.3 = VOC - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CVOC 14.80 = ppmvd VOC - Outlet Concentration (C VOCc15), ppmvd @ 15% O₂ 20.9 - 15 20.9 - O₂ where, CVOC 14.8 = VOC - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % CVOCc15 8.43 = ppmvd @15% O₂ VOC - Outlet Emission Rate (ERVOC), lb/hr where, CVOC 14.8 = VOC - Outlet Concentration, ppmvd MW 44.1 = VOC molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ERVOC 0.61 = lb/hr VOC - Outlet Emission Rate (ERVOCTPY), ton/yr ERVOC x 8,760 2,000 where, ERVOC 0.61 = VOC - Outlet Emission Rate, lb/hr ERVOCTPY 2.7 = ton/yr VOC - Outlet Emission Factor (EFVOC), g/hp-hr ERVOC x 454 EBW where, ERVOC 0.61 = VOC - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EFVOC 0.12 = g/hp-hr Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 CVOCc15 = CVOC x CVOC = ERVOCTPY = EFVOC = ERVOC =CVOC x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 17 of 99 Example Calculations Location: Source: Project No.: Run No. /Method Methane - Outlet Concentration (C CH₄), ppmvd CCH₄w 1 - BWS where, CCH₄w 1721.5 = Methane - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CCH₄1919.5 = ppmvd Methane - Outlet Concentration (C<CH ₄w>), ppmvw where, C<CH₄> 1919.5 = Methane - Outlet Concentration, ppmvd BWS 0.103 = moisture fraction, unitless C<CH₄w> 1721.5 = ppmvw Methane - Outlet Concentration (C<CH₄c15>), ppmvd @ 15% O₂ 20.9 - 15 20.9 - O₂ where, C<CH₄> 1919.5 = Methane - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % C<CH₄c15> 1093.7 = ppmvd @15% O₂ Methane - Outlet Emission Rate (ER<CH₄>), lb/hr where, C<CH₄> 1919.5 = Methane - Outlet Concentration, ppmvd MW 16.04 = CH₄ molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ER<CH₄> 28.8 = lb/hr Methane - Outlet Emission Rate (ER<CH₄TPY>), ton/yr ER<CH₄> x 8,760 2,000 where, ER<CH₄> 28.8 = Methane - Outlet Emission Rate, lb/hr ER<CH₄TPY> 125.9 = ton/yr Methane - Outlet Emission Factor (EF<CH₄>), g/hp-hr ER<CH₄> x 454 EBW where, ER<CH₄> 28.8 = Methane - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EF<CH₄> 5.7 = g/hp-hr Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 C<CH₄w> = C<CH₄> x (1 - BWS) C<CH₄c15> = C<CH₄> x CCH₄ = ER<CH₄TPY> = EF<CH₄> = ER<CH₄> =C<CH₄> x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 18 of 99 Example Calculations Location: Source: Project No.: Run No. /Method Ethane - Outlet Concentration (C<C ₂H₆>), ppmvd CC₂H₆w 1 - BWS where, CC₂H₆w 17.4 = Ethane - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CC₂H₆19.4 = ppmvd Ethane - Outlet Concentration (C<C ₂H₆w>), ppmvw where, C<C₂H₆> 19.4 = Ethane - Outlet Concentration, ppmvd BWS 0.103 = moisture fraction, unitless C<C₂H₆w> 17.4 = ppmvw Ethane - Outlet Concentration (C<C ₂H₆c15>), ppmvd @ 15% O₂ 20.9 - 15 20.9 - O₂ where, C<C₂H₆> 19.4 = Ethane - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % C<C₂H₆c15> 11.0 = ppmvd @15% O₂ Ethane - Outlet Emission Rate (ER<C₂H₆>), lb/hr where, C<C₂H₆> 19.4 = Ethane - Outlet Concentration, ppmvd MW 30.07 = C₂H₆ molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ER<C₂H₆> 0.54 = lb/hr Ethane - Outlet Emission Rate (ER<C₂H₆TPY>), ton/yr ER<C₂H₆> x 8,760 2,000 where, ER<C₂H₆> 0.54 = Ethane - Outlet Emission Rate, lb/hr ER<C₂H₆TPY> 2.4 = ton/yr Ethane - Outlet Emission Factor (EF<C₂H₆>), g/hp-hr ER<C₂H₆> x 454 EBW where, ER<C₂H₆> 0.54 = Ethane - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EF<C₂H₆> 0.11 = g/hp-hr Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 C<C₂H₆w> = C<C₂H₆> x (1 - BWS) C<C₂H₆c15> = C<C₂H₆> x CC₂H₆ = ER<C₂H₆TPY> = EF<C₂H₆> = ER<C₂H₆> =C<C₂H₆> x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 19 of 99 Example Calculations Location: Source: Project No.: Run No. /Method Formaldehyde - Outlet Concentration (C CHOH), ppmvd CCHOHw 1 - BWS where, CCHOHw 55.9 = Formaldehyde - Outlet Concentration, ppmvw BWS 0.103 = moisture fraction, unitless CCHOH 62.3 = ppmvd Formaldehyde - Outlet Concentration (C<CHOHw>), ppmvw where, C<CHOH> 62.3 = Formaldehyde - Outlet Concentration, ppmvd BWS 0.103 = moisture fraction, unitless C<CHOHw> 55.9 = ppmvw Formaldehyde - Outlet Concentration (C<CHOHc15>), ppmvd @ 15% O ₂ 20.9 - 15 20.9 - O₂ where, C<CHOH> 62.3 = Formaldehyde - Outlet Concentration, ppmvd CO₂10.5 = oxygen concentration, % C<CHOHc15> 35.5 = ppmvd @15% O₂ Formaldehyde - Outlet Emission Rate (ER<CHOH>), lb/hr where, C<CHOH> 62.3 = Formaldehyde - Outlet Concentration, ppmvd MW 30.031 = CHOH molecular weight, g/g-mole Qs 5,993 = stack gas volumetric flow rate at standard conditions, dscfm ER<CHOH> 1.7 = lb/hr Formaldehyde - Outlet Emission Rate (ER<CHOHTPY>), ton/yr ER<CHOH> x 8,760 2,000 where, ER<CHOH> 1.7 = Formaldehyde - Outlet Emission Rate, lb/hr ER<CHOHTPY> 7.7 = ton/yr Formaldehyde - Outlet Emission Factor (EF<CHOH>), g/hp-hr ER<CHOH> x 454 EBW where, ER<CHOH> 1.7 = Formaldehyde - Outlet Emission Rate, lb/hr EBW 2,280 = engine brake work, HP EF<CHOH> 0.35 = g/hp-hr Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run 1 / Method 320 C<CHOHw> = C<CHOH> x (1 - BWS) C<CHOHc15> = C<CHOH> x CCHOH = R<CHOHTPY> = EF<CHOH> = ER<CHOH> =C<CHOH> x MW x Qs x 60 x 28.32 24.04 x 1.0E06 x 454 𝑚𝑖𝑛 ℎ𝑟 𝐿 𝑓𝑡ଷ 𝐿 𝑔െ𝑚𝑜𝑙𝑒 𝑔 𝑙𝑏 𝑙𝑏 𝑡𝑜𝑛 ℎ𝑟 𝑦𝑟 𝑔 𝑙𝑏 20 of 99 Location Source(s) Project No. Date(s) Where, CTSavg 97.55 = average of all CTS calibration gas readings, ppm CTScyl 101 = CTS bottle certified gas value, ppm CTSR 96.6% = CTS recovery value, % Spike Dilution Factor (DF), % Where, SF6dir 4.45 = average of direct tracer gas value readings SF6nat 0.01 = average of native tracer gas value readings SF6spike 0.276888 = average of dynamic spike tracer gas value readings DF 5.99% = spike dilution factor, % Calculated Spike (Spikecalc), ppm Where, DF % 5.99% = spike dilution factor, % Analytedir 86.58 = average of direct analyte gas values, ppm Analyte nat 0.14 = average of native analyte gas values, ppm Spikecalc 5.32 = calculated spike, ppm value, ppm Spike Recovery Value (SpikeR), % Where, Spikecalc 5.32 = calculated spike, ppm value, ppm Analytespike 5.18 = average of spiked analyte gas values, ppm SpikeR 97.42% = spike recovery value, % Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/2024 CTS Recovery Value (CTSR), % 𝐶𝑇𝑆௔௩௚ 𝐶𝑇𝑆௖௬௟ ൈ 100 𝑆𝐹6௦௣௜௞௘ െ𝑆𝐹6௡௔௧ 𝑆𝐹6ௗ௜௥ ൈ 100 𝐷𝐹 ൈ 𝐴𝑛𝑎𝑙𝑦𝑡𝑒𝑑𝑖𝑟൅ሺ𝐴𝑛𝑎𝑙𝑦𝑡𝑒௡௔௧ ൈ 1 െ𝐷𝐹 ሻ 𝐴𝑛𝑎𝑙𝑦𝑡𝑒௦௣௜௞௘ 𝑆𝑝𝑖𝑘𝑒௖௔௟௖ ൈ 100 Example Calculations 21 of 99 Appendix B 22 of 99 Jenbacher Engine #1 23 of 99 Emissions Calculations Location Source Project No. Run Number Run 1 Run 2 Run 3 Average Date 9/4/24 9/5/24 9/5/24 -- Start Time 8:25 9:47 11:07 -- Stop Time 9:24 10:46 12:06 -- Engine Manufacturer Engine Model Engine Serial Number Engine Type Engine Date of Manufacturer DOM Engine Hour Meter Reading EMR Generator Output, Hz Gen OP 60 60 60 60 Engine Speed, RPM ES 1,500 1,500 1,500 1,500 Engine Brake Work, HP EBW 2,280 2,280 2,279 2,280 Maximum Brake Work, HP MaxEBW 2,509 2,509 2,509 2,509 Engine Load, % EL 94 94 94 94 Ambient Temperature TAmb 66 75 79 73 Relative Humidity, % RH 47 32 24 34 Barometric Pressure, in. Hg Pb 25.61 25.61 25.61 25.61 Moisture Fraction, dimensionless BWS 0.103 0.103 0.103 0.103 Volumetric Flow Rate (M1-4), dscfm Qs 5,993 5,941 5,948 5,961 O₂ Concentration, % dry CO₂10.54 10.54 10.52 10.54 CO₂ Concentration, % dry CCO₂8.49 8.49 8.49 8.49 Methane - Outlet Concentration, ppmvd CCH₄1919.50 1923.36 1916.31 1919.72 Methane - Outlet Concentration, ppmvw CCH₄w 1721.54 1724.46 1718.24 1721.41 Methane - Outlet Concentration, ppmvd @ 15 % O₂C<CH₄c15> 1093.67 1095.04 1089.75 1092.82 Methane - Outlet Emission Rate, lb/hr ER<CH₄> 28.8 28.6 28.5 28.6 Methane - Outlet Emission Rate, ton/yr ER<CH₄TPY> 125.9 125.1 124.8 125.3 Methane - Outlet Emission Factor, g/HP-hr EF<CH₄> 5.7 5.7 5.7 5.7 Ethane - Outlet Concentration, ppmvd CC₂H₆19.36 19.20 19.03 19.20 Ethane - Outlet Concentration, ppmvw CC₂H₆w 17.36 17.22 17.06 17.21 Ethane - Outlet Concentration, ppmvd @ 15 % O₂C<C₂H₆c15> 11.03 10.93 10.82 10.93 Ethane - Outlet Emission Rate, lb/hr ER<C₂H₆> 0.54 0.53 0.53 0.54 Ethane - Outlet Emission Rate, ton/yr ER<C₂H₆TPY> 2.4 2.3 2.3 2.3 Ethane - Outlet Emission Factor, g/HP-hr EF<C₂H₆> 0.11 0.11 0.11 0.11 Formaldehyde - Outlet Concentration, ppmvd CCHOH 62.32 62.50 62.31 62.38 Formaldehyde - Outlet Concentration, ppmvw CCHOHw 55.89 56.04 55.87 55.93 Formaldehyde - Outlet Concentration, ppmvd @ 15 % O₂C<CHOHc15> 35.51 35.58 35.43 35.51 Formaldehyde - Outlet Emission Rate, lb/hr ER<CHOH> 1.7 1.7 1.7 1.7 Formaldehyde - Outlet Emission Rate, ton/yr ER<CHOHTPY>7.7 7.6 7.6 7.6 Formaldehyde - Outlet Emission Factor, g/HP-hr EF<CHOH> 0.35 0.35 0.35 0.35 CO - Outlet Concentration, ppmvd CCO 470.10 470.62 469.96 470.23 CO - Outlet Concentration, ppmvw CCOw 421.62 421.95 421.38 421.65 CO - Outlet Concentration, ppmvd @ 15 % O₂CCOc15 267.85 267.94 267.25 267.68 CO - Outlet Emission Rate, lb/hr ERCO 12.3 12.2 12.2 12.2 CO - Outlet Emission Rate, ton/yr ERCOTPY 53.9 53.5 53.4 53.6 CO - Outlet Emission Factor, g/HP-hr EFCO 2.4 2.4 2.4 2.4 NOx - Outlet Concentration, ppmvd CNOx 61.32 61.25 61.40 61.32 NOx - Outlet Concentration, ppmvd @ 15 % O₂CNOxc15 34.94 34.87 34.91 34.91 NOx - Outlet Emission Rate, lb/hr ERNOx 2.6 2.6 2.6 2.6 NOx - Outlet Emission Rate, ton/yr ERNOxTPY 11.5 11.4 11.5 11.5 NOx - Outlet Emission Factor, g/HP-hr EFNOx 0.52 0.52 0.52 0.52 VOC - Outlet Concentration, ppmvd CVOC 14.80 13.98 13.04 13.94 VOC - Outlet Concentration, ppmvd @ 15 % O₂CVOCc15 8.43 7.96 7.42 7.94 VOC - Outlet Emission Rate, lb/hr ERVOC 0.61 0.57 0.53 0.57 VOC - Outlet Emission Rate, ton/yr ERVOCTPY 2.7 2.5 2.3 2.5 VOC - Outlet Emission Factor, g/HP-hr EFVOC 0.12 0.11 0.11 0.11 NMHC - Outlet Concentration, ppmvd CNMHC 34.16 33.18 32.07 33.14 NMHC - Outlet Concentration, ppmvd @ 15 % O₂CNMHCc15 19.46 18.89 18.24 18.86 NMHC - Outlet Emission Rate, lb/hr ERNMHC 1.4 1.4 1.3 1.4 NMHC - Outlet Emission Rate, ton/yr ERNMHCTPY 6.2 5.9 5.7 5.9 NMHC - Outlet Emission Factor, g/HP-hr EFNMHC 0.28 0.27 0.26 0.27 *VOC excludes Formaldehyde, methane, and ethane. NMHC value adds ethane back to VOC. Engine Data 25,878 Input Data - Outlet Calculated Data - Outlet Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 GE Jenbacher JMS 612-F28F02 1322399 Spark Ignition - 4SLB 2017-01-01 24 of 99 Run 1 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.45 8.56 Cal Gas Concentration (CMA)11.00 10.99 Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.01 -0.03 Average Zero Response (Co)0.01 -0.02 Pretest System Cal Response 10.91 11.08 Posttest System Cal Response 10.89 11.09 Average Cal Response (CM)10.90 11.09 Corrected Run Average (Corr)10.54 8.49 8:25 10.46 8.53 8:26 10.46 8.54 8:27 10.46 8.55 8:28 10.46 8.54 8:29 10.45 8.55 8:30 10.46 8.53 8:31 10.45 8.55 8:32 10.46 8.54 8:33 10.46 8.55 8:34 10.46 8.55 8:35 10.47 8.55 8:36 10.46 8.57 8:37 10.45 8.58 8:38 10.45 8.57 8:39 10.44 8.58 8:40 10.45 8.58 8:41 10.44 8.57 8:42 10.44 8.58 8:43 10.43 8.58 8:44 10.43 8.58 8:45 10.44 8.59 8:46 10.44 8.59 8:47 10.44 8.59 8:48 10.44 8.59 8:49 10.44 8.60 8:50 10.44 8.58 8:51 10.44 8.59 8:52 10.44 8.58 8:53 10.43 8.57 8:54 10.45 8.58 8:55 10.44 8.57 8:56 10.45 8.56 8:57 10.45 8.57 8:58 10.45 8.56 8:59 10.45 8.56 9:00 10.45 8.57 9:01 10.45 8.56 9:02 10.45 8.57 9:03 10.45 8.56 9:04 10.45 8.56 9:05 10.45 8.54 9:06 10.45 8.56 9:07 10.45 8.55 9:08 10.45 8.55 9:09 10.46 8.55 9:10 10.45 8.55 9:11 10.45 8.55 9:12 10.45 8.55 9:13 10.45 8.55 9:14 10.45 8.56 9:15 10.46 8.55 9:16 10.45 8.55 9:17 10.45 8.55 9:18 10.45 8.55 9:19 10.45 8.54 9:20 10.46 8.55 9:21 10.46 8.55 9:22 10.45 8.56 9:23 10.45 8.54 9:24 10.45 8.56 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/5/24 25 of 99 Run 1 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 8:25 192.1 1.008 1,721.7 17.7 55.8 422.5 61.6 14.0 31.7 10.3 8:26 192.1 1.009 1,711.2 17.4 55.5 420.5 61.4 14.5 31.9 10.3 8:27 192.1 1.008 1,721.4 17.6 56.2 421.6 61.1 14.6 32.2 10.4 8:28 192.1 1.009 1,723.3 17.7 56.2 422.4 61.1 14.3 32.1 10.3 8:29 192.1 1.010 1,729.4 17.6 55.8 421.6 61.1 14.7 32.3 10.3 8:30 192.2 1.011 1,721.9 17.5 55.7 421.0 61.3 15.0 32.5 10.3 8:31 192.1 1.009 1,710.0 17.6 55.4 420.0 60.9 14.3 31.9 10.3 8:32 192.2 1.009 1,730.2 17.8 56.5 422.2 60.3 15.2 33.1 10.4 8:33 192.2 1.009 1,725.0 17.7 56.4 421.7 61.0 14.5 32.2 10.3 8:34 192.2 1.010 1,730.8 17.8 56.2 422.5 60.9 15.1 32.9 10.3 8:35 192.2 1.009 1,729.0 17.6 56.1 421.2 60.9 15.2 32.8 10.3 8:36 192.1 1.008 1,719.7 17.6 55.8 421.2 60.5 15.0 32.6 10.3 8:37 192.2 1.010 1,733.9 17.9 56.3 422.9 60.1 15.2 33.1 10.3 8:38 192.1 1.009 1,738.7 17.7 56.5 421.5 60.7 15.1 32.8 10.3 8:39 192.2 1.009 1,732.5 17.6 56.3 422.2 61.0 15.0 32.6 10.3 8:40 192.2 1.009 1,730.0 17.5 56.1 421.8 60.9 14.9 32.5 10.3 8:41 192.2 1.009 1,733.8 17.9 55.9 422.5 60.9 15.2 33.1 10.3 8:42 192.1 1.010 1,729.4 17.7 55.9 422.1 61.0 15.1 32.7 10.3 8:43 192.2 1.009 1,737.4 17.7 56.2 423.6 61.5 14.6 32.3 10.3 8:45 192.1 1.009 1,729.2 17.7 56.2 422.2 61.7 14.7 32.3 10.3 8:46 192.1 1.008 1,725.5 17.7 56.2 421.4 61.2 14.9 32.5 10.4 8:47 192.1 1.010 1,713.3 17.5 55.7 421.7 61.3 14.0 31.5 10.3 8:48 192.1 1.010 1,726.2 17.7 55.9 420.7 61.0 14.6 32.3 10.3 8:49 192.1 1.009 1,744.0 17.9 56.2 424.2 61.2 14.8 32.8 10.3 8:50 192.1 1.009 1,725.4 17.8 55.9 421.5 61.7 14.7 32.5 10.3 8:51 192.1 1.010 1,728.6 17.6 56.6 422.0 61.2 14.8 32.4 10.4 8:52 192.1 1.009 1,722.8 17.4 55.8 421.6 61.5 14.4 31.8 10.3 8:53 192.1 1.008 1,730.0 17.5 55.6 423.1 61.2 15.1 32.7 10.3 8:54 192.1 1.007 1,739.6 17.6 55.9 424.9 61.6 14.7 32.3 10.3 8:55 192.1 1.009 1,720.0 17.3 56.2 421.1 61.8 15.0 32.3 10.4 8:56 192.1 1.008 1,720.2 17.6 55.9 422.4 61.5 14.6 32.2 10.3 8:57 192.1 1.010 1,728.8 17.4 56.0 423.2 61.1 14.9 32.3 10.3 8:58 192.1 1.008 1,717.6 17.4 55.9 421.6 61.3 14.6 32.0 10.4 8:59 192.1 1.009 1,727.9 17.2 55.8 422.9 61.2 15.1 32.3 10.3 9:00 192.2 1.009 1,711.5 17.2 56.1 420.7 61.4 15.1 32.3 10.4 9:01 192.1 1.010 1,723.6 17.1 56.3 422.2 61.2 14.8 31.9 10.3 9:02 192.1 1.009 1,717.9 17.0 55.9 421.1 61.8 15.3 32.4 10.3 9:03 192.1 1.010 1,722.2 17.3 55.8 422.5 61.5 15.1 32.5 10.3 9:04 192.1 1.008 1,706.7 16.9 55.5 420.7 61.4 15.1 32.0 10.3 9:05 192.1 1.009 1,715.2 16.9 55.5 420.8 61.8 14.5 31.4 10.3 9:06 192.1 1.009 1,719.5 17.0 55.6 421.1 61.9 15.1 32.1 10.3 9:08 192.1 1.009 1,712.6 17.0 55.8 420.0 61.8 14.9 31.9 10.3 9:09 192.1 1.009 1,710.6 16.9 55.6 420.2 61.7 15.0 31.9 10.3 9:10 192.1 1.009 1,703.0 16.8 55.4 419.4 61.7 15.0 31.8 10.3 9:11 192.1 1.009 1,709.6 17.0 55.5 420.4 61.7 15.4 32.4 10.3 9:12 192.1 1.010 1,708.1 17.0 55.7 420.5 61.7 14.6 31.6 10.3 9:13 192.1 1.010 1,716.0 17.0 55.6 421.7 61.4 15.1 32.2 10.3 9:14 192.1 1.009 1,720.2 17.0 55.7 422.4 61.7 14.6 31.6 10.3 9:15 192.1 1.009 1,712.5 17.0 55.6 421.4 61.8 14.4 31.4 10.3 9:16 192.1 1.009 1,717.4 17.1 55.7 422.5 61.7 14.7 31.8 10.3 9:17 192.1 1.010 1,719.3 17.2 55.7 420.2 61.4 14.6 31.8 10.3 9:18 192.1 1.010 1,723.0 17.2 56.0 421.9 61.7 14.6 31.8 10.3 9:19 192.1 1.009 1,713.7 17.1 55.8 421.2 61.6 14.8 31.9 10.4 9:20 192.1 1.009 1,717.2 17.0 55.7 421.8 61.4 14.8 31.8 10.3 9:21 192.1 1.009 1,708.9 16.9 55.4 420.0 61.4 14.8 31.6 10.4 9:22 192.1 1.010 1,712.6 17.0 55.6 420.4 61.4 14.3 31.2 10.3 9:23 192.1 1.009 1,715.4 17.0 56.0 421.1 61.5 14.6 31.6 10.4 9:24 192.1 1.008 1,706.2 16.8 55.7 420.4 61.3 14.9 31.7 10.3 9:25 192.1 1.010 1,719.5 17.0 56.2 421.6 61.3 14.8 31.8 10.4 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.1 1.009 1721.5 17.4 55.9 421.6 61.3 14.8 32.2 10.3 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/24 26 of 99 Run 2 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.44 8.58 Cal Gas Concentration (CMA)11.00 10.99 Pretest System Zero Response 0.01 -0.03 Posttest System Zero Response 0.01 -0.01 Average Zero Response (Co)0.01 -0.02 Pretest System Cal Response 10.89 11.09 Posttest System Cal Response 10.91 11.12 Average Cal Response (CM)10.90 11.11 Corrected Run Average (Corr)10.54 8.49 9:47 10.45 8.53 9:48 10.45 8.53 9:49 10.46 8.53 9:50 10.46 8.54 9:51 10.45 8.54 9:52 10.46 8.55 9:53 10.45 8.55 9:54 10.45 8.55 9:55 10.45 8.55 9:56 10.45 8.55 9:57 10.44 8.55 9:58 10.45 8.55 9:59 10.45 8.56 10:00 10.45 8.55 10:01 10.44 8.56 10:02 10.44 8.57 10:03 10.45 8.57 10:04 10.44 8.56 10:05 10.44 8.56 10:06 10.44 8.55 10:07 10.45 8.56 10:08 10.45 8.56 10:09 10.44 8.56 10:10 10.45 8.55 10:11 10.45 8.55 10:12 10.45 8.56 10:13 10.45 8.55 10:14 10.45 8.57 10:15 10.45 8.57 10:16 10.45 8.57 10:17 10.44 8.58 10:18 10.44 8.57 10:19 10.44 8.57 10:20 10.44 8.58 10:21 10.44 8.58 10:22 10.45 8.57 10:23 10.44 8.59 10:24 10.44 8.58 10:25 10.44 8.57 10:26 10.44 8.58 10:27 10.44 8.59 10:28 10.44 8.59 10:29 10.44 8.59 10:30 10.43 8.62 10:31 10.43 8.60 10:32 10.43 8.64 10:33 10.43 8.60 10:34 10.43 8.62 10:35 10.43 8.63 10:36 10.43 8.63 10:37 10.43 8.63 10:38 10.42 8.62 10:39 10.43 8.61 10:40 10.43 8.61 10:41 10.42 8.62 10:42 10.43 8.59 10:43 10.43 8.61 10:44 10.43 8.59 10:45 10.44 8.59 10:46 10.44 8.59 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/5/24 27 of 99 Run 2 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 9:47 192.1 1.010 1,728.4 17.3 55.4 421.6 61.1 13.5 30.8 10.2 9:48 192.1 1.010 1,741.5 17.5 55.8 423.7 61.2 13.5 31.0 10.3 9:49 192.1 1.012 1,723.8 17.1 55.6 421.9 61.5 13.9 31.1 10.4 9:50 192.1 1.009 1,730.2 17.3 55.6 421.7 61.1 13.1 30.4 10.3 9:51 192.1 1.010 1,742.8 17.4 55.9 422.7 61.2 14.0 31.4 10.4 9:52 192.1 1.011 1,725.6 17.5 55.9 421.1 61.4 13.6 31.1 10.3 9:53 192.1 1.009 1,729.6 17.4 55.8 423.1 61.3 13.8 31.1 10.3 9:54 192.1 1.008 1,728.7 17.4 55.5 422.5 61.4 13.2 30.6 10.4 9:55 192.1 1.010 1,732.3 17.3 55.5 422.9 61.3 13.6 30.9 10.3 9:56 192.1 1.009 1,728.5 17.5 55.7 422.2 61.5 14.0 31.5 10.4 9:57 192.1 1.010 1,719.3 17.3 56.7 420.2 61.0 13.7 31.0 10.5 9:58 192.1 1.009 1,733.3 17.4 56.1 422.5 61.5 14.1 31.5 10.3 9:59 192.1 1.009 1,738.0 17.3 55.7 422.5 61.2 13.9 31.2 10.3 10:00 192.0 1.009 1,727.2 17.3 55.4 421.0 61.3 14.6 32.0 10.3 10:01 192.1 1.009 1,710.6 16.9 56.3 420.4 61.2 13.8 30.7 10.5 10:02 192.1 1.010 1,733.7 17.2 56.5 421.8 61.2 13.9 31.1 10.4 10:03 192.1 1.011 1,712.1 17.1 55.9 420.0 61.2 13.8 31.0 10.3 10:04 192.1 1.011 1,730.9 17.3 56.2 422.6 61.2 14.1 31.4 10.3 10:05 192.1 1.010 1,711.4 17.1 56.3 420.7 61.1 14.0 31.1 10.4 10:06 192.1 1.009 1,716.4 17.0 55.9 422.5 61.0 13.3 30.3 10.3 10:08 192.1 1.009 1,725.7 17.1 56.2 422.5 61.6 13.6 30.7 10.4 10:09 192.1 1.009 1,714.8 17.1 55.8 421.4 61.7 14.2 31.3 10.3 10:10 192.1 1.011 1,726.1 17.1 55.9 422.8 61.2 14.1 31.2 10.3 10:11 192.1 1.010 1,706.4 16.8 55.5 420.1 61.8 13.4 30.2 10.3 10:12 192.1 1.009 1,719.4 17.1 55.9 422.0 61.5 13.8 30.9 10.4 10:13 192.1 1.009 1,722.1 17.3 55.9 421.9 61.5 13.6 30.9 10.3 10:14 192.1 1.010 1,723.7 17.1 56.2 422.2 61.6 13.9 31.0 10.3 10:15 192.1 1.008 1,724.9 17.2 56.2 421.9 61.4 14.0 31.2 10.3 10:16 192.1 1.012 1,714.6 17.2 55.8 421.6 61.2 13.6 30.9 10.3 10:17 192.1 1.011 1,718.1 17.2 56.0 419.7 60.9 14.3 31.5 10.4 10:18 192.1 1.008 1,734.3 17.1 56.2 422.4 60.8 14.2 31.4 10.3 10:19 192.1 1.008 1,732.6 17.3 56.3 422.6 61.5 14.5 31.8 10.4 10:20 192.1 1.009 1,722.7 17.3 56.1 421.7 61.3 13.6 30.9 10.3 10:21 192.1 1.009 1,741.8 17.4 56.3 423.4 61.1 14.4 31.8 10.4 10:22 192.0 1.009 1,715.0 17.0 55.6 420.8 61.2 14.0 30.9 10.3 10:23 192.1 1.009 1,723.0 17.2 55.8 422.7 61.1 14.2 31.4 10.4 10:24 192.1 1.009 1,736.2 17.3 56.3 423.7 61.5 14.2 31.5 10.3 10:25 192.0 1.008 1,722.8 17.3 56.0 421.2 61.9 13.6 31.0 10.4 10:26 192.1 1.010 1,712.6 17.2 55.7 422.0 61.5 13.7 30.9 10.3 10:27 192.1 1.010 1,731.7 17.4 56.3 424.0 61.0 14.2 31.5 10.4 10:28 192.1 1.010 1,725.6 17.2 56.2 422.0 61.0 13.8 31.1 10.3 10:29 192.1 1.011 1,731.2 17.1 56.5 422.8 61.0 14.1 31.2 10.3 10:31 192.1 1.008 1,724.7 17.4 56.5 422.4 60.9 14.8 32.2 10.4 10:32 192.0 1.009 1,734.0 17.3 56.9 423.6 60.5 14.3 31.7 10.4 10:33 192.1 1.009 1,724.7 17.2 56.7 422.3 61.1 14.2 31.4 10.4 10:34 192.1 1.011 1,719.5 17.2 56.6 421.5 60.9 14.3 31.5 10.3 10:35 192.0 1.010 1,718.8 17.2 55.8 421.2 60.9 14.7 31.9 10.3 10:36 192.0 1.009 1,737.4 17.3 56.2 423.7 61.1 14.2 31.5 10.3 10:37 192.1 1.007 1,732.4 17.3 56.3 422.6 60.9 14.6 31.8 10.4 10:38 192.0 1.012 1,720.3 17.0 55.9 421.1 60.9 14.6 31.6 10.3 10:39 192.1 1.011 1,716.8 17.2 56.2 421.3 61.0 14.3 31.5 10.3 10:40 192.1 1.011 1,713.4 16.9 55.9 419.6 61.1 14.3 31.3 10.3 10:41 192.1 1.010 1,725.8 17.3 56.3 421.8 61.3 14.1 31.5 10.4 10:42 192.1 1.011 1,725.9 17.3 56.4 422.2 61.6 14.1 31.3 10.3 10:43 192.1 1.010 1,704.0 17.0 55.8 420.6 61.6 14.0 31.0 10.3 10:44 192.1 1.009 1,717.4 17.1 56.0 422.0 61.6 14.1 31.2 10.4 10:45 192.2 1.009 1,711.2 16.9 56.0 421.1 61.7 14.1 30.9 10.3 10:46 192.2 1.009 1,716.7 17.2 55.9 421.6 61.5 14.1 31.3 10.4 10:47 192.2 1.010 1,730.2 17.3 56.2 423.3 61.4 13.8 31.0 10.3 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.1 1.010 1724.5 17.2 56.0 421.9 61.3 14.0 31.2 10.3 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/24 28 of 99 Run 3 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.43 8.59 Cal Gas Concentration (CMA)11.00 10.99 Pretest System Zero Response 0.01 -0.01 Posttest System Zero Response 0.02 -0.02 Average Zero Response (Co)0.02 -0.02 Pretest System Cal Response 10.91 11.12 Posttest System Cal Response 10.90 11.12 Average Cal Response (CM)10.91 11.12 Corrected Run Average (Corr)10.52 8.49 11:07 10.43 8.58 11:08 10.43 8.59 11:09 10.44 8.59 11:10 10.44 8.60 11:11 10.44 8.60 11:12 10.43 8.59 11:13 10.43 8.60 11:14 10.44 8.60 11:15 10.43 8.61 11:16 10.44 8.60 11:17 10.43 8.61 11:18 10.43 8.60 11:19 10.43 8.62 11:20 10.43 8.62 11:21 10.43 8.60 11:22 10.43 8.59 11:23 10.43 8.61 11:24 10.43 8.60 11:25 10.42 8.61 11:26 10.43 8.60 11:27 10.43 8.59 11:28 10.42 8.59 11:29 10.42 8.60 11:30 10.43 8.61 11:31 10.43 8.61 11:32 10.43 8.60 11:33 10.42 8.59 11:34 10.43 8.60 11:35 10.43 8.59 11:36 10.44 8.59 11:37 10.43 8.60 11:38 10.43 8.58 11:39 10.43 8.58 11:40 10.44 8.59 11:41 10.43 8.59 11:42 10.43 8.60 11:43 10.43 8.58 11:44 10.43 8.58 11:45 10.43 8.58 11:46 10.44 8.57 11:47 10.43 8.60 11:48 10.44 8.58 11:49 10.44 8.57 11:50 10.44 8.56 11:51 10.44 8.58 11:52 10.44 8.57 11:53 10.44 8.56 11:54 10.44 8.57 11:55 10.44 8.57 11:56 10.44 8.56 11:57 10.45 8.56 11:58 10.45 8.56 11:59 10.44 8.56 12:00 10.44 8.56 12:01 10.44 8.58 12:02 10.45 8.56 12:03 10.44 8.57 12:04 10.44 8.55 12:05 10.45 8.56 12:06 10.45 8.57 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/5/24 29 of 99 Run 3 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 11:07 192.1 1.011 1,728.4 17.2 56.2 422.9 61.0 13.0 30.2 10.3 11:08 192.1 1.011 1,726.1 17.3 56.0 422.8 60.8 13.7 31.0 10.4 11:10 192.2 1.008 1,733.8 17.3 56.3 423.7 61.0 13.2 30.5 10.3 11:11 192.2 1.011 1,732.1 17.4 55.9 423.5 60.7 12.9 30.3 10.3 11:12 192.2 1.009 1,728.2 17.1 56.0 422.5 61.1 13.3 30.4 10.3 11:13 192.2 1.008 1,730.9 17.2 56.2 422.4 61.1 13.3 30.5 10.4 11:14 192.2 1.010 1,734.2 17.1 56.1 423.2 61.0 13.3 30.4 10.3 11:15 192.1 1.010 1,728.7 17.0 55.9 421.9 61.1 13.2 30.2 10.4 11:16 192.1 1.010 1,727.7 17.3 56.1 421.9 60.9 13.1 30.4 10.3 11:17 192.0 1.009 1,730.3 17.3 56.2 422.4 61.3 13.5 30.8 10.4 11:18 192.0 1.008 1,727.4 17.2 56.2 422.4 61.1 12.7 30.0 10.3 11:19 192.1 1.009 1,722.9 17.2 56.1 422.3 61.3 13.3 30.6 10.4 11:20 192.1 1.010 1,721.2 17.1 56.0 421.7 61.5 13.0 30.1 10.3 11:21 192.1 1.008 1,733.0 17.4 56.1 423.0 61.3 13.3 30.7 10.4 11:22 192.1 1.010 1,736.3 17.3 56.3 424.5 61.0 13.2 30.6 10.3 11:23 192.1 1.009 1,718.7 17.3 55.7 421.8 60.8 13.0 30.3 10.4 11:24 192.1 1.011 1,726.7 17.2 55.9 422.4 60.6 13.4 30.6 10.3 11:25 192.1 1.010 1,726.7 17.1 56.0 422.7 60.9 12.9 30.1 10.4 11:26 192.1 1.010 1,711.2 16.9 55.5 421.4 60.5 13.3 30.2 10.3 11:27 192.0 1.009 1,725.1 17.2 56.1 422.8 61.0 13.4 30.6 10.4 11:28 192.0 1.008 1,728.1 17.2 56.1 423.2 61.2 13.2 30.4 10.3 11:29 192.1 1.008 1,713.7 17.2 55.9 420.7 61.3 13.1 30.3 10.4 11:30 192.1 1.009 1,716.1 17.3 55.9 422.2 61.2 13.2 30.5 10.4 11:31 192.1 1.010 1,718.6 17.1 55.9 420.2 60.6 13.1 30.2 10.3 11:33 192.2 1.009 1,709.2 16.7 55.8 420.6 61.1 13.1 29.9 10.4 11:34 192.2 1.009 1,726.1 17.0 56.2 423.4 61.3 12.9 30.0 10.3 11:35 192.2 1.009 1,707.3 16.9 55.9 420.1 61.5 12.6 29.5 10.4 11:36 192.2 1.010 1,706.9 17.0 55.8 420.5 61.4 12.6 29.6 10.3 11:37 192.2 1.010 1,693.6 16.6 55.4 418.5 61.5 12.8 29.4 10.4 11:38 192.1 1.009 1,706.3 17.1 55.7 420.0 61.4 12.9 30.1 10.3 11:39 192.1 1.009 1,709.8 16.9 55.7 420.8 61.6 13.4 30.2 10.4 11:40 192.1 1.008 1,710.8 16.8 55.8 420.8 62.0 13.2 30.0 10.3 11:41 192.0 1.011 1,714.3 16.9 55.7 420.1 61.6 12.7 29.7 10.4 11:42 192.0 1.011 1,711.6 17.1 55.6 420.4 61.3 13.0 30.1 10.3 11:43 192.1 1.010 1,709.5 17.0 55.8 420.1 61.6 13.0 30.0 10.4 11:44 192.0 1.010 1,711.9 16.9 55.8 420.9 62.0 12.3 29.2 10.3 11:45 192.0 1.009 1,713.1 17.2 55.8 420.7 61.8 13.1 30.3 10.4 11:46 192.1 1.011 1,706.5 17.0 55.7 419.4 61.8 13.1 30.1 10.3 11:47 192.0 1.009 1,723.9 16.9 55.8 422.2 61.4 13.8 30.7 10.4 11:48 192.0 1.010 1,712.8 16.7 55.7 420.4 61.3 13.0 29.8 10.3 11:49 192.0 1.010 1,714.2 16.9 55.9 420.6 61.8 13.3 30.2 10.4 11:50 192.1 1.010 1,717.2 17.2 56.0 421.0 61.8 12.3 29.5 10.3 11:51 192.1 1.010 1,702.6 16.8 55.8 418.9 62.1 13.3 30.1 10.4 11:52 192.2 1.009 1,722.2 16.9 56.2 421.4 61.9 13.1 30.0 10.3 11:53 192.2 1.008 1,703.0 16.9 55.8 419.3 62.3 13.3 30.2 10.4 11:54 192.2 1.009 1,712.3 16.8 55.7 420.4 61.9 12.6 29.4 10.3 11:56 192.2 1.009 1,715.6 17.0 55.9 421.2 61.8 12.8 29.8 10.4 11:57 192.2 1.009 1,706.8 17.0 55.5 419.8 61.7 12.6 29.6 10.3 11:58 192.2 1.008 1,714.9 17.0 55.5 421.1 61.7 12.8 29.8 10.4 11:59 192.1 1.009 1,721.1 17.1 55.5 421.3 61.8 12.8 29.9 10.3 12:00 192.1 1.009 1,716.2 16.8 55.7 420.9 61.8 13.0 29.9 10.4 12:01 192.1 1.009 1,714.2 16.9 55.6 421.0 61.4 13.3 30.2 10.3 12:02 192.0 1.010 1,725.8 17.1 56.0 422.1 61.6 13.2 30.3 10.3 12:03 192.0 1.008 1,708.2 17.0 55.8 419.4 62.1 12.4 29.4 10.3 12:04 192.0 1.010 1,719.5 17.2 55.7 421.3 61.4 12.6 29.7 10.4 12:05 192.0 1.009 1,713.0 16.9 55.7 420.5 61.3 13.2 30.1 10.3 12:06 192.0 1.010 1,705.3 17.1 55.4 419.9 61.6 12.6 29.7 10.3 12:07 192.0 1.010 1,726.7 17.1 56.0 422.7 61.7 13.1 30.3 10.3 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.1 1.009 1718.2 17.1 55.9 421.4 61.4 13.0 30.1 10.3 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/24 30 of 99 Method 1 Data Location Source Project No. Date Vertical Circular 36.50 in 16.50 in 20.00 in 2.18 ft2 2 1 1.1 ft 0.7 (must be > 0.5) 4.1 ft 2.5 (must be > 2) 16 16 Measurer (Initial and Date):JES 9/3/24 Reviewer (Initial and Date):AJE 9/3/24 2345 6 789101112 1 14.6 -- 6.7 --4.4 -- 3.2 -- 2.6 -- 2.1 1 3.2 0.64 17.14 2 85.4 -- 25.0 -- 14.6 -- 10.5 -- 8.2 -- 6.7 2 10.5 2.10 18.60 3 -- -- 75.0 -- 29.6 -- 19.4 -- 14.6 -- 11.8 3 19.4 3.88 20.38 4 -- -- 93.3 -- 70.4 -- 32.3 -- 22.6 -- 17.7 4 32.3 6.46 22.96 5 -- -- -- -- 85.4 -- 67.7 -- 34.2 -- 25.0 5 67.7 13.54 30.04 6 -- -- -- -- 95.6 -- 80.6 -- 65.8 -- 35.6 6 80.6 16.12 32.62 7 -- -- -- ------ 89.5 -- 77.4 -- 64.4 7 89.5 17.90 34.40 8 -- -- -- ------ 96.8 -- 85.4 -- 75.0 8 96.8 19.36 35.86 9 -- -- -- ------ -- -- 91.8 -- 82.3 9 -- -- -- 10 -- -- -- ------ -- -- 97.4 -- 88.2 10 -- -- -- 11 -- -- -- ------ -- -- -- -- 93.3 11 -- -- -- 12 -- -- -- ------ -- -- -- -- 97.9 12 -- -- -- *Percent of stack diameter from inside wall to traverse point. A = 1.1 ft. B = 4.1 ft. Depth of Duct = 20 in. Number of traverse points on a diameter Stack Diagram Cross Sectional Area LOCATION OF TRAVERSE POINTS Traverse Point % of Diameter Distance from inside wall Distance from outside of port Number of Readings per Point: Distance A: Distance A Duct Diameters: Distance B: Distance B Duct Diameters: Minimum Number of Traverse Points: Actual Number of Traverse Points: CIRCULAR DUCT Cross Sectional Area of Duct: Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 09/03/24 Stack Parameters Duct Orientation: Duct Design: Distance from Far Wall to Outside of Port: Nipple Length: Depth of Duct: No. of Test Ports: Upstream Disturbance Downstream Disturbance B A 31 of 99 Cyclonic Flow Check Location Source Project No. Date Sample Point Angle (ΔP=0) 1 4 2 7 3 3 4 3 5 2 6 4 7 1 8 4 9 6 10 8 11 3 12 2 13 4 14 2 15 3 16 1 Average 3.6 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/24 32 of 99 Field Data Method 2 Data Location Source Project No. Δ P (in. WC) Ts (°F) Δ P (in. WC) Ts (°F) Δ P (in. WC) Ts (°F) 1.41 287 1.37 295 1.45 297 1.34 288 1.44 296 1.41 298 1.37 290 1.41 296 1.26 297 1.36 291 1.34 295 1.25 296 1.42 290 1.31 294 1.43 295 1.28 289 1.27 294 1.32 295 1.25 287 1.29 295 1.35 296 1.31 288 1.33 294 1.37 297 1.43 289 1.42 296 1.34 298 1.37 290 1.28 296 1.41 297 1.42 291 1.40 295 1.42 297 1.36 288 1.34 295 1.24 297 1.35 287 1.29 294 1.26 296 1.33 286 1.31 295 1.33 296 1.30 286 1.28 296 1.29 294 1.18 285 1.22 296 1.25 295 Average Square Root of ΔP, (in. WC)1/2 (ΔP)1/2 1.156 Average ΔP, in. WC (ΔP)1.34 Pitot Tube Coefficient (Cp)0.840 Barometric Pressure, in. Hg (Pb)25.61 Static Pressure, in. WC (Pg)3.57 Stack Pressure, in. Hg (Ps)25.87 Average Temperature, °F (Ts)293.2 Average Temperature, °R (Ts)752.9 Measured Moisture Fraction (BWSmsd)0.103 Moisture Fraction @ Saturation (BWSsat)1.000 Moisture Fraction (BWS)0.103 O2 Concentration, % (O2)10.5 CO2 Concentration, % (CO2)8.5 Molecular Weight, lb/lb-mole (dry) (Md)29.78 Molecular Weight, lb/lb-mole (wet) (Ms)28.57 Velocity, ft/sec (Vs)83.8 VFR at stack conditions, acfm (Qa)10,965 VFR at standard conditions, scfh (Qsw)398,730 VFR at standard conditions, scfm (Qsw)6,645 VFR at standard conditions, dscfm (Qsd)5,961 1.0001.0001.000 0.1030.1030.103 5,993 5,941 5,948 6,681 6,624 6,631 400,883 397,425 397,882 10,954 10,958 10,984 83.7 83.7 83.9 28.57 28.57 28.57 29.78 29.78 29.78 10.54 10.54 10.52 8.49 8.49 8.49 0.103 0.103 0.103 747.9 754.8 756.0 288.3 295.1 296.3 25.87 25.87 25.88 3.50 3.55 3.65 25.61 25.61 25.61 0.840 0.840 0.840 1.34 1.33 1.34 1.158 1.154 1.156 3 4 5 6 7 5 6 7 8 B1 2 Traverse Point A1 2 3 4 Leak Check Pass Pass Pass Stop Time 8:50 10:14 11:26 Start Time 8:36 10:00 11:14 8 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Run No. 1 2 3 Status VALID VALID VALID Date 9/5/24 9/5/24 9/5/24 33 of 99 Jenbacher Engine #3 34 of 99 Emissions Calculations Location Source Project No. Run Number Run 1 Run 2 Run 3 Average Date 9/5/24 9/6/24 9/6/24 -- Start Time 14:50 8:20 9:45 -- Stop Time 15:49 9:19 10:44 -- Engine Manufacturer Engine Model Engine Serial Number Engine Type Engine Date of Manufacturer DOM Engine Hour Meter Reading EMR Generator Output, Hz Gen OP 60 60 60 60 Engine Speed, RPM ES 1,500 1,500 1,500 1,500 Engine Brake Work, HP EBW 2,280 2,280 2,279 2,279 Maximum Brake Work, HP MaxEBW 2,509 2,509 2,509 2,509 Engine Load, % EL 94949494 Ambient Temperature TAmb 86 66 77 76 Relative Humidity, %RH 18 38 31 29 Barometric Pressure, in. Hg Pb 25.61 25.60 25.60 25.60 Moisture Fraction, dimensionless BWS 0.103 0.105 0.105 0.104 Volumetric Flow Rate (M1-4), dscfm Qs 5,839 5,693 5,888 5,807 O₂ Concentration, % dry CO₂10.71 10.42 10.43 10.52 CO₂ Concentration, % dry CCO₂8.14 8.85 8.83 8.61 Methane - Outlet Concentration, ppmvd CCH₄1855.62 2035.82 2049.87 1980.44 Methane - Outlet Concentration, ppmvw CCH₄w 1664.69 1821.77 1834.89 1773.79 Methane - Outlet Concentration, ppmvd @ 15 % O₂C<CH₄c15> 1074.58 1145.75 1154.65 1125.00 Methane - Outlet Emission Rate, lb/hr ER<CH₄> 27.1 29.0 30.2 28.7 Methane - Outlet Emission Rate, ton/yr ER<CH₄TPY> 118.6 126.9 132.1 125.9 Methane - Outlet Emission Factor, g/HP-hr EF<CH₄> 5.4 5.8 6.0 5.7 Ethane - Outlet Concentration, ppmvd CC₂H₆22.58 13.03 13.26 16.29 Ethane - Outlet Concentration, ppmvw CC₂H₆w 20.26 11.66 11.87 14.60 Ethane - Outlet Concentration, ppmvd @ 15 % O₂C<C₂H₆c15> 13.08 7.33 7.47 9.29 Ethane - Outlet Emission Rate, lb/hr ER<C₂H₆> 0.62 0.35 0.37 0.44 Ethane - Outlet Emission Rate, ton/yr ER<C₂H₆TPY> 2.7 1.5 1.6 1.9 Ethane - Outlet Emission Factor, g/HP-hr EF<C₂H₆> 0.12 0.069 0.073 0.088 Formaldehyde - Outlet Concentration, ppmvd CCHOH 51.95 55.98 56.45 54.79 Formaldehyde - Outlet Concentration, ppmvw CCHOHw 46.60 50.09 50.53 49.08 Formaldehyde - Outlet Concentration, ppmvd @ 15 % O₂C<CHOHc15> 30.08 31.51 31.80 31.13 Formaldehyde - Outlet Emission Rate, lb/hr ER<CHOH> 1.4 1.5 1.6 1.5 Formaldehyde - Outlet Emission Rate, ton/yr ER<CHOHTPY>6.2 6.5 6.8 6.5 Formaldehyde - Outlet Emission Factor, g/HP-hr EF<CHOH> 0.28 0.30 0.31 0.30 CO - Outlet Concentration, ppmvd CCO 469.90 488.32 491.39 483.20 CO - Outlet Concentration, ppmvw CCOw 421.55 436.98 439.86 432.80 CO - Outlet Concentration, ppmvd @ 15 % O₂CCOc15 272.12 274.82 276.79 274.58 CO - Outlet Emission Rate, lb/hr ERCO 12.0 12.1 12.6 12.2 CO - Outlet Emission Rate, ton/yr ERCOTPY 52.5 53.1 55.3 53.6 CO - Outlet Emission Factor, g/HP-hr EFCO 2.4 2.4 2.5 2.4 NOx - Outlet Concentration, ppmvd CNOx 56.08 54.73 54.77 55.19 NOx - Outlet Concentration, ppmvd @ 15 % O₂CNOxc15 32.48 30.80 30.85 31.38 NOx - Outlet Emission Rate, lb/hr ERNOx 2.3 2.2 2.3 2.3 NOx - Outlet Emission Rate, ton/yr ERNOxTPY 10.3 9.8 10.1 10.1 NOx - Outlet Emission Factor, g/HP-hr EFNOx 0.47 0.44 0.46 0.46 VOC - Outlet Concentration, ppmvd CVOC 14.29 13.45 12.38 13.37 VOC - Outlet Concentration, ppmvd @ 15 % O₂CVOCc15 8.27 7.57 6.97 7.61 VOC - Outlet Emission Rate, lb/hr ERVOC 0.57 0.53 0.50 0.53 VOC - Outlet Emission Rate, ton/yr ERVOCTPY 2.5 2.3 2.2 2.3 VOC - Outlet Emission Factor, g/HP-hr EFVOC 0.11 0.10 0.10 0.11 NMHC - Outlet Concentration, ppmvd CNMHC 36.87 26.47 25.64 29.66 NMHC - Outlet Concentration, ppmvd @ 15 % O₂CNMHCc15 21.35 14.90 14.44 16.90 NMHC - Outlet Emission Rate, lb/hr ERNMHC 1.5 1.0 1.0 1.2 NMHC - Outlet Emission Rate, ton/yr ERNMHCTPY 6.5 4.5 4.5 5.2 NMHC - Outlet Emission Factor, g/HP-hr EFNMHC 0.29 0.21 0.21 0.24 *VOC excludes Formaldehyde, methane, and ethane. NMHC value adds ethane back to VOC. Engine Data 17,190 Input Data - Outlet Calculated Data - Outlet Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 GE Jenbacher JMS 612-F28F02 1322432 Spark Ignition - 4SLB 1/1/2018 35 of 99 Run 1 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.61 8.29 Cal Gas Concentration (CMA)11.00 10.90 Pretest System Zero Response 0.02 -0.02 Posttest System Zero Response 0.01 -0.02 Average Zero Response (Co)0.02 -0.02 Pretest System Cal Response 10.90 11.12 Posttest System Cal Response 10.88 11.09 Average Cal Response (CM)10.89 11.11 Corrected Run Average (Corr)10.71 8.14 14:50 10.62 8.30 14:51 10.62 8.29 14:52 10.62 8.28 14:53 10.63 8.28 14:54 10.63 8.28 14:55 10.65 8.27 14:56 10.65 8.27 14:57 10.65 8.26 14:58 10.64 8.28 14:59 10.66 8.26 15:00 10.64 8.27 15:01 10.63 8.28 15:02 10.63 8.28 15:03 10.63 8.28 15:04 10.63 8.28 15:05 10.61 8.30 15:06 10.63 8.28 15:07 10.62 8.29 15:08 10.61 8.29 15:09 10.62 8.28 15:10 10.62 8.28 15:11 10.62 8.27 15:12 10.60 8.31 15:13 10.60 8.29 15:14 10.60 8.29 15:15 10.60 8.30 15:16 10.59 8.30 15:17 10.59 8.29 15:18 10.59 8.29 15:19 10.59 8.29 15:20 10.59 8.29 15:21 10.58 8.30 15:22 10.57 8.30 15:23 10.59 8.30 15:24 10.58 8.28 15:25 10.59 8.30 15:26 10.59 8.30 15:27 10.58 8.29 15:28 10.58 8.30 15:29 10.59 8.29 15:30 10.60 8.29 15:31 10.60 8.28 15:32 10.59 8.28 15:33 10.60 8.29 15:34 10.59 8.29 15:35 10.59 8.30 15:36 10.62 8.28 15:37 10.59 8.29 15:38 10.61 8.28 15:39 10.59 8.28 15:40 10.59 8.30 15:41 10.58 8.30 15:42 10.59 8.29 15:43 10.58 8.30 15:44 10.60 8.28 15:45 10.59 8.30 15:46 10.58 8.30 15:47 10.58 8.30 15:48 10.59 8.31 15:49 10.58 8.30 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/24 36 of 99 Run 1 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 14:49 192.1 1.006 1,653.8 20.2 46.5 419.6 57.4 13.8 34.0 10.3 14:51 192.1 1.008 1,616.5 19.6 45.9 413.7 57.5 14.0 33.6 10.3 14:52 192.0 1.009 1,643.8 20.2 46.1 418.2 56.6 13.7 33.9 10.2 14:53 192.0 1.007 1,665.0 20.3 46.7 422.7 56.4 14.7 35.0 10.3 14:54 192.1 1.008 1,687.0 20.5 46.7 423.9 55.3 14.2 34.7 10.2 14:55 192.1 1.008 1,681.4 20.4 46.6 422.8 55.6 14.5 34.9 10.2 14:56 192.1 1.010 1,691.3 20.7 46.9 426.2 54.5 14.2 35.0 10.2 14:57 192.1 1.009 1,703.9 20.9 47.1 428.5 53.5 14.1 35.0 10.2 14:58 192.1 1.008 1,710.6 21.0 47.2 429.2 53.8 14.2 35.2 10.2 14:59 192.1 1.008 1,705.6 20.9 46.9 427.9 53.6 14.6 35.5 10.2 15:00 192.1 1.008 1,695.8 20.7 46.8 427.3 54.0 14.5 35.2 10.2 15:01 192.1 1.009 1,706.0 21.1 46.9 428.2 53.8 15.1 36.2 10.2 15:02 192.1 1.007 1,713.4 20.8 47.2 428.3 54.6 14.6 35.4 10.2 15:03 192.1 1.006 1,669.2 20.4 46.5 423.5 54.8 14.7 35.0 10.2 15:04 192.1 1.007 1,692.9 20.5 46.9 425.3 54.5 14.4 35.0 10.2 15:05 192.1 1.007 1,675.2 20.4 46.7 423.3 55.9 14.1 34.4 10.2 15:06 192.1 1.007 1,654.2 20.0 46.4 421.3 56.3 14.2 34.2 10.2 15:07 192.1 1.007 1,673.7 20.2 46.8 423.9 55.4 14.2 34.4 10.3 15:08 192.1 1.007 1,664.6 20.4 46.5 421.9 55.6 14.3 34.7 10.3 15:09 192.1 1.009 1,662.9 20.5 46.6 422.8 55.7 13.9 34.4 10.3 15:10 192.1 1.006 1,688.4 20.7 47.0 425.2 55.4 14.8 35.5 10.3 15:11 192.1 1.007 1,658.1 20.3 46.5 422.5 55.7 14.7 35.0 10.3 15:12 192.1 1.007 1,682.1 20.6 46.8 423.6 55.7 14.6 35.2 10.3 15:14 192.1 1.007 1,683.6 20.5 47.1 423.7 56.0 14.6 35.1 10.3 15:15 192.1 1.007 1,664.8 20.1 46.7 421.4 56.9 14.1 34.2 10.3 15:16 192.1 1.007 1,659.6 20.1 46.7 420.3 57.1 14.5 34.7 10.3 15:17 192.1 1.006 1,659.5 20.3 46.6 419.6 57.2 14.3 34.5 10.3 15:18 192.1 1.008 1,625.1 19.7 46.1 414.3 57.6 14.0 33.7 10.3 15:19 192.1 1.008 1,642.4 20.0 46.4 417.0 57.2 13.8 33.8 10.4 15:20 192.1 1.008 1,621.9 19.9 46.0 413.6 57.7 14.0 33.8 10.3 15:21 192.1 1.006 1,615.0 19.6 46.0 412.9 57.9 13.9 33.6 10.3 15:22 192.1 1.008 1,621.6 19.6 46.0 415.2 57.2 14.6 34.2 10.3 15:23 192.1 1.008 1,611.2 19.5 45.9 412.9 58.1 14.2 33.7 10.3 15:24 192.1 1.007 1,642.3 19.8 46.4 417.3 57.3 14.7 34.5 10.3 15:25 192.1 1.007 1,647.9 19.8 46.5 419.3 57.0 14.3 34.1 10.3 15:26 192.1 1.009 1,630.6 19.7 46.1 415.4 57.6 14.0 33.7 10.3 15:27 192.0 1.007 1,652.8 20.0 46.6 419.2 56.9 14.5 34.5 10.3 15:28 192.1 1.009 1,637.1 19.9 46.2 417.5 56.7 14.1 33.9 10.3 15:29 192.1 1.008 1,626.1 19.6 46.1 416.6 57.1 14.2 33.7 10.3 15:30 192.1 1.006 1,654.4 19.9 46.6 421.7 56.6 14.6 34.6 10.3 15:31 192.0 1.007 1,665.0 20.1 46.7 422.4 56.3 14.7 34.8 10.3 15:32 192.1 1.009 1,670.2 20.3 46.6 422.8 55.8 14.2 34.5 10.3 15:33 192.1 1.008 1,661.9 20.0 46.6 420.2 56.7 14.6 34.6 10.3 15:34 192.1 1.007 1,661.9 20.3 46.6 422.8 55.6 14.6 34.8 10.3 15:35 192.1 1.006 1,648.6 20.1 46.5 421.2 56.0 14.2 34.4 10.3 15:37 192.0 1.007 1,674.2 20.4 46.7 422.9 55.6 13.7 34.2 10.4 15:38 192.0 1.007 1,730.6 21.2 47.5 432.1 54.1 14.3 35.4 10.3 15:39 192.0 1.008 1,692.0 20.7 46.9 424.5 55.2 14.2 34.9 10.4 15:40 192.0 1.008 1,681.2 20.6 46.7 425.5 54.8 14.0 34.5 10.3 15:41 192.0 1.008 1,670.2 20.4 46.8 422.2 56.0 14.1 34.4 10.3 15:42 192.0 1.007 1,671.7 20.5 46.7 421.1 56.2 13.9 34.3 10.4 15:43 192.0 1.007 1,657.8 20.1 46.6 421.3 56.2 14.3 34.4 10.3 15:44 192.0 1.009 1,655.8 20.1 46.4 419.2 56.8 14.0 34.0 10.3 15:45 192.0 1.008 1,648.0 20.0 46.2 418.1 56.8 14.5 34.6 10.3 15:46 192.0 1.008 1,678.5 20.5 46.9 422.6 56.3 14.0 34.5 10.3 15:47 192.0 1.006 1,679.6 20.4 46.9 423.5 56.6 14.0 34.4 10.4 15:48 192.0 1.006 1,656.3 20.1 46.7 420.8 57.0 14.3 34.4 10.3 15:49 192.0 1.008 1,672.0 20.2 46.9 421.7 56.8 14.6 34.8 10.3 15:50 192.0 1.007 1,650.1 20.0 46.5 419.0 57.0 14.2 10.3 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.1 1.007 1664.7 20.3 46.6 421.6 56.1 14.3 34.6 10.3 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/24 37 of 99 Run 2 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.34 9.03 Cal Gas Concentration (CMA)11.00 10.90 Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.02 0.00 Average Zero Response (Co)0.02 0.00 Pretest System Cal Response 10.91 11.11 Posttest System Cal Response 10.93 11.13 Average Cal Response (CM)10.92 11.12 Corrected Run Average (Corr)10.42 8.85 8:20 10.37 8.98 8:21 10.37 8.98 8:22 10.37 8.98 8:23 10.39 8.96 8:24 10.40 8.98 8:25 10.42 8.95 8:26 10.44 8.96 8:27 10.45 8.94 8:28 10.46 8.92 8:29 10.45 8.94 8:30 10.46 8.94 8:31 10.43 8.97 8:32 10.42 8.96 8:33 10.41 8.97 8:34 10.39 8.99 8:35 10.42 8.97 8:36 10.41 9.00 8:37 10.39 9.00 8:38 10.31 9.06 8:39 10.31 9.07 8:40 10.32 9.05 8:41 10.33 9.06 8:42 10.35 9.05 8:43 10.36 9.05 8:44 10.35 9.05 8:45 10.33 9.07 8:46 10.34 9.07 8:47 10.34 9.07 8:48 10.33 9.08 8:49 10.34 9.06 8:50 10.32 9.08 8:51 10.33 9.06 8:52 10.31 9.08 8:53 10.33 9.06 8:54 10.32 9.07 8:55 10.29 9.08 8:56 10.27 9.10 8:57 10.27 9.10 8:58 10.25 9.11 8:59 10.26 9.09 9:00 10.29 9.07 9:01 10.27 9.07 9:02 10.26 9.09 9:03 10.24 9.09 9:04 10.22 9.10 9:05 10.30 9.04 9:06 10.29 9.04 9:07 10.30 9.05 9:08 10.27 9.07 9:09 10.30 9.03 9:10 10.31 9.02 9:11 10.30 9.03 9:12 10.34 9.01 9:13 10.34 9.01 9:14 10.33 9.01 9:15 10.33 8.99 9:16 10.33 8.99 9:17 10.35 8.99 9:18 10.36 8.98 9:19 10.36 8.99 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/6/24 38 of 99 Run 2 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 8:20 192.1 1.013 1,847.7 11.9 50.2 441.0 54.0 13.3 25.2 10.5 8:21 192.1 1.016 1,824.2 11.9 49.8 438.0 54.1 13.3 25.2 10.5 8:22 192.1 1.015 1,826.3 11.8 50.0 437.4 54.3 12.9 24.7 10.5 8:23 192.0 1.014 1,837.1 11.9 50.1 439.8 54.2 13.6 25.6 10.5 8:24 192.1 1.015 1,850.5 11.9 50.4 442.0 54.1 13.1 25.0 10.5 8:25 192.1 1.015 1,880.8 12.2 50.5 446.7 53.0 13.7 25.9 10.5 8:26 192.1 1.015 1,893.0 12.4 50.9 449.8 51.2 13.8 26.2 10.5 8:27 192.1 1.016 1,915.6 12.4 50.7 453.5 50.4 13.9 26.3 10.4 8:28 192.1 1.015 1,958.5 12.8 51.1 458.9 49.3 14.0 26.8 10.4 8:29 192.2 1.016 1,971.7 12.7 51.4 458.3 49.1 14.2 26.9 10.4 8:30 192.1 1.016 1,991.3 13.1 51.7 464.3 48.7 14.4 27.5 10.4 8:31 192.1 1.016 1,983.7 13.1 51.4 461.1 48.8 14.0 27.1 10.4 8:32 192.1 1.014 1,937.2 12.7 50.9 454.3 50.1 13.5 26.2 10.5 8:33 192.1 1.014 1,958.0 13.0 51.4 457.6 50.5 14.2 27.1 10.5 8:35 192.1 1.017 1,926.7 12.5 51.0 452.5 50.7 14.1 26.6 10.4 8:36 192.1 1.015 1,923.9 12.4 51.0 451.8 51.1 14.0 26.4 10.5 8:37 192.1 1.015 1,974.0 12.7 51.5 459.7 49.3 14.0 26.7 10.4 8:38 192.1 1.015 1,934.4 12.5 51.1 453.3 50.7 14.6 27.1 10.5 8:39 192.1 1.015 1,872.7 12.1 50.7 445.6 52.3 13.8 25.9 10.5 8:40 192.1 1.014 1,823.7 12.0 50.4 437.9 55.0 13.5 25.5 10.6 8:41 192.1 1.013 1,824.2 11.7 50.3 435.3 55.4 13.6 25.3 10.6 8:42 192.1 1.015 1,841.8 11.8 50.4 440.0 54.9 13.6 25.5 10.5 8:43 192.1 1.016 1,856.8 11.9 50.5 441.1 53.7 13.2 25.1 10.5 8:44 192.1 1.016 1,851.6 12.1 50.5 440.9 53.5 13.4 25.5 10.5 8:45 192.1 1.014 1,873.7 12.4 50.7 446.5 52.2 13.7 26.0 10.5 8:46 192.1 1.015 1,829.1 12.1 50.3 437.8 54.5 13.6 25.7 10.6 8:47 192.1 1.015 1,860.6 12.0 50.6 442.2 54.0 13.3 25.3 10.5 8:48 192.1 1.016 1,843.3 12.0 50.3 439.7 53.5 13.1 25.1 10.5 8:49 192.1 1.014 1,846.6 12.1 50.4 441.8 53.5 13.2 25.2 10.6 8:50 192.2 1.015 1,847.2 11.9 50.5 442.0 53.5 13.6 25.5 10.5 8:51 192.1 1.016 1,848.6 12.0 50.4 440.0 53.9 13.3 25.3 10.5 8:52 192.1 1.014 1,826.0 11.8 50.5 436.8 54.3 13.7 25.5 10.5 8:53 192.1 1.015 1,811.3 11.7 50.1 437.5 54.8 13.9 25.5 10.6 8:54 192.1 1.015 1,841.0 12.0 50.5 438.1 54.6 13.3 25.3 10.6 8:55 192.1 1.014 1,836.0 11.6 50.5 438.4 54.9 13.5 25.1 10.6 8:56 192.1 1.016 1,783.3 11.3 50.0 431.2 56.1 13.4 24.7 10.6 8:58 192.1 1.015 1,755.4 10.9 49.8 428.1 57.2 13.6 24.5 10.6 8:59 192.1 1.015 1,735.1 10.8 49.5 424.0 57.6 13.4 24.1 10.6 9:00 192.1 1.014 1,706.6 10.7 49.0 419.1 58.7 12.9 23.6 10.6 9:01 192.1 1.014 1,725.5 10.7 49.2 422.1 58.0 13.3 24.0 10.6 9:02 192.1 1.015 1,761.9 10.9 49.6 427.0 56.7 12.9 23.8 10.6 9:03 192.1 1.015 1,747.0 10.9 49.4 424.1 57.8 13.4 24.3 10.6 9:04 192.1 1.016 1,708.5 10.5 49.2 419.6 58.9 13.2 23.7 10.6 9:05 192.1 1.015 1,699.1 10.5 49.1 418.3 59.7 13.3 23.8 10.6 9:06 192.1 1.015 1,685.5 10.5 48.9 417.3 59.6 12.8 23.3 10.6 9:07 192.1 1.013 1,759.5 11.0 49.6 427.3 56.9 13.4 24.4 10.6 9:08 192.1 1.014 1,758.0 11.0 49.6 427.1 57.3 12.9 24.0 10.6 9:09 192.1 1.014 1,714.0 10.7 49.0 419.6 58.9 12.9 23.5 10.6 9:10 192.1 1.015 1,695.9 10.6 48.9 418.5 59.6 12.6 23.1 10.6 9:11 192.1 1.016 1,726.8 10.8 49.1 423.0 57.9 13.0 23.8 10.5 9:12 192.1 1.015 1,715.0 10.9 49.0 421.2 58.8 12.9 23.7 10.5 9:13 192.1 1.015 1,734.2 11.1 49.1 424.5 57.3 12.8 23.9 10.5 9:14 192.0 1.014 1,754.8 11.1 49.2 427.0 57.2 13.1 24.2 10.5 9:15 192.0 1.015 1,732.4 10.8 49.1 423.1 58.4 13.1 23.9 10.5 9:16 192.0 1.013 1,712.3 10.6 48.8 419.4 58.4 13.0 23.6 10.5 9:17 192.0 1.018 1,728.0 10.7 48.8 421.9 58.0 13.5 24.2 10.4 9:18 192.0 1.014 1,771.8 11.0 49.5 428.9 57.0 13.4 24.4 10.5 9:19 192.0 1.014 1,783.5 11.3 49.7 431.0 56.7 13.4 24.7 10.5 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.1 1.015 1821.8 11.7 50.1 437.0 54.7 13.4 25.1 10.5 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/24 39 of 99 Run 3 - RM Data Location: Source: Project No.: Date: Time O₂ - Outlet CO₂ - Outlet Unit % dry % dry Status Valid Valid Uncorrected Run Average (Cobs)10.36 9.02 Cal Gas Concentration (CMA)11.00 10.90 Pretest System Zero Response 0.02 0.00 Posttest System Zero Response 0.02 0.00 Average Zero Response (Co)0.02 0.00 Pretest System Cal Response 10.93 11.13 Posttest System Cal Response 10.93 11.14 Average Cal Response (CM)10.93 11.14 Corrected Run Average (Corr)10.43 8.83 9:45 10.37 9.00 9:46 10.39 9.00 9:47 10.39 9.02 9:48 10.40 9.01 9:49 10.40 8.99 9:50 10.40 9.00 9:51 10.40 9.00 9:52 10.41 9.00 9:53 10.40 9.01 9:54 10.39 9.01 9:55 10.37 9.01 9:56 10.36 9.02 9:57 10.35 9.03 9:58 10.35 9.02 9:59 10.34 9.03 10:00 10.34 9.03 10:01 10.32 9.04 10:02 10.32 9.04 10:03 10.32 9.05 10:04 10.31 9.05 10:05 10.32 9.05 10:06 10.32 9.04 10:07 10.31 9.04 10:08 10.31 9.05 10:09 10.32 9.04 10:10 10.33 9.04 10:11 10.33 9.04 10:12 10.34 9.04 10:13 10.35 9.05 10:14 10.35 9.03 10:15 10.36 9.04 10:16 10.36 9.03 10:17 10.37 9.02 10:18 10.37 9.02 10:19 10.35 9.02 10:20 10.36 9.02 10:21 10.37 9.02 10:22 10.38 9.02 10:23 10.38 9.01 10:24 10.38 9.01 10:25 10.39 9.00 10:26 10.37 9.03 10:27 10.37 9.01 10:28 10.38 9.01 10:29 10.38 9.01 10:30 10.38 9.02 10:31 10.36 9.02 10:32 10.37 9.01 10:33 10.37 9.02 10:34 10.38 9.01 10:35 10.39 9.01 10:36 10.37 9.01 10:37 10.38 9.00 10:38 10.36 9.02 10:39 10.34 9.03 10:40 10.35 9.02 10:41 10.35 9.02 10:42 10.35 9.02 10:43 10.34 9.02 10:44 10.35 9.02 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/6/24 40 of 99 Run 3 - FTIR Data Location: Source: Project No.: Date: Time Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Unit ° C atm ppmvw ppmvw ppmvw ppmvw ppmvd ppmvd ppmvd % (wet) MDL ----0.69 0.15 0.09 0.1 0.36 ------ Status Valid Valid Valid Valid Valid Valid Valid Valid Valid Valid 9:45 191.0 1.000 1,871.1 12.1 50.9 446.2 52.5 12.4 24.5 10.5 9:46 192.0 1.016 1,902.7 12.4 51.3 450.2 52.0 13.2 25.7 10.5 9:47 192.0 1.015 1,899.4 12.5 51.1 449.0 52.3 13.2 25.7 10.5 9:48 192.1 1.015 1,925.2 12.5 51.4 452.6 51.7 12.4 24.9 10.5 9:49 192.1 1.016 1,906.6 12.3 51.2 451.3 51.7 12.7 25.0 10.5 9:50 192.1 1.015 1,916.5 12.5 51.3 453.4 50.8 12.8 25.3 10.5 9:51 192.1 1.016 1,940.2 12.6 51.5 454.2 51.0 12.7 25.3 10.5 9:52 192.1 1.017 1,938.5 12.6 51.6 454.4 51.0 12.5 25.0 10.5 9:53 192.1 1.015 1,960.8 12.8 51.9 458.8 50.6 13.0 25.7 10.5 9:54 192.0 1.015 1,949.9 12.5 51.8 456.4 50.9 12.7 25.2 10.5 9:55 192.0 1.015 1,928.3 12.7 51.7 454.8 51.7 12.5 25.2 10.5 9:56 192.0 1.014 1,897.2 12.3 51.2 450.2 51.9 12.8 25.2 10.5 9:57 192.0 1.015 1,881.8 12.1 50.9 447.2 53.6 12.6 24.7 10.5 9:58 191.9 1.016 1,869.7 12.0 51.0 445.9 53.4 12.6 24.6 10.5 9:59 192.0 1.016 1,861.4 12.0 50.9 443.5 54.1 12.7 24.7 10.5 10:00 192.0 1.015 1,833.7 11.6 50.7 439.3 55.0 12.6 24.1 10.5 10:01 192.0 1.015 1,837.6 11.7 50.8 438.9 55.2 12.3 23.9 10.5 10:02 192.0 1.015 1,799.2 11.5 50.5 434.6 56.2 12.5 24.0 10.6 10:03 192.1 1.015 1,769.9 11.4 50.0 430.8 56.5 11.7 23.1 10.6 10:05 192.1 1.014 1,793.7 11.6 50.4 434.9 56.1 12.1 23.7 10.6 10:06 192.1 1.015 1,753.7 11.2 49.9 429.3 56.6 12.2 23.4 10.6 10:07 192.2 1.014 1,786.3 11.6 50.2 432.8 56.7 11.8 23.4 10.5 10:08 192.1 1.017 1,790.2 11.6 50.4 434.0 56.6 12.1 23.7 10.6 10:09 192.1 1.014 1,769.9 11.5 50.1 430.2 57.3 11.7 23.2 10.6 10:10 192.0 1.015 1,790.7 11.5 50.4 433.0 57.3 12.4 23.9 10.5 10:11 192.0 1.015 1,797.3 11.6 50.2 434.4 56.5 12.4 24.0 10.5 10:12 192.0 1.015 1,777.1 11.3 50.1 431.4 56.8 12.2 23.5 10.5 10:13 192.0 1.015 1,756.9 11.4 49.6 429.7 56.6 11.7 23.1 10.5 10:14 191.9 1.015 1,801.9 11.7 50.3 433.9 56.0 11.9 23.6 10.5 10:15 192.0 1.016 1,800.5 11.7 50.2 433.7 56.3 12.1 23.8 10.5 10:16 192.0 1.016 1,827.6 12.0 50.7 438.1 55.6 12.1 24.1 10.5 10:17 192.0 1.014 1,826.1 11.9 50.4 438.5 55.0 12.5 24.4 10.5 10:18 192.0 1.017 1,829.2 11.8 50.4 440.2 54.5 12.2 24.0 10.5 10:19 192.1 1.016 1,828.6 11.7 50.3 439.4 54.5 12.6 24.3 10.4 10:20 192.1 1.016 1,798.3 11.6 49.8 434.3 55.6 12.5 24.1 10.5 10:21 192.1 1.014 1,800.5 11.7 49.9 435.1 55.9 12.5 24.1 10.5 10:22 192.1 1.014 1,814.9 11.7 50.1 437.4 55.2 12.2 23.9 10.4 10:23 192.1 1.015 1,837.0 11.8 50.3 439.2 54.6 12.6 24.3 10.4 10:24 192.0 1.015 1,861.5 12.0 50.7 442.0 54.3 12.8 24.8 10.4 10:25 192.0 1.015 1,840.3 12.0 50.7 440.9 54.9 12.1 24.1 10.4 10:26 192.0 1.014 1,859.0 12.2 50.8 444.0 54.4 12.6 24.9 10.4 10:28 192.0 1.014 1,823.6 11.8 50.3 438.2 55.2 12.7 24.6 10.4 10:29 191.9 1.016 1,820.8 11.9 50.1 436.6 54.7 12.2 24.1 10.4 10:30 191.9 1.015 1,843.1 12.0 50.5 440.4 55.0 13.2 25.2 10.4 10:31 191.9 1.015 1,852.9 11.9 50.6 441.0 54.5 12.2 24.1 10.4 10:32 191.9 1.015 1,821.4 12.0 50.2 437.7 55.2 12.5 24.6 10.4 10:33 192.0 1.014 1,811.3 11.7 50.1 435.4 55.6 12.3 24.0 10.4 10:34 192.0 1.013 1,812.6 11.7 50.3 437.8 55.7 12.4 24.1 10.4 10:35 192.1 1.014 1,835.2 11.8 50.4 439.2 55.2 12.2 24.0 10.5 10:36 192.1 1.014 1,831.1 12.0 50.4 439.3 55.2 12.0 23.9 10.5 10:37 192.1 1.013 1,847.3 12.1 50.6 441.3 55.0 12.3 24.4 10.4 10:38 192.1 1.015 1,844.8 12.0 50.7 441.2 55.3 12.6 24.6 10.4 10:39 192.1 1.014 1,803.5 11.8 50.1 434.5 55.5 12.3 24.1 10.5 10:40 192.1 1.014 1,787.1 11.5 50.0 432.2 56.2 12.5 23.9 10.4 10:41 192.0 1.016 1,790.7 11.5 50.0 432.7 56.3 11.9 23.4 10.5 10:42 192.0 1.014 1,786.8 11.4 49.9 432.3 56.6 12.3 23.8 10.4 10:43 192.0 1.014 1,781.1 11.5 49.8 432.3 56.8 12.0 23.5 10.5 10:44 191.9 1.014 1,758.5 11.3 49.8 429.3 57.3 11.7 23.0 10.5 10:45 191.9 1.013 1,775.8 11.5 49.9 432.2 56.7 12.0 23.6 10.5 191.9 1.015 Parameter Temperature Pressure Methane - Outlet Ethane - Outlet Formaldehyde - Outlet CO - Outlet NOx - Outlet VOC - Outlet NMHC - Outlet BWS - Outlet Run Average 192.0 1.015 1834.9 11.9 50.5 439.9 54.8 12.4 24.3 10.5 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/24 41 of 99 Method 1 Data Location Source Project No. Date Vertical Circular 36.50 in 16.50 in 20.00 in 2.18 ft2 2 1 1.1 ft 0.7 (must be > 0.5) 4.1 ft 2.5 (must be > 2) 16 16 Measurer (Initial and Date):JES 9/5/24 Reviewer (Initial and Date):AJE 9/5/24 2345 6 789101112 1 14.6 -- 6.7 --4.4 -- 3.2 -- 2.6 -- 2.1 1 3.2 0.64 17.14 2 85.4 -- 25.0 -- 14.6 -- 10.5 -- 8.2 -- 6.7 2 10.5 2.10 18.60 3 -- -- 75.0 -- 29.6 -- 19.4 -- 14.6 -- 11.8 3 19.4 3.88 20.38 4 -- -- 93.3 -- 70.4 -- 32.3 -- 22.6 -- 17.7 4 32.3 6.46 22.96 5 -- -- -- -- 85.4 -- 67.7 -- 34.2 -- 25.0 5 67.7 13.54 30.04 6 -- -- -- -- 95.6 -- 80.6 -- 65.8 -- 35.6 6 80.6 16.12 32.62 7 -- -- -- ------ 89.5 -- 77.4 -- 64.4 7 89.5 17.90 34.40 8 -- -- -- ------ 96.8 -- 85.4 -- 75.0 8 96.8 19.36 35.86 9 -- -- -- ------ -- -- 91.8 -- 82.3 9 -- -- -- 10 -- -- -- ------ -- -- 97.4 -- 88.2 10 -- -- -- 11 -- -- -- ------ -- -- -- -- 93.3 11 -- -- -- 12 -- -- -- ------ -- -- -- -- 97.9 12 -- -- -- *Percent of stack diameter from inside wall to traverse point. A = 1.1 ft. B = 4.1 ft. Depth of Duct = 20 in. Number of traverse points on a diameter Stack Diagram Cross Sectional Area LOCATION OF TRAVERSE POINTS Traverse Point % of Diameter Distance from inside wall Distance from outside of port Number of Readings per Point: Distance A: Distance A Duct Diameters: Distance B: Distance B Duct Diameters: Minimum Number of Traverse Points: Actual Number of Traverse Points: CIRCULAR DUCT Cross Sectional Area of Duct: Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 09/05/24 Stack Parameters Duct Orientation: Duct Design: Distance from Far Wall to Outside of Port: Nipple Length: Depth of Duct: No. of Test Ports: Upstream Disturbance Downstream Disturbance B A 42 of 99 Cyclonic Flow Check Location Source Project No. Date Sample Point Angle (ΔP=0) 1 2 2 4 3 6 4 3 5 2 6 1 7 1 8 5 9 4 10 3 11 2 12 5 13 4 14 2 15 4 16 6 Average 3.4 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/24 43 of 99 Field Data Method 2 Data Location Source Project No. Δ P (in. WC) Ts (°F) Δ P (in. WC) Ts (°F) Δ P (in. WC) Ts (°F) 1.02 281 1.11 288 1.14 282 1.16 283 1.08 287 1.17 282 1.18 284 1.05 286 1.22 283 1.25 285 1.22 286 1.18 285 1.31 285 1.23 285 1.24 284 1.41 284 1.25 284 1.27 284 1.33 284 1.44 285 1.41 285 1.35 284 1.41 287 1.45 284 0.98 283 1.11 286 1.32 283 1.15 283 1.23 286 1.32 284 1.19 284 1.24 286 1.41 285 1.34 285 1.20 285 1.32 285 1.39 285 1.16 285 1.26 284 1.44 286 1.25 284 1.24 283 1.36 286 1.28 283 1.34 283 1.40 287 1.31 382 1.40 282 Average Square Root of ΔP, (in. WC)1/2 (ΔP)1/2 1.122 Average ΔP, in. WC (ΔP)1.26 Pitot Tube Coefficient (Cp)0.840 Barometric Pressure, in. Hg (Pb)25.61 Static Pressure, in. WC (Pg)4.10 Stack Pressure, in. Hg (Ps)25.91 Average Temperature, °F (Ts)286.5 Average Temperature, °R (Ts)746.2 Measured Moisture Fraction (BWSmsd)0.104 Moisture Fraction @ Saturation (BWSsat)1.000 Moisture Fraction (BWS)0.104 O2 Concentration, % (O2)10.5 CO2 Concentration, % (CO2)8.6 Molecular Weight, lb/lb-mole (dry) (Md)29.80 Molecular Weight, lb/lb-mole (wet) (Ms)28.57 Velocity, ft/sec (Vs)80.9 VFR at stack conditions, acfm (Qa)10,586 VFR at standard conditions, scfh (Qsw)388,999 VFR at standard conditions, scfm (Qsw)6,483 VFR at standard conditions, dscfm (Qsd)5,807 1.0001.0001.000 0.1050.1050.103 5,839 5,693 5,888 6,510 6,361 6,579 390,586 381,682 394,730 10,595 10,461 10,701 80.9 79.9 81.7 28.52 28.59 28.59 29.73 29.83 29.83 10.71 10.42 10.43 8.14 8.85 8.83 0.103 0.105 0.105 744.0 751.2 743.3 284.3 291.6 283.6 25.92 25.90 25.91 4.20 4.00 4.10 25.61 25.61 25.61 0.840 0.840 0.840 1.27 1.22 1.29 1.124 1.105 1.136 3 4 5 6 7 5 6 7 8 B1 2 Traverse Point A1 2 3 4 Leak Check Pass Pass Pass Stop Time 15:18 8:37 10:04 Start Time 15:04 8:24 9:50 8 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 Run No. 1 2 3 Status VALID VALID VALID Date 9/5/24 9/6/24 9/5/24 44 of 99 Appendix C 45 of 99 QA Data Location Source Project No. O₂ - Outlet CO₂ - Outlet Make Servomex Servomex Model 4900 4900 S/N 100269 100269 Operating Range 25 100 Cylinder ID Zero NA NA Mid RR02538 RR02538 High EB0069884 EB0069884 Cylinder Certifed Values Zero NA NA Mid 11 10.9 High 23.99 23.9 Cylinder Expiration Date Zero NA NA Mid 9/19/31 9/19/31 High 4/1/32 4/1/32 Type of Sample Line Heated Sample Line Parameter Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 46 of 99 Response Times Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Zero 30 30 Low NA NA Mid 30 30 Average 30.0 30.0 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Parameter Response Times, seconds 47 of 99 Calibration Data Location: Source: Project No.: Date: O₂ - Outlet CO₂ - Outlet Expected Average Concentration 10.50 8.50 Span Between Low 10.50 8.50 High 52.50 42.50 Desired Span 23.99 23.90 Low Range Gas Low NA NA High NA NA Mid Range Gas Low 9.60 9.56 High 14.39 14.34 High Range Gas Low NA NA High NA NA Actual Concentration (% or ppm) Zero 0.00 0.00 Low NA NA Mid 11.00 10.99 High 23.99 23.90 Upscale Calibration Gas (CMA)Mid Mid Instrument Response (% or ppm) Zero 0.00 -0.02 Low NA NA Mid 10.95 11.19 High 23.90 23.98 Performance (% of Span or Cal. Gas Conc.) Zero 0.00 0.08 Low NA NA Mid 0.21 0.84 High 0.38 0.33 Status Zero PASS PASS Low NA NA Mid PASS PASS High PASS PASS Jenbacher #1 Central Valley Water Reclamation (CVWR) Parameter 9/4/24 AST-2024-3767 48 of 99 Calibration Data Location: Source: Project No.: Date: O₂ - Outlet CO₂ - Outlet Expected Average Concentration 11.00 7.00 Span Between Low 11.00 7.00 High 55.00 35.00 Desired Span 23.99 23.90 Low Range Gas Low NA NA High NA NA Mid Range Gas Low 9.60 9.56 High 14.39 14.34 High Range Gas Low NA NA High NA NA Actual Concentration (% or ppm) Zero 0.00 0.00 Low NA NA Mid 11.00 10.99 High 23.99 23.90 Upscale Calibration Gas (CMA)Mid Mid Instrument Response (% or ppm) Zero 0.00 -0.01 Low NA NA Mid 10.99 11.16 High 23.98 23.91 Performance (% of Span or Cal. Gas Conc.) Zero 0.00 0.04 Low NA NA Mid 0.04 0.71 High 0.04 0.04 Status Zero PASS PASS Low NA NA Mid PASS PASS High PASS PASS Parameter 9/5/24 AST-2024-3767 Jenbacher #1 Central Valley Water Reclamation (CVWR) 49 of 99 Bias/Drift Determinations Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.01 -0.03 Pretest System Upscale Response 10.91 11.08 Posttest System Upscale Response 10.89 11.09 Pretest System Zero Response 0.01 -0.03 Posttest System Zero Response 0.01 -0.01 Pretest System Upscale Response 10.89 11.09 Posttest System Upscale Response 10.91 11.12 Pretest System Zero Response 0.01 -0.01 Posttest System Zero Response 0.02 -0.02 Pretest System Upscale Response 10.91 11.12 Posttest System Upscale Response 10.90 11.12 Run 2 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 Parameter Run 1 Run 3 50 of 99 Bias/Drift Determinations Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Run 1 Date 9/4/24 Span Value 23.99 23.90 Initial Instrument Zero Cal Response 0.00 -0.02 Initial Instrument Upscale Cal Response 10.95 11.19 Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.01 -0.03 Pretest System Upscale Response 10.91 11.08 Posttest System Upscale Response 10.89 11.09 Bias (%) Pretest Zero 0.04 0.08 Posttest Zero 0.04 -0.04 Pretest Span -0.17 -0.46 Posttest Span -0.25 -0.42 Drift (%) Zero 0.00 -0.13 Mid -0.08 0.04 Run 2 Date 9/5/24 Span Value 23.99 23.90 Instrument Zero Cal Response 0.00 -0.01 Instrument Upscale Cal Response 10.99 11.16 Pretest System Zero Response 0.01 -0.03 Posttest System Zero Response 0.01 -0.01 Pretest System Upscale Response 10.89 11.09 Posttest System Upscale Response 10.91 11.12 Bias (%) Pretest Zero 0.04 -0.08 Posttest Zero 0.04 0.00 Pretest Span -0.42 -0.29 Posttest Span -0.33 -0.17 Drift (%) Zero 0.00 0.08 Mid 0.08 0.13 Run 3 Date 9/5/24 Span Value 23.99 23.90 Instrument Zero Cal Response 0.00 -0.01 Instrument Upscale Cal Response 10.99 11.16 Pretest System Zero Response 0.01 -0.01 Posttest System Zero Response 0.02 -0.02 Pretest System Upscale Response 10.91 11.12 Posttest System Upscale Response 10.90 11.12 Bias (%) Pretest Zero 0.04 0.00 Posttest Zero 0.08 -0.04 Pretest Span -0.33 -0.17 Posttest Span -0.38 -0.17 Drift (%) Zero 0.04 -0.04 Mid -0.04 0.00 Parameter Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 51 of 99 QA Data Location Source Project No. O₂ - Outlet CO₂ - Outlet Make Servomex Servomex Model 4900 4900 S/N 100269 100269 Operating Range 25 100 Cylinder ID Zero NA NA Mid RR02538 RR02538 High EB0069884 EB0069884 Cylinder Certifed Values Zero NA NA Mid 11 10.9 High 23.99 23.9 Cylinder Expiration Date Zero NA NA Mid 9/19/31 9/19/31 High 4/1/32 4/1/32 Type of Sample Line Heated Sample Line Parameter Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 52 of 99 Response Times Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Zero 30 30 Low NA NA Mid 30 30 Average 30.0 30.0 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 Parameter Response Times, seconds 53 of 99 Calibration Data Location: Source: Project No.: Date: O₂ - Outlet CO₂ - Outlet Expected Average Concentration 10.50 8.50 Span Between Low 10.50 8.50 High 52.50 42.50 Desired Span 23.99 23.90 Low Range Gas Low NA NA High NA NA Mid Range Gas Low 9.60 9.56 High 14.39 14.34 High Range Gas Low NA NA High NA NA Actual Concentration (% or ppm) Zero 0.00 0.00 Low NA NA Mid 11.00 10.90 High 23.99 23.90 Upscale Calibration Gas (CMA)Mid Mid Instrument Response (% or ppm) Zero 0.00 -0.01 Low NA NA Mid 10.99 11.16 High 23.98 23.91 Performance (% of Span or Cal. Gas Conc.) Zero 0.00 0.04 Low NA NA Mid 0.04 1.09 High 0.04 0.04 Status Zero PASS PASS Low NA NA Mid PASS PASS High PASS PASS Jenbacher #3 Central Valley Water Reclamation (CVWR) Parameter 9/5/24 AST-2024-3767 54 of 99 Calibration Data Location: Source: Project No.: Date: O₂ - Outlet CO₂ - Outlet Expected Average Concentration 10.61 8.29 Span Between Low 10.61 8.29 High 53.03 41.44 Desired Span 23.99 23.90 Low Range Gas Low NA NA High NA NA Mid Range Gas Low 9.60 9.56 High 14.39 14.34 High Range Gas Low NA NA High NA NA Actual Concentration (% or ppm) Zero 0.00 0.00 Low NA NA Mid 11.00 10.90 High 23.99 23.90 Upscale Calibration Gas (CMA)Mid Mid Instrument Response (% or ppm) Zero 0.00 -0.02 Low NA NA Mid 11.00 11.20 High 23.99 23.94 Performance (% of Span or Cal. Gas Conc.) Zero 0.00 0.08 Low NA NA Mid 0.00 1.26 High 0.00 0.17 Status Zero PASS PASS Low NA NA Mid PASS PASS High PASS PASS Parameter 9/6/24 AST-2024-3767 Jenbacher #3 Central Valley Water Reclamation (CVWR) 55 of 99 Bias/Drift Determinations Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Pretest System Zero Response 0.02 -0.02 Posttest System Zero Response 0.01 -0.02 Pretest System Upscale Response 10.90 11.12 Posttest System Upscale Response 10.88 11.09 Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.02 0.00 Pretest System Upscale Response 10.91 11.11 Posttest System Upscale Response 10.93 11.13 Pretest System Zero Response 0.02 0.00 Posttest System Zero Response 0.02 0.00 Pretest System Upscale Response 10.93 11.13 Posttest System Upscale Response 10.93 11.14 Run 2 Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 Parameter Run 1 Run 3 56 of 99 Bias/Drift Determinations Location: Source: Project No.: O₂ - Outlet CO₂ - Outlet Run 1 Date 9/5/24 Span Value 23.99 23.90 Initial Instrument Zero Cal Response 0.00 -0.01 Initial Instrument Upscale Cal Response 10.99 11.16 Pretest System Zero Response 0.02 -0.02 Posttest System Zero Response 0.01 -0.02 Pretest System Upscale Response 10.90 11.12 Posttest System Upscale Response 10.88 11.09 Bias (%) Pretest Zero 0.08 -0.04 Posttest Zero 0.04 -0.04 Pretest Span -0.38 -0.17 Posttest Span -0.46 -0.29 Drift (%) Zero -0.04 0.00 Mid -0.08 -0.13 Run 2 Date 9/6/24 Span Value 23.99 23.90 Instrument Zero Cal Response 0.00 -0.02 Instrument Upscale Cal Response 11.00 11.20 Pretest System Zero Response 0.01 0.00 Posttest System Zero Response 0.02 0.00 Pretest System Upscale Response 10.91 11.11 Posttest System Upscale Response 10.93 11.13 Bias (%) Pretest Zero 0.04 0.08 Posttest Zero 0.08 0.08 Pretest Span -0.38 -0.38 Posttest Span -0.29 -0.29 Drift (%) Zero 0.04 0.00 Mid 0.08 0.08 Run 3 Date 9/6/24 Span Value 23.99 23.90 Instrument Zero Cal Response 0.00 -0.02 Instrument Upscale Cal Response 11.00 11.20 Pretest System Zero Response 0.02 0.00 Posttest System Zero Response 0.02 0.00 Pretest System Upscale Response 10.93 11.13 Posttest System Upscale Response 10.93 11.14 Bias (%) Pretest Zero 0.08 0.08 Posttest Zero 0.08 0.08 Pretest Span -0.29 -0.29 Posttest Span -0.29 -0.25 Drift (%) Zero 0.00 0.00 Mid 0.00 0.04 Parameter Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 57 of 99 Balance Red Ball Technical Gas Service 555 Craig Kennedy Way Shreveport, LA 71107 800-551-8150 Accreditation #62754 PGVP Vendor ID # G12024 EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS Cylinder Number:EB0069884 Certification Date:04/03/2024 Product ID Number:127907 Expiration Date:04/01/2032 Cylinder Pressure:1900 PSIG MFG Facility: - Shreveport - LA COA #EB0069884.20240320-0 Lot Number:EB0069884.20240320 Customer PO. NO.:Tracking Number:084212711 Customer:Previous Certification Dates: This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-12/531, using procedure G2. Do Not Use This Cylinder Below 100 psig (0.7 Megapascal). Certified Concentration(s) Component Concentration Uncertainty Analytical Principle Assayed On Carbon Dioxide 23.9 %±0.1 %FTIR 04/03/2024 Oxygen 23.99 %±0.06 %MPA 03/27/2024 Nitrogen Analytical Measurement Data Available Online. Reference Standard(s) Serial Number Lot Expiration Type Balance Component Concentration Uncertainty(%)NIST Reference CC520205 CC520205.20230108 07/09/2031 GMIS N2 O2 20.01 %0.112 SRM 2659a EB0022009 EB0022009.20201022 04/05/2030 GMIS N2 CO2 24.76 %0.237 C1847810.03 Analytical Instrumentation SMART-CERT Component Principle Make MPC Date O2 MPA Thermo 03/18/2024 CO2 FTIR MKS 04/02/2024 Serial 1162980025 017146467 This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This calibration/test was performed using Gases or Scales that are traceable through National Institute of Standards and Technology (NIST) to the International System of Units (SI). The basis of compliance stated is a comparison of the measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball Technical Gas Services. If not included, the uncertainty of calibrations are available upon request and were taken into account when determining pass or fail. Brittany Johnson Analytical Chemist Assay Laboratory: Red Ball TGS Version 02-J, Revised on 2018-09-17 Model 410i MKS 2031DJG2EKVS13T 58 of 99 Balance Red Ball Technical Gas Service 555 Craig Kennedy Way Shreveport, LA 71107 800-551-8150 Accreditation #62754 PGVP Vendor ID # G12023 EPA PROTOCOL GAS CERTIFICATE OF ANALYSIS Cylinder Number:RR02538 Certification Date:09/21/2023 Product ID Number:125371 Expiration Date:09/19/2031 Cylinder Pressure:1900 PSIG MFG Facility: - Shreveport - LA COA #RR02538.20230831-0 Lot Number:RR02538.20230831 Customer PO. NO.:Tracking Number:103925725 Customer:Previous Certification Dates: This calibration standard has been certified per the May 2012 EPA Traceability Protocol, Document EPA-600/R-12/531, using procedure G1. Do Not Use This Cylinder Below 100 psig (0.7 Megapascal). Certified Concentration(s) Component Concentration Uncertainty Analytical Principle Assayed On Carbon Dioxide 10.9 %±0.11 %FTIR 09/21/2023 Oxygen 11.00 %±0.03 %MPA 09/18/2023 Nitrogen Analytical Measurement Data Available Online. Reference Standard(s) Serial Number Lot Expiration Type Balance Component Concentration Uncertainty(%)NIST Reference CC737012 CC737012.20230228 07/09/2031 GMIS N2 O2 20 %0.112 SRM 2659a EB0022021 EB0022021.20180323 07/15/2026 GMIS N2 CO2 14.9 %0.777 101001 Analytical Instrumentation SMART-CERT Component Principle Make MPC Date O2 MPA Thermo 09/18/2023 CO2 FTIR MKS 09/21/2023 Serial 1162980025 017146467 This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This calibration/test was performed using Gases or Scales that are traceable through National Institute of Standards and Technology (NIST) to the International System of Units (SI). The basis of compliance stated is a comparison of the measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball Technical Gas Services. If not included, the uncertainty of calibrations are available upon request and were taken into account when determining pass or fail. Jasmine Godfrey Analytical Chemist Assay Laboratory: Red Ball TGS Version 02-J, Revised on 2018-09-17 Model 410i MKS 2031DJG2EKVS13T 59 of 99 Location: Source: Project No.: Date EPA O2 Servomex 4900 100269 25.0 Cylinder Number ID Zero NA Mid RR02538 High EB0069884 Cylinder Certified Values Zero 0.0 Mid 11 High 23.99 Instrument Response (% or ppm) Zero 0.00 Mid 11.00 High 24.0 Calibration Gas Selection (% of Span) Mid 44.0 High 96.0 Calibration Error Performance (% of Span) Zero 0.0 Mid 0.0 High -0.1 Linearity (% of Range) 0.1 (%) lpm (%) (%) (%) (%) (%) (%) (%)( ± 2 %) 10L/5L 80.0 5.0 19.2 19.20 19.33 19.28 19.26 19.29 0.09 0.5% 10L/5L 50.0 5.0 12.0 12.00 12.09 12.04 12.04 12.06 0.06 0.5% 10L/1L 20.0 4.0 4.8 4.80 4.85 4.86 4.86 4.86 0.06 1.2% 10L/1L 10.0 4.0 2.4 2.40 2.42 2.42 2.43 2.42 0.02 1.0% (%)( ± 2 %)( ± 2 %)( ± 2 %) 19.29 0.2% -0.1% -0.2% 12.06 0.3% -0.1% -0.1% 4.86 -0.1% 0.1% 0.1% 2.42 -0.1% -0.1% 0.3% Mid-Level Supply Gas Calibration Direct to Analyzer Calibration Injection 1 Injection 2 Injection 3 Average Gas Analyzer Analyzer Analyzer Analyzer Concentration Concentration Concentration Concentration Concentration (%) (%) (%) (%) (%) (%)( ± 2 %) 11.00 10.96 10.97 10.98 10.97 -0.03 -0.3% Analyzer Make: Servomex Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/24 Parameter Make Model S/N Span Method Criteria Analyzer Model: 4900 Analyzer SN: 100269 Environics ID: 8029 Component/Balance Gas: O2/N2 Cylinder Gas ID (Dilution): EB0069884 Cylinder Gas Concentration (Dilution), %: 23.99 *Not all AST Environics Units have 2-10L Mass Flow Controllers. For these units the 90% @ 7lpm and 80% @ 7lpm injections will not be conducted. Cylinder Gas ID (Mid-Level): RR02538 Cylinder Gas Concentration (Mid-Level), %: 11 Target Mass Flow Contollers Target Dilution Target Flow Rate Target Concentration Actual Concentration Injection 1 Analyzer Concentration Injection 2 Analyzer Concentration Injection 3 Analyzer Concentration Average Analyzer Concentration Difference Average Error Average Analyzer Concentration Injection 1 Error Injection 2 Error Injection 3 Error Difference Average Error 60 of 99 Dilution System Make: Dilution System Model: Dilution System S/N: Calibration Equipment Make: Calibration Equipment Model: Calibration Equipment S/N: Flow Cell S/N: Flow Cell S/N: Calibration Gas: Barometric Pressure, mmHg: Ambient Temperature, °F: Mass Flow Controller ID Size, ccm: Make: Model: S/N: Set Flow True Flow Difference Set Flow True Flow Difference Set Flow True Flow Difference cc/min cc/min cc/min cc/min cc/min cc/min 5%500 502 0.4%500 495 1.0%50 47 5.8% 10%1,000 1,015 1.5%1,000 1,014 1.4%100 98 2.4% 20%2,000 2,040 2.0%2,000 2,037 1.9%200 199 0.3% 30%3,000 3,060 2.0%3,000 3,057 1.9%300 301 0.4% 40%4,000 4,083 2.1%4,000 4,071 1.8%400 403 0.6% 50%5,000 5,093 1.9%5,000 5,082 1.6%500 504 0.7% 60%6,000 6,110 1.8%6,000 6,100 1.7%600 606 0.9% 70%7,000 7,124 1.8%7,000 7,130 1.9%700 709 1.2% 80%8,000 8,150 1.9%8,000 8,150 1.9%800 814 1.7% 90%9,000 9,172 1.9%9,000 9,176 2.0%900 919 2.2% 100%10,000 10,214 2.1%10,000 10,202 2.0%1,000 1,028 2.8% Date 4040 4040 72 Environics 8029 #1 10,000 Environics 4040 Alicat Scientific 197206; 197208 197208 197206 Nitrogen 25.6 Calibration Performed By Ryan Lyons 4/26/23 455242003 Mass Flow Controller Calibration Note: The mass flow controller's calibration values are used by the dilution system's operating software to improve accuracy. These calibrations are not necessarily indicative of the systems overall performance. Performance is verified by conducting a Method 205 prior to each field use. M-10SLPD/5MM-D/5M, M-1SLPM-D/5M 4040 10,000 # 2 # 3 Environics 455242004 1,000 Environics 455242002 61 of 99 Location Source(s) Project No. Date(s) Ethylene Cylinder ID Concentration (ppmv) Instrument Outlet CTS 1 99.34 CTS 7 97.38 AVERAGE 97.55 Greatest Deviation from average CTS 2 97.16 CTS 8 97.19 MAX 99.34 1.83% CTS 3 97.61 CTS 9 97.47 deviation 1.79 CTS 4 97.44 CTS 10 97.49 MIN 97.16 Agreement with Assumed Pathlength CTS 5 97.22 CTS 11 97.50 deviation 0.39 96.58% CTS 6 97.26 CTS 12 --within 5% no correction required CTS 1 CTS 7 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/4/24 9:01:50 24-3767 CVWR JENBACHER #1_000018.LAB 191.7 1.128 99.28 9/5/24 12:20:27 24-3767 CVWR JEN 192.0 1.015 97.36 9/4/24 9:02:53 24-3767 CVWR JENBACHER #1_000019.LAB 191.7 1.129 99.25 9/5/24 12:21:30 24-3767 CVWR JEN 192.0 1.015 97.40 9/4/24 9:03:56 24-3767 CVWR JENBACHER #1_000020.LAB 191.7 1.130 99.47 9/5/24 12:22:33 24-3767 CVWR JEN 192.0 1.014 97.40 CTS 2 CTS 8 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/4/24 10:00:40 24-3767 CVWR JENBACHER #1_000073.LAB 192.2 1.020 97.21 9/5/24 16:04:06 24-3767 CVWR JEN 192.0 1.012 97.22 9/4/24 10:01:42 24-3767 CVWR JENBACHER #1_000074.LAB 192.2 1.019 97.10 9/5/24 16:05:09 24-3767 CVWR JEN 192.0 1.013 97.08 9/4/24 10:02:45 24-3767 CVWR JENBACHER #1_000075.LAB 192.2 1.019 97.16 9/5/24 16:06:11 24-3767 CVWR JEN 192.0 1.012 97.27 CTS 3 CTS 9 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/4/24 15:06:52 24-3767 CVWR JENBACHER #1_000347.LAB 192.1 1.020 97.58 9/6/24 7:33:21 24-3767 CVWR JEN 192.1 1.024 97.45 9/4/24 15:07:55 24-3767 CVWR JENBACHER #1_000348.LAB 192.0 1.020 97.64 9/6/24 7:34:23 24-3767 CVWR JEN 192.1 1.024 97.58 9/6/24 7:35:26 24-3767 CVWR JEN 192.1 1.024 97.38 CTS 4 CTS 10 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/5/24 7:34:56 24-3767 CVWR JENBACHER #1_000370.LAB 192.1 1.018 97.45 9/6/24 9:35:45 24-3767 CVWR JEN 192.1 1.021 97.23 9/5/24 7:35:59 24-3767 CVWR JENBACHER #1_000371.LAB 192.1 1.018 97.49 9/6/24 9:36:48 24-3767 CVWR JEN 192.0 1.020 97.80 9/5/24 7:37:02 24-3767 CVWR JENBACHER #1_000372.LAB 192.1 1.017 97.37 9/6/24 9:37:51 24-3767 CVWR JEN 192.0 1.020 97.46 CTS 5 CTS 11 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/5/24 9:38:45 24-3767 CVWR JENBACHER #1_000487.LAB 192.1 1.015 97.30 9/6/24 10:59:13 24-3767 CVWR JEN 191.9 1.019 97.69 9/5/24 9:39:48 24-3767 CVWR JENBACHER #1_000488.LAB 192.0 1.016 97.20 9/6/24 11:00:16 24-3767 CVWR JEN 191.9 1.019 97.60 9/5/24 9:40:51 24-3767 CVWR JENBACHER #1_000489.LAB 192.1 1.016 97.16 9/6/24 11:01:19 24-3767 CVWR JEN 191.9 1.020 97.19 CTS 6 CTS 12 Date Time File Temperature (CPressure Ethylene Date Time File Temperature (CPressure Ethylene 9/5/24 11:00:36 24-3767 CVWR JENBACHER #1_000564.LAB 192.0 1.015 97.16 9/5/24 11:01:39 24-3767 CVWR JENBACHER #1_000565.LAB 192.0 1.017 97.06 9/5/24 11:02:42 24-3767 CVWR JENBACHER #1_000566.LAB 192.1 1.016 97.54 MKS 14 (Serial #184146639) Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/2024 101.0 EB0073902 62 of 99 Location Source Project No. Date EB0038762 Component 93.0 Acetaldehyde EB0038762 Component 4.57 SF6 Instrument ID Outlet Direct Spike Values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/04/24 9:13:20 24-3767 CVWR JE 191.9 1.072 86.53 4.421 09/04/24 9:14:23 24-3767 CVWR JE 192.0 1.055 86.25 4.403 09/04/24 9:15:26 24-3767 CVWR JE 192.0 1.063 85.86 4.389 09/04/24 9:16:29 24-3767 CVWR JE 191.8 1.226 86.75 4.488 09/04/24 9:17:31 24-3767 CVWR JE 191.7 1.227 86.99 4.493 09/04/24 9:18:34 24-3767 CVWR JE 191.7 1.229 86.91 4.495 09/04/24 9:19:37 24-3767 CVWR JE 191.7 1.230 86.76 4.494 Average 86.58 4.455 Native Values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/04/24 9:25:53 24-3767 CVWR JE 192.0 1.048 0.14 0.010 09/04/24 9:26:56 24-3767 CVWR JE 192.0 1.045 0.14 0.010 09/04/24 9:27:59 24-3767 CVWR JE 192.0 1.045 0.14 0.010 09/04/24 9:29:01 24-3767 CVWR JE 192.1 1.045 0.14 0.010 09/04/24 9:30:04 24-3767 CVWR JE 192.0 1.044 0.14 0.010 09/04/24 9:31:07 24-3767 CVWR JE 192.1 1.044 0.14 0.010 09/04/24 9:32:10 24-3767 CVWR JE 192.0 1.044 0.14 0.010 Average 0.14 0.010 Spiked values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/04/24 9:41:34 24-3767 CVWR JE 192.1 1.042 5.24 0.282 09/04/24 9:42:37 24-3767 CVWR JE 192.2 1.042 5.16 0.282 09/04/24 9:43:40 24-3767 CVWR JE 192.1 1.042 5.42 0.274 09/04/24 9:44:42 24-3767 CVWR JE 192.1 1.044 5.12 0.276 09/04/24 9:45:45 24-3767 CVWR JE 192.1 1.043 5.19 0.278 09/04/24 9:46:48 24-3767 CVWR JE 192.1 1.040 4.96 0.269 Average 5.18 0.277 Dilution Factor 6.0% Calculated Spike 5.32 Spike Recovery 97.42% MKS 14 (Serial #184146639) Tracer Cylinder ID Tracer Gas concentration Spike Gas concentration Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/2024 Spike Cylinder ID 63 of 99 Location Source Project No. Date EB0038762 Component 93.0 Acetaldehyde EB0038762 Component 4.57 SF6 Instrument ID Outlet Direct Spike Values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/04/24 9:13:20 24-3767 CVWR JENBACHER #1_000029.LAB 191.9 1.072 86.53 4.421 09/04/24 9:14:23 24-3767 CVWR JENBACHER #1_000030.LAB 192.0 1.055 86.25 4.403 09/04/24 9:15:26 24-3767 CVWR JENBACHER #1_000031.LAB 192.0 1.063 85.86 4.389 09/04/24 9:16:29 24-3767 CVWR JENBACHER #1_000032.LAB 191.8 1.226 86.75 4.488 09/04/24 9:17:31 24-3767 CVWR JENBACHER #1_000033.LAB 191.7 1.227 86.99 4.493 09/04/24 9:18:34 24-3767 CVWR JENBACHER #1_000034.LAB 191.7 1.229 86.91 4.495 09/04/24 9:19:37 24-3767 CVWR JENBACHER #1_000035.LAB 191.7 1.230 86.76 4.494 Average 86.58 4.455 Native Values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/05/24 14:30:06 24-3767 CVWR JENBACHER #1_000763.LAB 192.1 1.007 0.14 0.010 09/05/24 14:31:09 24-3767 CVWR JENBACHER #1_000764.LAB 192.1 1.008 0.14 0.010 09/05/24 14:32:12 24-3767 CVWR JENBACHER #1_000765.LAB 192.1 1.007 0.14 0.010 09/05/24 14:33:15 24-3767 CVWR JENBACHER #1_000766.LAB 192.1 1.009 0.14 0.010 09/05/24 14:34:18 24-3767 CVWR JENBACHER #1_000767.LAB 192.1 1.006 0.14 0.010 09/05/24 14:35:20 24-3767 CVWR JENBACHER #1_000768.LAB 192.1 1.010 0.14 0.010 09/05/24 14:36:23 24-3767 CVWR JENBACHER #1_000769.LAB 192.1 1.008 0.14 0.010 Average 0.14 0.010 Spiked values Date Time File Temperature (C) Pressure Spike (ppm) Tracer (ppm) 09/05/24 14:39:31 24-3767 CVWR JENBACHER #1_000772.LAB 192.1 1.008 5.90 0.288 09/05/24 14:40:34 24-3767 CVWR JENBACHER #1_000773.LAB 192.1 1.007 5.77 0.293 09/05/24 14:41:37 24-3767 CVWR JENBACHER #1_000774.LAB 192.1 1.008 5.65 0.294 09/05/24 14:42:39 24-3767 CVWR JENBACHER #1_000775.LAB 192.1 1.008 5.65 0.294 09/05/24 14:43:42 24-3767 CVWR JENBACHER #1_000776.LAB 192.1 1.011 5.68 0.293 09/05/24 14:44:45 24-3767 CVWR JENBACHER #1_000777.LAB 192.1 1.009 5.72 0.296 09/05/24 14:45:47 24-3767 CVWR JENBACHER #1_000778.LAB 192.1 1.008 5.63 0.295 Average 5.72 0.293 Dilution Factor 6.4% Calculated Spike 5.64 Spike Recovery 101.39% MKS 14 (Serial #184146639) Tracer Cylinder ID Tracer Gas concentration Spike Gas concentration Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/2024 Spike Cylinder ID 64 of 99 Location Project No. Instrument Source Jenbacher #1 Jenbacher #3 Date 9/4/24 9/5/24 Time 9:41 14:39 Analyte Acetaldehyde Acetaldehyde Direct 86.58 86.58 Native 0.14 0.14 Spiked 5.18 5.72 Dilution 6.0% 6.4% Recovery 97% 101% Result PASS PASS Summary of Spikes Central Valley Water Reclamation (CVWR) AST-2024-3767 MKS 14 (Serial #184146639) 65 of 99 This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This calibration/test was performed using Gases or Scales that are traceable through National Institute of Standards and Technology (NIST) to the International System of Units (SI). The basis of compliance stated is a comparison of the measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball Technical Gas Services. If not included, the uncertainty of calibrations are available upon request and were taken into account when determining pass or fail. Aaron Varelas Analytical Chemist Assay Laboratory: Red Ball TGS Version 02-G, Revised on 2017-07-02 MPC Date C2H4 FTIR MKS MKS 2031DJG2EKVS13T 017146467 Analytical Instrumentation SMART-CERT Component Principle Make Model Serial 102 PPM 2 4034426CC722751CC72275107/28/2024 PS N2 C2H4 Reference Standard(s) Serial Number Lot Expiration Type Balance Component Concentration Uncertainty(%)NIST Reference Nitrogen Analytical Measurement Data Available Online. Balance Ethylene Certified Concentration(s) Component Concentration Uncertainty Analytical Principle 101 PPM ± 2% NIST FTIR Customer:Previous Certification Dates: Do Not Use This Cylinder Below 100 psig (0.7 Megapascal). This mixture is for laboratory use only, not for drug, household or other use. This mixture is certified in Mole % to be within ±2% of the actual number reported with a confidence of 95%. This mixture was manufactured by scale; weights traceable to N.I.S.T. Certificate #822/266926-02. COA #EB0073902.20230730-0 Lot Number:EB0073902.20230730 Customer PO. NO.:Tracking Number:084266022 Product ID Number:124838 Expiration Date:08/06/2025 Cylinder Pressure:1900 PSIG MFG Facility: - Shreveport - LA CERTIFIED GAS CERTIFICATE OF ANALYSIS Cylinder Number:EB0073902 Certification Date:08/07/2023 Red Ball Technical Gas Service 555 Craig Kennedy Way Shreveport, LA 71107 800-551-8150 Accreditation #62754 PGVP Vendor ID # G12023 66 of 99 4.57 PPM ± 2% NIST FTIR This is to certify the gases referenced have been calibrated/tested, and verified to meet the defined specifications. This calibration/test was performed using Gases or Scales that are traceable through National Institute of Standards and Technology (NIST) to the International System of Units (SI). The basis of compliance stated is a comparison of the measurement parameters to the specified or required calibration/testing process. The expanded uncertainties use a coverage factor of k=2 to approximate the 95% confidence level of the measurement, unless otherwise noted. This calibration certificate applies only to the item described and shall not be reproduced other than in full, without written approval from Red Ball Technical Gas Services. If not included, the uncertainty of calibrations are available upon request and were taken into account when determining pass or fail. Anthony Cyr Assistant Operations Manager Assay Laboratory: Red Ball TGS Version 02-G, Revised on 2017-07-02 MKS MKS 2031DJG2EKVS13T 017146467 MPC Date SF6 FTIR MKS MKS 2031DJG2EKVS13T 017146467 C2H4O FTIR Analytical Instrumentation SMART-CERT Component Principle Make Model Serial 2 4011772 9.97 PPM 5 4011772 CC742079 CC742079 07/27/2023 PS N2 C2H4O 98.1 PPM CC518670 CC518670 07/27/2023 PS N2 SF6 Reference Standard(s) Serial Number Lot Expiration Type Balance Component Concentration Uncertainty(%)NIST Reference Nitrogen Analytical Measurement Data Available Online. Balance Acetaldehyde Sulfur Hexafluoride Certified Concentration(s) Component Concentration Uncertainty Analytical Principle 93.0 PPM ± 2% NIST FTIR Customer:Previous Certification Dates: Do Not Use This Cylinder Below 100 psig (0.7 Megapascal). This mixture is for laboratory use only, not for drug, household or other use. This mixture is certified in Mole % to be within ±2% of the actual number reported with a confidence of 95%. This mixture was manufactured by scale; weights traceable to N.I.S.T. Certificate #822/266926-02. COA #EB0038762.20230306-0 Lot Number:EB0038762.20230306 Customer PO. NO.:Tracking Number:065156566 Product ID Number:125303 Expiration Date:03/14/2025 Cylinder Pressure:1900 PSIG MFG Facility: - Shreveport - LA CERTIFIED GAS CERTIFICATE OF ANALYSIS Cylinder Number:EB0038762 Certification Date:03/15/2023 Red Ball Technical Gas Service 555 Craig Kennedy Way Shreveport, LA 71107 800-551-8150 Accreditation #62754 PGVP Vendor ID # G12023 67 of 99 Location Source(s) Project No. Health Check Parameter Single Beam (Pre-Test) Instrument ID MKS 14 (Serial #184146639) Date Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/3/2024 68 of 99 Location Source(s) Project No. Health Check Parameter Single Beam (Post-Test) Instrument ID MKS 14 (Serial #184146639) Date Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/6/2024 69 of 99 Location Source(s) Project No. Health Check Parameter Detector Linearity Instrument ID MKS 14 (Serial #184146639) Date Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/3/2024 70 of 99 Location Source(s) Project No. Health Check Parameter Peak Analysis Instrument ID MKS 14 (Serial #184146639) Date Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/3/2024 71 of 99 Location Source(s) Project No. Health Check Parameter Signal to Noise Ratio Instrument ID MKS 14 (Serial #184146639) Date Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/3/2024 72 of 99 Location Source(s) Project No. Health Check Parameter Analysis Validation Utility Instrument ID MKS 14 (Serial #184146639) Date Analysis Validation Report Sample Filename: D:\Documents\2024\24-3767 CVWR\24-3767 CVWR JENBACHER #1_000386.LAB Filename for noise: D:\Documents\2024\24-3767 CVWR\24-3767 CVWR JENBACHER #1_000356.LAB Interferences Filenames: C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct C C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #2.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #3.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #4.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #5.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #6.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #7.LAB C:\OLT\Analysis Validation Utility\Support spectra\1min 191C LN2\Interferents H2O 20pct CO2 20pct 1min #8.LAB Recipe path: C:\OLT\RECIPES\NG Engines R3 - Copy-DO NOT USE.MGRCP Gas calibration Name Conc MDC3 MDC2 MDC1 MAU FMU*R OCU ~ DL NO (350,3000) 191C 9.52 4.88 0.15 0.56 0.76 6.66 6.66 2.28 NO2 (150) 191C (1OF2) 51.44 1.04 0.21 0.06 0.07 1.1 1.1 0.41 NO2 (2000) 191C (2OF2) 52 8.8 0.69 2.34 2.99 11.23 11.23 4.18 N2O (100,200,300) 191C 0.3 0.22 0.05 0.08 0.1 0.25 0.25 0.06 NH3 (300) 191C (1OF2) 0.04 0.84 0.04 0.21 0.36 1.41 1.41 0.62 NH3 (3000) 191C (2OF2) -0.9 6.66 0.52 2.52 4.75 12.57 12.57 2.86 H2O% (20) 191C 9.99 0.08 -0.02 0.03 0.17 0.17 - CO2% (20) 191C 5.85 0.15 -0.03 0.04 0.21 0.21 - CO (500) 191C (1OF2) 397.86 19.42 0.1 0.45 0.97 37.77 37.77 0.44 CO% (1) 191C (2OF2) 0.04 0 0 00000 CH4 (3000) 191C 1446.94 19.64 0.69 2.32 3.84 29.06 29.06 1.82 ETHANE (500) 191C 33.93 -0.15 ---- 0.4 ETHYLENE (100,3000) 191C 18.81 1.19 0.13 0.27 0.47 2.09 2.09 0.71 ACETYLENE (1000) 191C 1.2 5.15 0.25 1.52 2.04 6.91 6.91 0.31 PROPANE (200) 191C -1.02 0.98 0.28 0.27 0.29 1.05 1.05 0.72 PROPYLENE (200,1000) 191 0.49 2.65 0.22 0.73 0.86 3.1 3.1 1.63 BUTANE (200) 191C 3.32 0.91 0.27 0.25 0.29 1.08 1.08 0.3 FORMALDEHYDE (70) 191C 46.41 -0.09 ----0.24 ACETALDEHYDE (500) 191C -0.58 5.68 0.14 1.15 1.48 7.31 7.31 1.58 FORMIC ACID (10) 191C 0.77 0.34 0.02 0.12 0.14 0.41 0.41 0.68 MEOH (10) 191C 2.06 0.48 0.27 0.25 0.29 0.55 0.55 0.57 SF6 (10) 191C 0 0.01 0.01 0 0.01 0.01 0.01 0.09 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/3/2024 73 of 99 Location Source(s) Project No. Spectra (CTS) 24-3767 CVWR JENBACHER #1_000018.LAB Date 9/4/2024 Time 1 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9:01:50 AM 74 of 99 Location Source(s) Project No. Spectra (Analyte Direct) 24-3767 CVWR JENBACHER #1_000029.LAB Date 9/4/2024 Time 1 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9:13:20 AM 75 of 99 Location Source(s) Project No. Spectra (Native) 24-3767 CVWR JENBACHER #1_000041.LAB Date 9/4/2024 Time 1 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9:25:53 AM 76 of 99 Location Source(s) Project No. Spectra (Spike) 24-3767 CVWR JENBACHER #1_000056.LAB Date 9/4/2024 Time 1 Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9:41:34 AM 77 of 99 QA Data Location Source Project No. Parameter(s) Date Pitot ID Evidence of damage? Evidence of mis-alignment? Calibration or Repair required? 9/4/24 p-743 no no no Date Probe or Thermocouple ID Reference Temp. (°F) Indicated Temp. (°F)Difference Criteria 9/4/24 p705-2 82.0 82.0 0.0% Date Barometric Pressure Evidence of damage? Reading Verified Calibration or Repair required? 9/4/24 Weather Station NA NA NA Weather Station Location Salt Lake City, Utah Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 VFR ± 1.5 % (absolute) 78 of 99 QA Data Location Source Project No. Parameter(s) Date Pitot ID Evidence of damage? Evidence of mis-alignment? Calibration or Repair required? 9/4/24 p-743 no no no Date Probe or Thermocouple ID Reference Temp. (°F) Indicated Temp. (°F)Difference Criteria 9/4/24 p705-2 82.0 82.0 0.0% Date Barometric Pressure Evidence of damage? Reading Verified Calibration or Repair required? 9/5/24 Weather Station NA NA NA Weather Station Location Salt Lake City, Utah Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 VFR ± 1.5 % (absolute) 79 of 99 Location: Source: Project No.: Date: Time O2 CO2 (%) (%) A-1 14:47 10.61 8.29 2 14:48 10.61 8.29 3 14:49 10.61 8.28 10.6 8.3 Single Point Single Point Central Valley Water Reclamation (CVWR) Jenbacher #3 AST-2024-3767 9/5/2024 Average Criteria Met Traverse Point 80 of 99 Location: Source: Project No.: Date: Time O2 CO2 (%) (%) A-1 10:12 11.25 6.53 2 10:13 11.25 6.52 3 10:14 11.25 6.52 11.3 6.5 Single Point Single Point Central Valley Water Reclamation (CVWR) Jenbacher #1 AST-2024-3767 9/4/2024 Average Criteria Met Traverse Point 81 of 99 Appendix D 82 of 99 Location Central Valley Water Reclamation (CVWR) Source Jenbacher #1 Project No.AST-2024-3767 Run Number Run 1 Run 2 Run 3 Date 9/4/24 9/5/24 9/5/24 Start Time 8:25 9:47 11:07 Stop Time 9:24 10:46 12:06 Generator Output, Hz (Gen OP) Time, 0 min 60 60 60 Time, 15 min 60 60 60 Time, 30 min 60 60 60 Time, 45 min 60 60 60 Time, 60 min 60 60 60 Average 60 60 60 Engine Speed, RPM (ES) Time, 0 min 1,500 1,500 1,500 Time, 15 min 1,500 1,500 1,500 Time, 30 min 1,500 1,500 1,500 Time, 45 min 1,500 1,500 1,500 Time, 60 min 1,499 1,500 1,500 Average 1,500 1,500 1,500 Engine Brake Work, HP (EBW) Time, 0 min 2,282 2,282 2,286 Time, 15 min 2,279 2,283 2,276 Time, 30 min 2,275 2,278 2,275 Time, 45 min 2,280 2,279 2,280 Time, 60 min 2,282 2,280 2,280 Average 2,280 2,280 2,279 Engine Load, % (EL) Time, 0 min 94 94 94 Time, 15 min 94 94 94 Time, 30 min 94 94 94 Time, 45 min 94 94 94 Time, 60 min 94 94 94 Average 94 94 94 Fuel Rate, scfh (FR) Time, 0 min 22,947 23,250 23,400 Time, 15 min 23,275 23,397 23,571 Time, 30 min 23,249 23,209 23,391 Time, 45 min 23,109 23,518 23,397 Time, 60 min 23,196 23,249 23,444 Average 23,155 23,325 23,441 Operational Data 83 of 99 Location Central Valley Water Reclamation (CVWR) Source Jenbacher #3 Project No.AST-2024-3767 Run Number Run 1 Run 2 Run 3 Date 9/5/24 9/6/24 9/6/24 Start Time 14:50 8:20 9:45 Stop Time 15:49 9:19 10:44 Generator Output, Hz (Gen OP) Time, 0 min 60 60 60 Time, 15 min 60 60 60 Time, 30 min 60 60 60 Time, 45 min 60 60 60 Time, 60 min 60 60 60 Average 60 60 60 Engine Speed, RPM (ES) Time, 0 min 1,500 1,500 1,500 Time, 15 min 1,500 1,500 1,500 Time, 30 min 1,500 1,500 1,500 Time, 45 min 1,500 1,500 1,500 Time, 60 min 1,500 1,500 1,500 Average 1,500 1,500 1,500 Engine Brake Work, HP (EBW) Time, 0 min 2,280 2,282 2,279 Time, 15 min 2,283 2,280 2,276 Time, 30 min 2,279 2,278 2,280 Time, 45 min 2,278 2,280 2,280 Time, 60 min 2,280 2,278 2,279 Average 2,280 2,280 2,279 Engine Load, % (EL) Time, 0 min 94 94 94 Time, 15 min 94 94 94 Time, 30 min 94 94 94 Time, 45 min 94 94 94 Time, 60 min 94 94 94 Average 94 94 94 Fuel Rate, scfh (FR) Time, 0 min 21,842 33,862 32,650 Time, 15 min 22,075 33,014 33,049 Time, 30 min 21,722 31,994 30,962 Time, 45 min 21,886 30,422 32,011 Time, 60 min 21,817 34,988 32,370 Average 21,868 32,856 32,208 Operational Data 84 of 99 Appendix E 85 of 99 Site Specific Test Plan Central Valley Water Reclamation Facility 800 W Central Valley Road Salt Lake City, UT 84119-3379 Source to be Tested: Jenbacher #1 & #3 Proposed Test Dates: September 4 & 5, 2024 Project No. AST-2024-3767 Prepared By Alliance Technical Group, LLC 3683 W 2270 S, Suite E West Valley City, UT 84120 86 of 99 Site Specific Test Plan Test Program Summary AST-2024-3767 Central Valley – Salt Lake City, UT Page i Regulatory Information Permit No. DAQE-AN104140015-21 Regulatory Citation 40 CFR 60, Subpart JJJJ Source Information Source Name Source ID Target Parameters GE Jenbacher Model JMS 612- F28F02 Generator Engine Jenbacher #1 NOx, CO, VOC, NMHC GE Jenbacher Model JMS 612- F28F02 Generator Engine Jenbacher #3 Contact Information Test Location Test Company Central Valley Water Reclamation Facility Wastewater Treatment Plant 800 W Central Valley Road Salt Lake City, UT 84119-3379 Facility Contact Bryan Mansell mansellb@cvwrf.org (801) 973-9100 Alliance Technical Group, LLC 3683 W 2270 S, Suite E West Valley City, UT 84120 Project Manager Charles Horton charles.horton@alliancetg.com (352) 663-7568 Field Team Leader Alan Jensen alan.jensen@alliancetg.com (847) 220-3949 (subject to change) QA/QC Manager Kathleen Shonk katie.shonk@alliancetg.com (812) 452-4785 Test Plan/Report Coordinator Delaine Spangler delaine.spangler@alliancetg.com 87 of 99 Site Specific Test Plan Table of Contents AST-2024-3767 Central Valley – Salt Lake City, UT Page ii TABLE OF CONTENTS 1.0 Introduction ................................................................................................................................................. 1-1 1.1 Facility and Process Descriptions ................................................................................................................ 1-1 1.2 Project Team ............................................................................................................................................... 1-1 1.3 Safety Requirements ................................................................................................................................... 1-1 2.0 Summary of Test Program .......................................................................................................................... 2-1 2.1 General Description ..................................................................................................................................... 2-1 2.2 Process/Control System Parameters to be Monitored and Recorded ........................................................... 2-1 2.3 Proposed Test Schedule............................................................................................................................... 2-1 2.4 Emission Limits ........................................................................................................................................... 2-2 2.5 Test Report .................................................................................................................................................. 2-3 3.0 Testing Methodology .................................................................................................................................. 3-1 3.1 U.S. EPA Reference Test Methods 1 and 2 – Sampling/Traverse Points and Volumetric Flow Rate ........ 3-1 3.2 U.S. EPA Reference Test Method 3A – Oxygen/Carbon Dioxide .............................................................. 3-1 3.3 U.S. EPA Reference Test Method 320 – Moisture Content, Nitrogen Oxides, Carbon Monoxide, Volatile Organic Compounds and Non-Methane Hydrocarbons ........................................................................................... 3-2 3.4 U.S. EPA Reference Test Method 205 – Gas Dilution System Certification .............................................. 3-2 3.5 Quality Assurance/Quality Control – U.S. EPA Reference Test Method 3A.............................................. 3-2 3.6 Quality Assurance/Quality Control – U.S. EPA Reference Method 320 .................................................... 3-3 4.0 Quality Assurance Program ......................................................................................................................... 4-1 4.1 Equipment ................................................................................................................................................... 4-1 4.2 Field Sampling ............................................................................................................................................ 4-2 LIST OF TABLES Table 1-1: Project Team ........................................................................................................................................... 1-1 Table 2-1: Program Outline and Tentative Test Schedule ........................................................................................ 2-2 Table 2-2: Emission Limits ...................................................................................................................................... 2-2 Table 3-1: Source Testing Methodology .................................................................................................................. 3-1 88 of 99 Site Specific Test Plan Introduction AST-2024-3767 Central Valley – Salt Lake City, UT Page 1-1 1.0 Introduction Alliance Technical Group, LLC (Alliance) was retained by Central Valley Wastewater Reclamation Facility (Central Valley) to conduct compliance testing at the Wastewater Treatment Plant in Salt Lake City, Utah. Portions of the facility are subject to provisions of the 40 CFR 60, Subpart JJJJ and the Utah Department of Environmental Quality, Division of Air Quality (UDAQ) Approval Order (AO) DAQE-AN104140015-21. Testing will be conducted to determine the emission rates of nitrogen oxides (NOx), carbon monoxide (CO), volatile organic compounds (VOC) minus formaldehyde, and non-methane hydrocarbons (NMHC) from the exhausts of two (2) GE Jenbacher Model JSM 612-F28F02 engines designated as Jenbacher #1 and Jenbacher #3. This site-specific test plan (SSTP) has been prepared to address the notification and testing requirements of the UDAQ permit and the NSPS. 1.1 Facility and Process Descriptions Central Valley operates two (2) GE Jenbacher Model JMS 612-F28F02 generator engines. Each engine is rated at 2,509 horsepower (hp) each. The engines can be fired on natural gas or digester gas. Jenbacher #1 and #3 are the subject of this test program and will be fired on a mixed gas of blended digester gas and natural gas. 1.2 Project Team Personnel planned to be involved in this project are identified in the following table. Table 1-1: Project Team Central Valley Personnel Bryan Mansell Regulatory Agency UDAQ Alliance Personnel Alan Jensen other field personnel assigned at time of testing event 1.3 Safety Requirements Testing personnel will undergo site-specific safety training for all applicable areas upon arrival at the site. Alliance personnel will have current OSHA or MSHA safety training and be equipped with hard hats, safety glasses with side shields, steel-toed safety shoes, hearing protection, fire resistant clothing, and fall protection (including shock corded lanyards and full-body harnesses). Alliance personnel will conduct themselves in a manner consistent with Client and Alliance’s safety policies. A Job Safety Analysis (JSA) will be completed daily by the Alliance Field Team Leader. 89 of 99 Site Specific Test Plan Summary of Test Programs AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-1 2.0 Summary of Test Program To satisfy the requirements of the UDAQ permit and the NSPS, the facility will conduct a performance test program to determine the compliance status of two (2) GE Jenbacher Model JSM 612-F28F02 engines designated as Jenbacher #1 and Jenbacher #3. 2.1 General Description All testing will be performed in accordance with specifications stipulated in U.S. EPA Reference Test Methods 1, 2, 3A, and 320. Table 2-1 presents an outline and tentative schedule for the emissions testing program. The following is a summary of the test objectives. • Testing will be performed to demonstrate compliance with the UDAQ permit and 40 CFR 60, Subpart JJJJ. • Emissions testing will be conducted on the exhaust of Jenbacher #1 and Jenbacher #3. • Performance testing will be conducted while the engines are fired on a mixed gas of blended digester gas and natural gas. • Each of the three (3) test runs will be 60 minutes in duration. • The VOC measurements will not include formaldehyde. • Concurrent oxygen (O2), carbon dioxide (CO2) and moisture content (H2O) will be collected during each test run and combined with facility data to calculate emission rates in grams per break horsepower hour (g/bhp-hr). 2.2 Process/Control System Parameters to be Monitored and Recorded Plant personnel will collect operational and parametric data at least once every 15 minutes during the testing. The following list identifies the measurements, observations and records that will be collected during the testing program: • Ambient Temperature (°F) • Barometric Pressure (“HgA) • Relative Humidity (%) • Compressor Process Conditions • Engine Operating Load • Fuel Consumption 2.3 Proposed Test Schedule Table 2-1 presents an outline and tentative schedule for the emissions testing program. 90 of 99 Site Specific Test Plan Summary of Test Programs AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-2 Table 2-1: Program Outline and Tentative Test Schedule Testing Location Parameter US EPA Method No. of Runs Run Duration Est. Onsite Time DAY 1 – September 3, 2024 Equipment Setup & Pretest QA/QC Checks 6 hr DAY 2 – September 4, 2024 Jenbacher #1 VFR 1-2 3 60 min 8 hr O2 / CO2 3A BWS 320 NOx CO VOC 1 NMHC DAY 3 – September 5, 2024 Jenbacher #3 VFR 1-2 3 60 min 10 hr O2 / CO2 3A BWS 320 NOx CO VOC 1 NMHC DAY 4 – September 6, 2024 Contingency Day (if needed) 1 VOC measurements will not include formaldehyde 2.4 Emission Limits Emission limits for each pollutant are below. Table 2-2: Emission Limits Source Pollutant Citation Jenbacher #1 Jenbacher #3 NOx – 0.55 g/bhp-hr Permit CO – 2.50 g/bhp-hr VOC – 1.0 g/bhp-hr NMHC – 0.3 g/bhp-hr 91 of 99 Site Specific Test Plan Summary of Test Programs AST-2024-3767 Central Valley – Salt Lake City, UT Page 2-3 2.5 Test Report The final test report must be submitted within 60 days of the completion of the performance test and will include the following information. • Introduction – Brief discussion of project scope of work and activities. • Results and Discussion – A summary of test results and process/control system operational data with comparison to regulatory requirements or vendor guarantees along with a description of process conditions and/or testing deviations that may have affected the testing results. • Methodology – A description of the sampling and analytical methodologies. • Sample Calculations – Example calculations for each target parameter. • Field Data – Copies of actual handwritten or electronic field data sheets. • Quality Control Data – Copies of all instrument calibration data and/or calibration gas certificates. • Process Operating/Control System Data – Process operating and control system data (as provided by Central Valley) to support the test results. 92 of 99 Site Specific Test Plan Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 3-1 3.0 Testing Methodology This section provides a description of the sampling and analytical procedures for each test method that will be employed during the test program. All equipment, procedures and quality assurance measures necessary for the completion of the test program meet or exceed the specifications of each relevant test method. The emission testing program will be conducted in accordance with the test methods listed in Table 3-1. Table 3-1: Source Testing Methodology Parameter U.S. EPA Reference Test Methods Notes/Remarks Volumetric Flow Rate 1 & 2 Full Velocity Traverses Oxygen / Carbon Dioxide 3A Instrumental Analysis Moisture Content / Nitrogen Oxides / Carbon Monoxide / Volatile Organic Compounds / Non-Methane Hydrocarbons 320 FTIR – Continuous Sampling Gas Dilution System Certification 205 -- All stack diameters, depths, widths, upstream and downstream disturbance distances and nipple lengths will be measured on site with a verification measurement provided by the Field Team Leader. 3.1 U.S. EPA Reference Test Methods 1 and 2 – Sampling/Traverse Points and Volumetric Flow Rate The sampling location and number of traverse (sampling) points will be selected in accordance with U.S. EPA Reference Test Method 1. To determine the minimum number of traverse points, the upstream and downstream distances will be equated into equivalent diameters and compared to Figure 1-2 in U.S. EPA Reference Test Method 1. Full velocity traverses will be conducted in accordance with U.S. EPA Reference Test Method 2 to determine the average stack gas velocity pressure, static pressure and temperature. The velocity and static pressure measurement system will consist of a pitot tube and inclined manometer. The stack gas temperature will be measured with a K- type thermocouple and pyrometer. Stack gas velocity pressure and temperature readings will be recorded during each test run. The data collected will be utilized to calculate the volumetric flow rate in accordance with U.S. EPA Reference Test Method 2. 3.2 U.S. EPA Reference Test Method 3A – Oxygen/Carbon Dioxide The oxygen (O2) and carbon dioxide (CO2) testing will be conducted in accordance with U.S. EPA Reference Test Method 3A. Data will be collected online and reported in one-minute averages. The sampling system will consist of a stainless steel probe, Teflon sample line(s), gas conditioning system and the identified gas analyzer. The gas conditioning system will be a non-contact condenser used to remove moisture from the stack gas. If an unheated Teflon sample line is used, then a portable non-contact condenser will be placed in the system directly after the probe. Otherwise, a heated Teflon sample line will be used. The quality control measures are described in Section 3.5. 93 of 99 Site Specific Test Plan Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 3-2 3.3 U.S. EPA Reference Test Method 320 – Moisture Content, Nitrogen Oxides, Carbon Monoxide, Volatile Organic Compounds and Non-Methane Hydrocarbons The concentrations of moisture content (BWS), nitrogen oxides (NOx), carbon monoxide (CO), volatile organic compounds (VOC) and non-methane hydrocarbons (NMHC) will be determined in accordance with U.S. EPA Reference Test Method 320. Each source gas stream will be extracted at a constant rate through a heated probe, heated filter and heated sample line and analyzed with an MKS MultiGas 2030 FTIR operated by a portable computer. The computer has FTIR spectra of calibration gases stored on the hard drive. These single component calibration spectra are used to analyze the measured sample spectra. The gas components to be measured will be selected from the spectra library and incorporated into the analytical method. The signal amplitude, linearity, and signal to noise ratio will be measured and recorded to document analyzer performance. A leak check will be performed on the sample cell. The instrument path length will be verified using ethylene as the Calibration Transfer Standard. Dynamic spiking will be performed using a certified standard of the target compound or appropriate surrogate in nitrogen with sulfur hexafluoride blended as a tracer to calculate the dilution factor. All test spectra, interferograms, and analytical method information are recorded and stored with the calculated analytical results. The quality control measures are described in Section 3.6. 3.4 U.S. EPA Reference Test Method 205 – Gas Dilution System Certification A calibration gas dilution system field check will be conducted in accordance with U.S. EPA Reference Method 205. An initial three (3) point calibration will be conducted, using individual Protocol 1 gases, on the analyzer used to complete the dilution system field check. Multiple dilution rates and total gas flow rates will be utilized to force the dilution system to perform two dilutions on each mass flow controller. The diluted calibration gases will be sent directly to the analyzer, and the analyzer response will be recorded in an electronic field data sheet. A mid-level supply gas, with a cylinder concentration within 10% of one of the gas divider settings described above, will be introduced directly to the analyzer, and the analyzer response recorded in an electronic field data sheet. The cylinder concentration and the analyzer response must agree within 2%. These steps will be repeated three (3) times. The average analyzer response must agree within 2% of the predicted gas concentration. No single injection shall differ more than 2% from the average instrument response for that dilution. 3.5 Quality Assurance/Quality Control – U.S. EPA Reference Test Method 3A Cylinder calibration gases will meet EPA Protocol 1 (+/- 2%) standards. Copies of all calibration gas certificates will be included in the Quality Assurance/Quality Control Appendix of the report. Low Level gas will be introduced directly to the analyzer. After adjusting the analyzer to the Low Level gas concentration and once the analyzer reading is stable, the analyzer value will be recorded. This process will be repeated for the High Level gas. For the Calibration Error Test, Low, Mid, and High Level calibration gases will be sequentially introduced directly to the analyzer. The Calibration Error for each gas must be within 2.0 percent of the Calibration Span or 0.5% absolute difference. High or Mid Level gas (whichever is closer to the stack gas concentration) will be introduced at the probe and the time required for the analyzer reading to reach 95 percent or 0.5% (whichever was less restrictive) of the gas concentration will be recorded. The analyzer reading will be observed until it reaches a stable value, and this value will be recorded. Next, Low Level gas will be introduced at the probe and the time required for the analyzer reading to decrease to a value within 5.0 percent or 0.5% (whichever was less restrictive) will be recorded. If the Low Level gas is zero gas, the acceptable response must be 5.0 percent of the upscale gas concentration or 0.5% (whichever was less restrictive). The analyzer reading will be observed until it reaches a stable value and this value will be 94 of 99 Site Specific Test Plan Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 3-3 recorded. The measurement system response time and initial system bias will be determined from these data. The System Bias for each gas must be within 5.0 percent of the Calibration Span or 0.5% absolute difference. High or Mid Level gas (whichever is closer to the stack gas concentration) will be introduced at the probe. After the analyzer response is stable, the value will be recorded. Next, Low Level gas will be introduced at the probe, and the analyzer value will be recorded once it reaches a stable response. The System Bias for each gas must be within 5.0 percent of the Calibration Span or 0.5% absolute difference or the data is invalidated and the Calibration Error Test and System Bias must be repeated. The Drift between pre- and post-run System Bias must be within 3 percent of the Calibration Span or 0.5% absolute difference or the Calibration Error Test and System Bias must be repeated. To determine the number of sampling points, a gas stratification check will be conducted prior to initiating testing. The pollutant concentrations will be measured at twelve traverse points (as described in Method 1) or three points (16.7, 50.0 and 83.3 percent of the measurement line). Each traverse point will be sampled for a minimum of twice the system response time. If the pollutant concentration at each traverse point do not differ more than 5% or 0.5 0.3% (whichever is less restrictive) of the average pollutant concentration, then single point sampling will be conducted during the test runs. If the pollutant concentration does not meet these specifications but differs less than 10% or 0.5% from the average concentration, then three (3) point sampling will be conducted (stacks less than 7.8 feet in diameter - 16.7, 50.0 and 83.3 percent of the measurement line; stacks greater than 7.8 feet in diameter – 0.4, 1.0, and 2.0 meters from the stack wall). If the pollutant concentration differs by more than 10% or 0.5% from the average concentration, then sampling will be conducted at a minimum of twelve (12) traverse points. Copies of stratification check data will be included in the Quality Assurance/Quality Control Appendix of the report. A Data Acquisition System with battery backup will be used to record the instrument response in one (1) minute averages. The data will be continuously stored as a *.CSV file in Excel format on the hard drive of a computer. At the completion of testing, the data will also be saved to the Alliance server. All data will be reviewed by the Field Team Leader before leaving the facility. Once arriving at Alliance’s office, all written and electronic data will be relinquished to the report coordinator and then a final review will be performed by the Project Manager. 3.6 Quality Assurance/Quality Control – U.S. EPA Reference Method 320 EPA Protocol 1 Calibration Gases – Cylinder calibration gases used will meet EPA Protocol 1 (+/- 2%) standards or will be certified standards. After providing ample time for the FTIR to reach the desired temperature and to stabilize, zero gas (nitrogen) will be introduced directly to the instrument sample port. While flowing nitrogen the signal amplitude will be recorded, a background spectra will be taken, a linearity check will be performed and recorded, the peak to peak noise and the root mean square in the spectral region of interest will be measured and a screenshot will be recorded. Following the zero gas checks, room air will be pulled through the sample chamber and the line width and resolution will be verified to be at 1879 cm-1, the peak position will be entered and the FWHH will be recorded (screenshot). Following these checks, another background spectra will be recorded and the calibration transfer standard (CTS) 95 of 99 Site Specific Test Plan Testing Methodology AST-2024-3767 Central Valley – Salt Lake City, UT Page 3-4 will be introduced directly to the instrument sample port. The CTS instrument recovery will be recorded and the instrument mechanical response time will be measured. Next, stack gas will be introduced to the FTIR through the sampling system and several scans will be taken until a stable reading will be achieved. The native concentration of our surrogate or target spiking analyte will be recorded. Spike gas will be introduced to the sampling system at a constant flow rate ≤ 10% of the total sample flow rate and a corresponding dilution ratio will be calculated along with a system response time. Matrix spike recovery spectra will be recorded and will be within the ± 30% of the calculated value of the spike concentration that the method requires. The matrix spike recovery will be conducted once at the beginning of the testing and the CTS recovery procedures will be repeated following each test run. The corresponding values will be recorded. 96 of 99 Site Specific Test Plan Quality Assurance Program AST-2024-3767 Central Valley – Salt Lake City, UT Page 4-1 4.0 Quality Assurance Program Alliance follows the procedures outlined in the Quality Assurance/Quality Control Management Plan to ensure the continuous production of useful and valid data throughout the course of this test program. The QC checks and procedures described in this section represent an integral part of the overall sampling and analytical scheme. Adherence to prescribed procedures is quite often the most applicable QC check. 4.1 Equipment Field test equipment is assigned a unique, permanent identification number. Prior to mobilizing for the test program, equipment is inspected before being packed to detect equipment problems prior to arriving on site. This minimizes lost time on the job site due to equipment failure. Occasional equipment failure in the field is unavoidable despite the most rigorous inspection and maintenance procedures. Therefore, replacements for critical equipment or components are brought to the job site. Equipment returning from the field is inspected before it is returned to storage. During the course of these inspections, items are cleaned, repaired, reconditioned and recalibrated where necessary. Calibrations are conducted in a manner, and at a frequency, which meets or exceeds U.S. EPA specifications. The calibration procedures outlined in the U.S. EPA Methods, and those recommended within the Quality Assurance Handbook for Air Pollution Measurement Systems: Volume III (EPA-600/R-94/038c, September 1994) are utilized. When these methods are inapplicable, methods such as those prescribed by the American Society for Testing and Materials (ASTM) or other nationally recognized agency may be used. Data obtained during calibrations is checked for completeness and accuracy. Copies of calibration forms are included in the report. The following sections elaborate on the calibration procedures followed by Alliance for these items of equipment. • Dry Gas Meter and Orifice. A full meter calibration using critical orifices as the calibration standard is conducted at least semi-annually, more frequently if required. The meter calibration procedure determines the meter correction factor (Y) and the meter’s orifice pressure differential (ΔH@). Alliance uses approved Alternative Method 009 as a post-test calibration check to ensure that the correction factor has not changed more than 5% since the last full meter calibration. This check is performed after each test series. • Pitot Tubes and Manometers. Type-S pitot tubes that meet the geometric criteria required by U.S. EPA Reference Test Method 2 are assigned a coefficient of 0.84 unless a specific coefficient has been determined from a wind tunnel calibration. If a specific coefficient from a wind tunnel calibration has been obtained that coefficient will be used in lieu of 0.84. Standard pitot tubes that meet the geometric criteria required by U.S. EPA Reference Test Method 2 are assigned a coefficient of 0.99. Any pitot tubes not meeting the appropriate geometric criteria are discarded and replaced. Manometers are verified to be level and zeroed prior to each test run and do not require further calibration. • Temperature Measuring Devices. All thermocouple sensors mounted in Dry Gas Meter Consoles are calibrated semi-annually with a NIST-traceable thermocouple calibrator (temperature simulator) and verified during field use using a second NIST-traceable meter. NIST-traceable thermocouple calibrators are calibrated annually by an outside laboratory. • Nozzles. Nozzles are measured three (3) times prior to initiating sampling with a caliper. The maximum difference between any two (2) dimensions is 0.004 in. • Digital Calipers. Calipers are calibrated annually by Alliance by using gage blocks that are calibrated annually by an outside laboratory. 97 of 99 Site Specific Test Plan Quality Assurance Program AST-2024-3767 Central Valley – Salt Lake City, UT Page 4-2 • Barometer. The barometric pressure is obtained from a nationally recognized agency or a calibrated barometer. Calibrated barometers are checked prior to each field trip against a mercury barometer. The barometer is acceptable if the values agree within ± 2 percent absolute. Barometers not meeting this requirement are adjusted or taken out of service. • Balances and Weights. Balances are calibrated annually by an outside laboratory. A functional check is conducted on the balance each day it is use in the field using a calibration weight. Weights are re-certified every two (2) years by an outside laboratory or internally. If conducted internally, they are weighed on a NIST traceable balance. If the weight does not meet the expected criteria, they are replaced. • Other Equipment. A mass flow controller calibration is conducted on each Environics system annually following the procedures in the Manufacturer’s Operation manual. A methane/ethane penetration factor check is conducted on the total hydrocarbon analyzers equipped with non-methane cutters every six (6) months following the procedures in 40 CFR 60, Subpart JJJJ. Other equipment such as probes, umbilical lines, cold boxes, etc. are routinely maintained and inspected to ensure that they are in good working order. They are repaired or replaced as needed. 4.2 Field Sampling Field sampling will be done in accordance with the Standard Operating Procedures (SOP) for the applicable test method(s). General QC measures for the test program include: • Cleaned glassware and sample train components will be sealed until assembly. • Sample trains will be leak checked before and after each test run. • Appropriate probe, filter and impinger temperatures will be maintained. • The sampling port will be sealed to prevent air from leaking from the port. • Dry gas meter, ΔP, ΔH, temperature and pump vacuum data will be recorded during each sample point. • An isokinetic sampling rate of 90-110% will be maintained, as applicable. • All raw data will be maintained in organized manner. • All raw data will be reviewed on a daily basis for completeness and acceptability. 98 of 99 Last Page of Report 99 of 99 Jen 1 Nox CO VOC 2024 Reference Methods 2, 3A, 6C, 7E, 10, & 19 Source Information Company Name Central Valley Water Reclamation Facility Company Contact:Bryan Mansell Contact Phone No.(801) 657-9466 Stack Designation:Jenbacher #1 Test & Review Dates Test Date:9/4/2024 & 9/5/2024 Review Date: 9/24/2024 Observer:Unobserved Reviewer:Paul Morris Emission Limits Emission Rates VOC NOX CO VOC NOX CO lbs./MMBtu g/bHP-hr 0.3 0.6 2.5 0.11 0.523 2.189 ppm Percent %O2 Correction as a whole # Test Information Heat Input Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static) fuel flow rate (Btu/hr.) Heat Input (Btu/hr.) 20.00 2.182 0.84 25.61 3.57 Contractor Information Contact: Charles Horton Contracting Company: Alliance Technical Group, LLC Address: 3683 W 2270 S, Suite E West Valley City, UT 84120 Phone No.: (464) 352-7568 Project No.: Division of Air Quality Instrumental Reference Methods - Gaseous Measurements Round Method 19 - F factors for Coal, Oil, and Gas Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu Diluent F factor used O2 CO2 Anthrocite 2 Bituminous 2 Lignite Natural Propane Butane 10100 COAL OIL GAS 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 Wet CEM Correct For O2 CO2 Interference w/CO Yes Yes Yes Jen 1 Nox CO VOC 2024 Division of Air Quality NSPS Relative Accuracy Performance Specification Test - CEMS Certification Central Valley Water Reclamation Facility Jenbacher #1 Average Emission Dry VOC NOX CO lbs./MMbtu Average % concentration lbs./hr.0.56 2.63 11.00 CO2 O2 ppm or % 13.77 61.33 421.63 8.49 10.53 0.11 0.52 2.19 Run 1 Enter O2 or CO2 Dry VOC NOX CO CO2 O2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.634E-06 7.322E-06 3.065E-05 lbs./hr.0.59 2.64 11.05 8.49 10.55 ppm or %14.30 61.30 421.60 8.56 10.45 Run 2 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.600E-06 7.322E-06 3.068E-05 lbs./hr.0.57 2.62 10.96 8.50 10.54 ppm or %14.00 61.30 421.90 8.56 10.44 Raw Value Run 3 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2279 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.485E-06 7.334E-06 3.064E-05 lbs./hr.0.53 2.63 10.99 8.49 10.52 ppm or %13.00 61.40 421.400 8.59 10.43 Raw Value Run 4 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value Run 5 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value C For Cal Drift Raw Value g/bHP-hr C For Cal Drift C For Cal Drift C For Cal Drift C For Cal Drift O2 CO2 Clear lbs./MMBTU Jen 1 Nox CO VOC 2024 Calibration Error Test Test Date September 4, 2024 O2 CS - Cal. Span 23.99 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.00% Passed Cal. RR02538 09/19/31 Mid-level 11.00 10.95 0.05 0.21% Passed Cal. EB0069884 04/01/32 High-level 23.99 23.99 0.00 0.00% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of CS - Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.85% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO2 CS - Cal. Span 23.90 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 -0.02 0.02 0.084% Passed Cal. RR02538 09/19/31 Mid-level 10.99 11.19 0.20 0.837% Passed Cal. EB0069884 04/01/32 High-level 23.90 23.98 0.08 0.335% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.98% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 VOC CS - Cal. Span 20.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 10.00 10.00 0.00 0.000% Passed Cal. High-level 20.00 20.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 NOx CS - Cal. Span 100.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 50.00 50.00 0.00 0.000% Passed Cal. High-level 100.00 100.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO 2.5 CS - Cal. Span 500.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 250.00 250.00 0.00 0.000% Passed Cal. High-level 500.00 500.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Valid Cal Gas Valid Cal Gas Valid Cal Gas Valid Cal Gas Jen 1 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % Unprotected CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.99 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CDir CMA 20.00 100.00 500.00 10.99 11.00 Calibration Error Test Cs - Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.19 10.95 High-Level 20.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmdv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmdv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0 0 0 0.02 0.01 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.08 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.17% Difference 0.00 0.00 0.00 0.11 0.04 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 VOC NOX CO CO2 O2 NOX 14.3 61.3 421.60 8.6 10.5 CO 71.5% 61.3% 84.3% 35.8% 43.6% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.03 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.09 10.89 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.42% 0.25% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.04% 0.00% Drift Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.04% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.182 25.61 3.57 25.87 288 8.49 10.55 80.97 29.78 28.59 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 4.4630 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs (ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1583 83.660 400,996 10,953 360,495.47 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.41 1.187 287 2 1.34 1.158 288 3 1.37 1.170 290 4 1.36 1.166 291 5 1.42 1.192 290 6 1.28 1.131 289 7 1.25 1.118 287 8 1.31 1.145 288 9 1.43 1.196 289 10 1.37 1.170 290 11 1.42 1.192 291 12 1.36 1.166 288 13 1.35 1.162 287 14 1.33 1.153 286 15 1.30 1.140 286 16 1.18 1.086 285 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog CO Calibration Gas Failed Bias Dialog Jen 1 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.99 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 20.00 100.00 500.00 10.99 11.00 Calibration Error Test Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.19 10.95 High-Level 20.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmdv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmdv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.03 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0 0 0 0.01 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.09 10.89 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.42% 0.25% Difference 0 0 0 0.1 0.06 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 VOC NOX CO CO2 O2 NOX 14.0 61.3 421.90 8.6 10.4 CO 70.0% 61.3% 84.4% 35.9% 43.5% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.01 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.12 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.17% Difference 0.0 0.0 0.0 0.1 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.00% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.13% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 295 8.50 10.54 80.97 29.78 28.59 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1536 83.70 397,535 10,958 357,384.15 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.37 1.170 295 2 1.44 1.200 296 3 1.41 1.187 296 4 1.34 1.158 295 5 1.31 1.145 294 6 1.27 1.127 294 7 1.29 1.136 295 8 1.33 1.153 294 9 1.42 1.192 296 10 1.28 1.131 296 11 1.40 1.183 295 12 1.34 1.158 295 13 1.29 1.136 294 14 1.31 1.145 295 15 1.28 1.131 296 16 1.22 1.105 296 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog Failed Bias Dialog Jen 1 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.99 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 20.00 100.00 500.00 10.99 11.00 Calibration Error Test Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.19 10.95 High-Level 20.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.01 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0 0 0 0.01 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.12 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.17% Difference 0 0 0 0.07 0.04 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 VOC NOX CO CO2 O2 NOX 13.0 61.4 421.40 8.6 10.4 CO 65.0% 61.4% 84.3% 35.9% 43.5% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.08%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.12 10.90 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.21% Difference 0.0 0.0 0.0 0.1 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.04% 0.04% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.00% 0.04% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 296 8.49 10.52 80.99 29.78 28.63 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.0980 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1555 83.85 397,622 10,978 358,655.35 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.45 1.204 297 2 1.41 1.187 298 3 1.26 1.122 297 4 1.25 1.118 296 5 1.43 1.196 295 6 1.32 1.149 295 7 1.35 1.162 296 8 1.37 1.170 297 9 1.34 1.158 298 10 1.41 1.187 297 11 1.42 1.192 297 12 1.24 1.114 297 13 1.26 1.122 296 14 1.33 1.153 296 15 1.29 1.136 294 16 1.25 1.118 295 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Cal Error Dialog Failed Drift Dialog Failed Bias Dialog Jen 1 NMHC 2024 Reference Methods 2, 3A, 6C, 7E, 10, & 19 Source Information Company Name Central Valley Water Reclamation Facility Company Contact:Bryan Mansell Contact Phone No.(801) 657-9466 Stack Designation:Jenbacher #1 Test & Review Dates Test Date:9/4/2024 & 9/5/2024 Review Date: 9/25/2024 Observer:Unobserved Reviewer:Paul Morris Emission Limits Emission Rates NMHC NOX CO NMHC NOX CO lbs./MMBtu g/bHP-hr 0.3 0.6 2.5 0.26 0.000 0.000 ppm Percent %O2 Correction as a whole # Test Information Heat Input Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static) fuel flow rate (Btu/hr.) Heat Input (Btu/hr.) 20.00 2.182 0.84 25.61 3.57 Contractor Information Contact: Charles Horton Contracting Company: Alliance Technical Group, LLC Address: 3683 W 2270 S, Suite E West Valley City, UT 84120 Phone No.: (464) 352-7568 Project No.: Round Division of Air Quality Instrumental Reference Methods - Gaseous Measurements Method 19 - F factors for Coal, Oil, and Gas Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu Diluent F factor used O2 CO2 Anthrocite 2 Bituminous 2 Lignite Natural Propane Butane 10100 COAL OIL GAS 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 Wet CEM Correct For O2 CO2 Interference w/CO Yes Yes Yes Jen 1 NMHC 2024 Division of Air Quality NSPS Relative Accuracy Performance Specification Test - CEMS Certification Central Valley Water Reclamation Facility Jenbacher #1 Average Emission Dry NMHC NOX CO lbs./MMbtu Average % concentration lbs./hr.1.32 CO2 O2 ppm or % 32.20 8.49 10.54 0.26 Run 1 Enter O2 or CO2 Dry NMHC NOX CO CO2 O2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 3.679E-06 lbs./hr.1.33 8.49 10.55 ppm or %32.20 8.56 10.45 Run 2 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr.8.50 10.54 ppm or %8.56 10.44 Raw Value Run 3 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2279 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 3.679E-06 lbs./hr.1.32 8.48 10.53 ppm or %32.20 8.58 10.44 Raw Value Run 4 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value Run 5 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value C For Cal Drift Raw Value g/bHP-hr C For Cal Drift C For Cal Drift C For Cal Drift C For Cal Drift O2 CO2 Clear lbs./MMBTU Jen 1 NMHC 2024 Calibration Error Test Test Date September 4, 2024 O2 CS - Cal. Span 23.99 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.00% Passed Cal. RR02538 09/19/31 Mid-level 11.00 10.95 0.05 0.21% Passed Cal. EB0069884 04/01/32 High-level 23.99 23.99 0.00 0.00% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of CS - Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.85% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO2 CS - Cal. Span 23.90 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 -0.02 0.02 0.084% Passed Cal. RR02538 09/19/31 Mid-level 10.99 11.19 0.20 0.837% Passed Cal. EB0069884 04/01/32 High-level 23.90 23.98 0.08 0.335% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.98% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 NMHC CS - Cal. Span 50.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 25.00 25.00 0.00 0.000% Passed Cal. High-level 50.00 50.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 NOx CS - Cal. Span 100.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 50.00 50.00 0.00 0.000% Passed Cal. High-level 100.00 100.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO 2.5 CS - Cal. Span 500.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 250.00 250.00 0.00 0.000% Passed Cal. High-level 500.00 500.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Valid Cal Gas Valid Cal Gas Valid Cal Gas Valid Cal Gas Jen 1 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % Unprotected CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.99 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CDir CMA 50.00 100.00 500.00 10.99 11.00 Calibration Error Test Cs - Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.19 10.95 High-Level 50.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmdv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmdv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0 0 0 0.02 0.01 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.08 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.17% Difference 0.00 0.00 0.00 0.11 0.04 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 32.2 8.6 10.5 CO 64.4% 0.0% 0.0% 35.8% 43.6% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.03 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.09 10.89 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.42% 0.25% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.04% 0.00% Drift Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.04% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.182 25.61 3.57 25.87 288 8.49 10.55 80.97 29.78 28.59 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 4.4630 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs (ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1583 83.660 400,996 10,953 360,495.47 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.41 1.187 287 2 1.34 1.158 288 3 1.37 1.170 290 4 1.36 1.166 291 5 1.42 1.192 290 6 1.28 1.131 289 7 1.25 1.118 287 8 1.31 1.145 288 9 1.43 1.196 289 10 1.37 1.170 290 11 1.42 1.192 291 12 1.36 1.166 288 13 1.35 1.162 287 14 1.33 1.153 286 15 1.30 1.140 286 16 1.18 1.086 285 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog CO Calibration Gas Failed Bias Dialog Jen 1 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.99 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 50.00 100.00 500.00 10.99 11.00 Calibration Error Test Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.19 10.95 High-Level 50.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmdv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmdv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.03 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0 0 0 0.01 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.09 10.89 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.42% 0.25% Difference 0 0 0 0.1 0.06 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 8.6 10.4 CO 0.0% 0.0% 0.0% 35.9% 43.5% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.01 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.12 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.17% Difference 0.0 0.0 0.0 0.1 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.00% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.13% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 295 8.50 10.54 80.97 29.78 28.59 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1536 83.70 397,535 10,958 357,384.15 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.37 1.170 295 2 1.44 1.200 296 3 1.41 1.187 296 4 1.34 1.158 295 5 1.31 1.145 294 6 1.27 1.127 294 7 1.29 1.136 295 8 1.33 1.153 294 9 1.42 1.192 296 10 1.28 1.131 296 11 1.40 1.183 295 12 1.34 1.158 295 13 1.29 1.136 294 14 1.31 1.145 295 15 1.28 1.131 296 16 1.22 1.105 296 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog Failed Bias Dialog Jen 1 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.99 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 46.0% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 50.00 100.00 500.00 10.99 11.00 Calibration Error Test Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.19 10.95 High-Level 50.00 100.00 500.00 23.98 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.19 10.95 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 0.84% 0.21% ppmv Difference 0 0 0 0.2 0.05 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.33% 0.00% ppmv Difference 0 0 0 0.08 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.01 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.04% 0.04%± 5% of Span Difference 0 0 0 0.01 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.12 10.91 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.17% Difference 0 0 0 0.07 0.04 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 32.2 8.6 10.4 CO 64.4% 0.0% 0.0% 35.9% 43.5% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.08%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.12 10.90 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.21% Difference 0.0 0.0 0.0 0.1 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.04% 0.04% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.00% 0.04% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 296 8.48 10.53 80.99 29.78 28.63 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.0980 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1555 83.85 397,622 10,978 358,655.35 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.45 1.204 297 2 1.41 1.187 298 3 1.26 1.122 297 4 1.25 1.118 296 5 1.43 1.196 295 6 1.32 1.149 295 7 1.35 1.162 296 8 1.37 1.170 297 9 1.34 1.158 298 10 1.41 1.187 297 11 1.42 1.192 297 12 1.24 1.114 297 13 1.26 1.122 296 14 1.33 1.153 296 15 1.29 1.136 294 16 1.25 1.118 295 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Cal Error Dialog Failed Drift Dialog Failed Bias Dialog Jen 3 Nox CO VOC 2024 Reference Methods 2, 3A, 6C, 7E, 10, & 19 Source Information Company Name Central Valley Water Reclamation Facility Company Contact:Bryan Mansell Contact Phone No.(801) 657-9466 Stack Designation:Jenbacher #3 Test & Review Dates Test Date:9/5/2024 & 9/6/2024 Review Date: 9/25/2024 Observer:Unobserved Reviewer:Paul Morris Emission Limits Emission Rates VOC NOX CO VOC NOX CO lbs./MMBtu g/bHP-hr 0.3 0.6 2.5 0.11 0.460 2.194 ppm Percent %O2 Correction as a whole # Test Information Heat Input Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static) fuel flow rate (Btu/hr.) Heat Input (Btu/hr.) 20.00 2.182 0.84 25.61 4.1 Contractor Information Contact: Charles Horton Contracting Company: Alliance Technical Group, LLC Address: 3683 W 2270 S, Suite E West Valley City, UT 84120 Phone No.: (464) 352-7568 Project No.: Division of Air Quality Instrumental Reference Methods - Gaseous Measurements Round Method 19 - F factors for Coal, Oil, and Gas Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu Diluent F factor used O2 CO2 Anthrocite 2 Bituminous 2 Lignite Natural Propane Butane 10100 COAL OIL GAS 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 Wet CEM Correct For O2 CO2 Interference w/CO Yes Yes Yes Jen 3 Nox CO VOC 2024 Division of Air Quality NSPS Relative Accuracy Performance Specification Test - CEMS Certification Central Valley Water Reclamation Facility Jenbacher #3 Average Emission Dry VOC NOX CO lbs./MMbtu Average % concentration lbs./hr.0.54 2.31 11.03 CO2 O2 ppm or % 13.37 55.20 432.83 8.59 10.52 0.11 0.46 2.19 Run 1 Enter O2 or CO2 Dry VOC NOX CO CO2 O2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.634E-06 6.701E-06 3.065E-05 lbs./hr.0.57 2.35 10.77 8.08 10.72 ppm or %14.30 56.10 421.60 8.23 10.61 Run 2 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.531E-06 6.534E-06 3.177E-05 lbs./hr.0.53 2.25 10.95 8.86 10.43 ppm or %13.40 54.70 437.00 8.23 10.34 Raw Value Run 3 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2279 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 1.417E-06 6.546E-06 3.198E-05 lbs./hr.0.50 2.33 11.38 8.83 10.43 ppm or %12.40 54.80 439.900 9.02 10.36 Raw Value Run 4 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value Run 5 Dry VOC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value C For Cal Drift Raw Value g/bHP-hr C For Cal Drift C For Cal Drift C For Cal Drift C For Cal Drift O2 CO2 Clear lbs./MMBTU Jen 3 Nox CO VOC 2024 Calibration Error Test Test Date September 5, 2024 O2 CS - Cal. Span 23.99 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.00% Passed Cal. RR02538 09/19/31 Mid-level 11.00 11.00 0.00 0.00% Passed Cal. EB0069884 04/01/32 High-level 23.99 23.99 0.00 0.00% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of CS - Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.85% 100% of Cal. Span High-level 100.00% Test Date September 5, 2024 CO2 CS - Cal. Span 23.90 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 -0.02 0.02 0.084% Passed Cal. RR02538 09/19/31 Mid-level 10.90 11.20 0.30 1.255% Passed Cal. EB0069884 04/01/32 High-level 23.90 23.94 0.04 0.167% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.61% 100% of Cal. Span High-level 100.00% Test Date September 5, 2024 VOC CS - Cal. Span 20.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 10.00 10.00 0.00 0.000% Passed Cal. High-level 20.00 20.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 5, 2024 NOx CS - Cal. Span 100.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 50.00 50.00 0.00 0.000% Passed Cal. High-level 100.00 100.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 5, 2024 CO 2.5 CS - Cal. Span 500.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 250.00 250.00 0.00 0.000% Passed Cal. High-level 500.00 500.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Valid Cal Gas Valid Cal Gas Valid Cal Gas Valid Cal Gas Jen 3 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #3 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % Unprotected CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.90 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CDir CMA 20.00 100.00 500.00 10.90 11.00 Calibration Error Test Cs - Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.20 11.00 High-Level 20.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmdv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmdv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.08%± 5% of Span Difference 0 0 0 0 0.02 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.12 10.90 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.33% 0.42% Difference 0.00 0.00 0.00 0.08 0.10 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/5/2024 SO2 VOC NOX CO CO2 O2 NOX 14.3 56.1 421.60 8.2 10.6 CO 71.5% 56.1% 84.3% 34.4% 44.2% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.09 10.88 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.50% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.04% Drift Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.13% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #3 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.182 25.61 4.10 25.91 284 8.08 10.72 81.20 29.72 28.54 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 4.1878 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs (ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1236 80.950 390,647 10,598 351,191.41 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.02 1.010 281 2 1.16 1.077 283 3 1.18 1.086 284 4 1.25 1.118 285 5 1.31 1.145 285 6 1.41 1.187 284 7 1.33 1.153 284 8 1.35 1.162 284 9 0.98 0.990 283 10 1.15 1.072 283 11 1.19 1.091 284 12 1.34 1.158 285 13 1.39 1.179 285 14 1.44 1.200 286 15 1.36 1.166 286 16 1.40 1.183 287 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog CO Calibration Gas Failed Bias Dialog Jen 3 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #3 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.90 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 20.00 100.00 500.00 10.90 11.00 Calibration Error Test Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.20 11.00 High-Level 20.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmdv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmdv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.04%± 5% of Span Difference 0 0 0 0 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.09 10.88 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.50% Difference 0 0 0 0.11 0.12 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/5/2024 SO2 VOC NOX CO CO2 O2 NOX 13.4 54.7 437.00 9.0 10.3 CO 67.0% 54.7% 87.4% 37.8% 43.1% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.13 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.29% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.08% 0.00% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.17% 0.21% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #3 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 4.10 25.91 285 8.86 10.43 80.71 29.83 28.64 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1050 79.53 383,279 10,412 344,567.99 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.11 1.054 288 2 1.08 1.039 287 3 1.05 1.025 286 4 1.22 1.105 286 5 1.23 1.109 285 6 1.25 1.118 284 7 1.44 1.200 285 8 1.41 1.187 287 9 1.11 1.054 286 10 1.23 1.109 286 11 1.24 1.114 286 12 1.20 1.095 285 13 1.16 1.077 285 14 1.25 1.118 284 15 1.28 1.131 283 16 1.31 1.145 282 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog Failed Bias Dialog Jen 3 Nox CO VOC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility VOC NOX CO CO2 O2 Jenbacher #3 CS Calibration Span 20.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 10.00 50.00 250.00 10.90 11.00 High-Level 20.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 20.00 100.00 500.00 10.90 11.00 Calibration Error Test Measured Concentration VOC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 10.00 50.00 250.00 11.20 11.00 High-Level 20.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 20.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0 0 0 0.02 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.13 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.29% Difference 0 0 0 0.07 0.07 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/5/2024 SO2 VOC NOX CO CO2 O2 NOX 12.4 54.8 439.90 9.0 10.4 CO 62.0% 54.8% 88.0% 37.7% 43.2% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values VOC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.08%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 20.00 100.00 500.00 11.14 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.25% 0.29% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.04% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.04% 0.00% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #3 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 4.10 25.91 284 8.83 10.43 80.74 29.83 28.67 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.0980 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1365 81.65 394,389 10,690 355,738.93 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.14 1.068 282 2 1.17 1.082 282 3 1.22 1.105 283 4 1.18 1.086 285 5 1.24 1.114 284 6 1.27 1.127 284 7 1.41 1.187 285 8 1.45 1.204 284 9 1.32 1.149 283 10 1.32 1.149 284 11 1.41 1.187 285 12 1.32 1.149 285 13 1.26 1.122 284 14 1.24 1.114 283 15 1.34 1.158 283 16 1.40 1.183 282 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Cal Error Dialog Failed Drift Dialog Failed Bias Dialog Jen 3 NMHC 2024 Reference Methods 2, 3A, 6C, 7E, 10, & 19 Source Information Company Name Central Valley Water Reclamation Facility Company Contact:Bryan Mansell Contact Phone No.(801) 657-9466 Stack Designation:Jenbacher #1 Test & Review Dates Test Date:9/4/2024 & 9/5/2024 Review Date: 9/25/2024 Observer:Unobserved Reviewer:Paul Morris Emission Limits Emission Rates NMHC NOX CO NMHC NOX CO lbs./MMBtu g/bHP-hr 0.3 0.6 2.5 0.22 0.000 0.000 ppm Percent %O2 Correction as a whole # Test Information Heat Input Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static) fuel flow rate (Btu/hr.) Heat Input (Btu/hr.) 20.00 2.182 0.84 25.61 3.57 Contractor Information Contact: Charles Horton Contracting Company: Alliance Technical Group, LLC Address: 3683 W 2270 S, Suite E West Valley City, UT 84120 Phone No.: (464) 352-7568 Project No.: Round Division of Air Quality Instrumental Reference Methods - Gaseous Measurements Method 19 - F factors for Coal, Oil, and Gas Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu Diluent F factor used O2 CO2 Anthrocite 2 Bituminous 2 Lignite Natural Propane Butane 10100 COAL OIL GAS 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 Wet CEM Correct For O2 CO2 Interference w/CO Yes Yes Yes Jen 3 NMHC 2024 Division of Air Quality NSPS Relative Accuracy Performance Specification Test - CEMS Certification Central Valley Water Reclamation Facility Jenbacher #1 Average Emission Dry NMHC NOX CO lbs./MMbtu Average % concentration lbs./hr.1.12 CO2 O2 ppm or % 28.00 8.57 10.52 0.22 Run 1 Enter O2 or CO2 Dry NMHC NOX CO CO2 O2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 3.953E-06 lbs./hr.1.39 8.05 10.71 ppm or %34.60 8.20 10.60 Run 2 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2280 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 2.868E-06 lbs./hr.0.99 8.83 10.39 ppm or %25.10 8.20 10.30 Raw Value Run 3 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)EBW, HP 2279 E=Cd x Fc x (100 / % CO2d) lbs./cu.ft 2.776E-06 lbs./hr.0.99 8.81 10.47 ppm or %24.30 9.00 10.40 Raw Value Run 4 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value Run 5 Dry NMHC NOX CO CO2 O2 Atomic Weight 44 46 28 lbs./MMBtu (O2)E=Cd x Fd x (20.9/(20.9-%O2d)) lbs./MMBtu (CO2)E=Cd x Fc x (100 / % CO2d) lbs./cu.ft lbs./hr. ppm or %Raw Value C For Cal Drift Raw Value g/bHP-hr C For Cal Drift C For Cal Drift C For Cal Drift C For Cal Drift O2 CO2 Clear lbs./MMBTU Jen 3 NMHC 2024 Calibration Error Test Test Date September 4, 2024 O2 CS - Cal. Span 23.99 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.00% Passed Cal. RR02538 09/19/31 Mid-level 11.00 11.00 0.00 0.00% Passed Cal. EB0069884 04/01/32 High-level 23.99 23.99 0.00 0.00% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of CS - Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.85% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO2 CS - Cal. Span 23.90 Units % Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 -0.02 0.02 0.084% Passed Cal. RR02538 09/19/31 Mid-level 10.90 11.20 0.30 1.255% Passed Cal. EB0069884 04/01/32 High-level 23.90 23.94 0.04 0.167% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 45.61% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 NMHC CS - Cal. Span 50.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 25.00 25.00 0.00 0.000% Passed Cal. High-level 50.00 50.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 NOx CS - Cal. Span 100.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 50.00 50.00 0.00 0.000% Passed Cal. High-level 100.00 100.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Test Date September 4, 2024 CO 2.5 CS - Cal. Span 500.00 Units ppm Cylinder No. Expiration Date Cal. Gas CV- Certified Concentration CDir or CS - Measured Concentration Difference ACE Eq. 7E-1 Analyzer Cal. Error Status Low-level 0.00 0.00 0.00 0.000% Passed Cal. Mid-level 250.00 250.00 0.00 0.000% Passed Cal. High-level 500.00 500.00 0.00 0.000% Passed Cal. % of Span Sec. 8.2.1 Cal Gas Verification 0 to 20% of Cal. Span Low-Level 0.00% 40 to 60% of Cal. Span Mid-level 50.00% 100% of Cal. Span High-level 100.00% Valid Cal Gas Valid Cal Gas Valid Cal Gas Valid Cal Gas Jen 3 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % Unprotected CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.90 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CDir CMA 50.00 100.00 500.00 10.90 11.00 Calibration Error Test Cs - Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.20 11.00 High-Level 50.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmdv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmdv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.08%± 5% of Span Difference 0 0 0 0 0.02 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.12 10.90 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.33% 0.42% Difference 0.00 0.00 0.00 0.08 0.10 Pass or Failed Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 34.6 8.2 10.6 CO 69.2% 0.0% 0.0% 34.3% 44.2% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.09 10.88 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.50% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.04% Drift Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.13% 0.08% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.182 25.61 3.57 25.87 284 8.05 10.71 81.24 29.72 28.54 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 4.1941 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs (ft/sec.)Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1236 81.010 390,348 10,606 350,923.14 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.02 1.010 281 2 1.16 1.077 283 3 1.18 1.086 284 4 1.25 1.118 285 5 1.31 1.145 285 6 1.41 1.187 284 7 1.33 1.153 284 8 1.35 1.162 284 9 0.98 0.990 283 10 1.15 1.072 283 11 1.19 1.091 284 12 1.34 1.158 285 13 1.39 1.179 285 14 1.44 1.200 286 15 1.36 1.166 286 16 1.40 1.183 287 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog CO Calibration Gas Failed Bias Dialog Jen 3 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.90 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 50.00 100.00 500.00 10.90 11.00 Calibration Error Test Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.20 11.00 High-Level 50.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmdv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmdv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmdv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 -0.02 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.00% 0.04%± 5% of Span Difference 0 0 0 0 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.09 10.88 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.46% 0.50% Difference 0 0 0 0.11 0.12 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 25.1 9.0 10.3 CO 50.2% 0.0% 0.0% 37.7% 42.9% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.13 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.29% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.08% 0.00% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.17% 0.21% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 285 8.83 10.39 80.78 29.83 28.64 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.1010 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1050 79.59 382,991 10,420 344,309.32 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.11 1.054 288 2 1.08 1.039 287 3 1.05 1.025 286 4 1.22 1.105 286 5 1.23 1.109 285 6 1.25 1.118 284 7 1.44 1.200 285 8 1.41 1.187 287 9 1.11 1.054 286 10 1.23 1.109 286 11 1.24 1.114 286 12 1.20 1.095 285 13 1.16 1.077 285 14 1.25 1.118 284 15 1.28 1.131 283 16 1.31 1.145 282 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Drift Dialog Failed Cal Error Dialog Failed Bias Dialog Jen 3 NMHC 2024 Division of Air Quality Stack Test Review of Central Valley Water Reclamation Facility NMHC NOX CO CO2 O2 Jenbacher #1 CS Calibration Span 50.00 100.00 500.00 23.90 23.99 Units ppm ppm ppm % % CV - Cylinder Value: NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 0.00 0.00 Mid-Level 25.00 50.00 250.00 10.90 11.00 High-Level 50.00 100.00 500.00 23.90 23.99 0 to 20% of Cal. Span 0.00% 0.00% 0.00% 0.00% 0.00% 40 to 60% of Cal. Span 50.0% 50.0% 50.0% 45.6% 45.9% 100% of Cal. Span 100.0% 100.0% 100.0% 100.0% 100.0% Cdir - Enter Actual Up-scale Cylinder Value Used To Correct Emission Concentration. CMA 50.00 100.00 500.00 10.90 11.00 Calibration Error Test Measured Concentration NMHC NOX CO CO2 O2 Low-Level 0.00 0.00 0.00 -0.02 0.00 Mid-Level 25.00 50.00 250.00 11.20 11.00 High-Level 50.00 100.00 500.00 23.94 23.99 Enter Up-scale Analyzer Response to be used during testing. ACE Eq. 7E-1 50.00 100.00 500.00 11.20 11.00 Low-Level 0.00% 0.00% 0.00% 0.08% 0.00% ppmv Difference 0 0 0 0.02 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Mid-Level 0.00% 0.00% 0.00% 1.26% 0.00% ppmv Difference 0 0 0 0.3 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. High-Level 0.00% 0.00% 0.00% 0.17% 0.00% ppmv Difference 0 0 0 0.04 0 Status Passed Cal. Passed Cal. Passed Cal. Passed Cal.Passed Cal. Pre-Test Sampling System Bias Initial Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.01 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.04%± 5% of Span Difference 0 0 0 0.02 0.01 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.13 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.29% 0.29% Difference 0 0 0 0.07 0.07 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Raw Test Data Time Start Stop Test Date:9/4/2024 SO2 NMHC NOX CO CO2 O2 NOX 24.3 9.0 10.4 CO 48.6% 0.0% 0.0% 37.7% 43.4% CO2/O2 Post-Test System Bias 7E-2 SB=(Cs - Cdir)/CS x 100 Final Values NMHC NOX CO CO2 O2 CO - Low-Level 0.00 0.00 0.00 0.00 0.02 System Bias. SBi - Zero Bias 0.00% 0.00% 0.00% 0.08% 0.08%± 5% of Span Difference 0.0 0.0 0.0 0.0 0.0 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. CM - Up-scale Gas 50.00 100.00 500.00 11.14 10.93 SBi - Up-Scale Bias 0.00% 0.00% 0.00% 0.25% 0.29% Difference 0.0 0.0 0.0 0.1 0.1 Pass or Invalid Run Passed Cal. Passed Cal. Passed Cal. Passed Cal. Passed Cal. Calibration Drift % of Span - D=ABS(SBf - SBi) Low-Level Drift 0.00% 0.00% 0.00% 0.00% 0.04% Response Spec. Difference 0.0 0.0 0.0 0.0 0.0 3% of Span Pass or Re-Calibrate Pass Pass Pass Pass Pass Up-scale Gas Drift 0.00% 0.00% 0.00% 0.04% 0.00% Difference 0.0 0.0 0.0 0.0 0.0 Pass or Re-Calibrate Pass Pass Pass Pass Pass Jenbacher #1 Flow & Moisture As ft^2 Pbar Pq (static) Ps Avg Ts F CO2 - FCO2 O2 N2+C Md Ms 2.18 25.61 3.57 25.87 284 8.81 10.47 80.72 29.83 28.67 Y Cp Vm cf Vlc AVG Tm F Vm std Vw std Bws S Bws 0.0000 0.84 0.0980 0.999 Load - Megawatts Avg. √∆P's Vs Qsw scfh wet Qa acfm Qsd dscfh Heat Input Btu/hr Low Mid High 1.1365 81.72 394,134 10,699 355,508.43 Enert > #1 - Times Date Point No.∆P √∆P ts F tm F (in) tm F (out) Final Vf Initial Vi 1 1.14 1.068 282 2 1.17 1.082 282 3 1.22 1.105 283 4 1.18 1.086 285 5 1.24 1.114 284 6 1.27 1.127 284 7 1.41 1.187 285 8 1.45 1.204 284 9 1.32 1.149 283 10 1.32 1.149 284 11 1.41 1.187 285 12 1.32 1.149 285 13 1.26 1.122 284 14 1.24 1.114 283 15 1.34 1.158 283 16 1.40 1.183 282 17 18 19 20 21 22 23 24 Failed Bias Dialog Failed Cal Error Dialog Failed Drift Dialog Failed Bias Dialog