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Address Info: 1150 O Street, P.O. Box 758, Greeley, CO 80632 | Phone:
(970) 400-4225
| Fax: (970) 336-7233 | Email:
egesick@weld.gov
| Official: Esther Gesick -
Clerk to the Board
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20142940.tiff
coPHE '.., COLORADO CO Department of Public Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150 0 St PO Box 758 RECEIVED Greeley,y, CO 80632 September 18, 2014 SEP 2 3 2014 WCOMMISSIONERS S LD COUNTY E S Dear Sir or Madam: On September 21, 2014, the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company, LLC - State Seventy Holes K-3 Production Facility, in the The Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, j; 71 , 4_y-jam Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure fir F { ,. d -,*, 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe I ,.z- 'c John W. Hickenlooper, Governor I Larry Wolk, MD,MSPH, Executive Director and Chief Medical Officer . k'', ROItG -1eV1tlAD 2014-2940 q - 2-q - li4 CC: ITL,PW, FL g/23 CDPHE Public Notice Of A Proposed Project CO Or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - State Seventy Holes K-3 Production Facility - Weld County Released To: The Greeley Tribune On: September 18, 2014 Published: September 21, 2014 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company, LLC Facility: State Seventy Holes K-3 Production Facility Oil and gas exploration and production facility Lot 1 Sec 3, T4N, R62W Weld County The proposed project or activity is as follows: The applicant proposes to operate an oil and gas production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 14WE0462 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1 ' ®® CO ORADO ,PIuA ISTATEOFOLORADO w "3F1 � A4 W „cop-2,, •LOR 4 D RT *FP %L C HEALTH AND ENVIRONMENT FQ % AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692-3150 ; ,* *18964 CONSTRUCTION PERMIT PERMIT NO: 14WE0462 E0462 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State Seventy Holes K-3 Production Facility, located in Lot 1 of Section 3, Township 4N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Truck 006 Truck Condensate Loadout Loadout FUG 007 Fugitive VOC equipment leaks One emergency flare with a minimum combustion efficiency FL-1 008 of 95%.The flare is not enclosed. The emergency flare is used during periods when the pipeline is not available. One low-pressure separator controlled by two enclosed Sep-1 009 flares. Each flare has a minimum combustion efficiency of 95%. One (1) pneumatic water transfer pump, Sandpiper G1 F P-1 010 model, Serial #4016694, rated at 600 scf/hr, controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. Point 010: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS)in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et sect), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: AIRS ID: 123/9C09 Page 1 of 16 olor Depa en P li ealth and Environment it Pollution Control Division REQUIREMENTS TN TION 1. AIRS Point 008: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submittina a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. AIRS Point 008: The following information shall be provided to the Division within fifteen (15) days after commencement of operation. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 3. AIRS Point 008: Within one hundred and eighty days (180) after commencement of operation, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 4. AIRS Points 006, 007, 009, 010: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 5. AIRS Points 006, 007, 009, 010: Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 6. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (Hi) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 7. AIRS Point 009:Within one hundred and eighty(180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from the low pressure separator. The operator shall use the gas flow rate AIRS ID: 123/9C09 Page 2 of 16 olor epa en }• Pli ealth and Environment f .it Pollution Control Division listed in the a• f at flow • "=,: is installed, not to exceed one hundred and eighty(180) days after issuance of this permit. 8. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 9. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 10. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO, VOC CO Emission Type Truck Loadout 006 --- 6.5 --- Point FUG 007 --- 7.8 --- Fugitive FL-1 008 --- 5.2 3.1 Point Sep-1 009 --- 4.0 1.1 Point P-1 010 --- 2.1 1.3 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 11. Point 007: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent extended gas analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 12. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID AIRS ID: 123/9C09 Page 3 of 16 olor epa en P Ii ealth and Environment it Pollution Control Division FL-1 VOC Sep-1 009 Enclosed Flare VOC P-1 010 Enclosed Flare VOC PROCESS LIMITATIONS AND RECORDS 13. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Equipment Point Process Parameter Annual Limit ID Truck 006 Condensate Loaded 70,080 BBL Loadout FUG 007 NA NA FL-1 008 Total Gas Vented from Separator to 12.8 MMSCF Emergency Flare Sep-1 009 Total Gas Vented from Low-Pressure 3.2 MMSCF Separator P-1 010 Natural Gas Consumed 5.3 MMSCF Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility,for Division review. 14. AIRS Point 009: Upon installation of the flow meter required under Condition 7, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from each low pressure separator using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented from each low-pressure separator. The owner or operator shall use monthly throughput records to demonstrate compliance with the limits specified in Condition 13 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 15. AIRS Points 006, 008, 009, 010: The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.)(State only enforceable) 16. Visible emissions shall not exceed twenty percent(20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. &4.) AIRS ID: 123/9C09 Page 4 of 16 olor Depa en P! •Ii "' ealth and Environment it Pollution Control Division 17. This source • t e eq of ' .` • .ation No. 2. (State only enforceable) 18. No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 19. This source is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. The operator shall comply with all applicable requirements of Section XII. 20. AIRS Point 006: This source is located in an ozone non-attainment or attainment- maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 21. AIRS Point 006: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 21 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 22. AIRS Point 006: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 23. AIRS Point 007: This source is subject to Regulation No. 7, Section XVII.F. leak detection and repair requirements, which include but are not limited to: XVII.F.1. As of the compliance date specified in XVII.F.4, the provisions of Section XVII.F. shall apply in lieu of any directed inspection and maintenance program requirements established pursuant to Regulation Number 3, Part B, Section I I I.D.2. XVII.F.4. Requirements for well production facilities XVII.F.4.b. Owners or operators of well production facilities constructed before October 15, 2014, must identify leaks from components using an approved instrument monitoring method within ninety (90) days of the Phase-In Schedule in Table 4; within thirty (30) days for well production facilities subject to monthly approved instrument monitoring method inspections; or by January 1, 2016, for well production facilities subject to a one time approved instrument monitoring method inspection. Thereafter, approved instrument monitoring method and AVO AIRS ID: 123/9C09 Page 5 of 16 Depa en P li ealth and Environment it Pollution Control Division inspeDolor n in wit Inspection Frequencies in Table 4. XVII.F.4.c. The estimated uncontrolled actual VOC emissions from the highest emitting storage tank at the well production facility determines the frequency at which inspections must be performed. Table 4—Well Production Facility Component Inspections Thresholds(per XVII.F.4.c)—Well Production Facilities Approved Instrument AVO with Storage Tanks Monitoring method Inspection Phase-In (tpy) Inspection Frequency Frequency Schedule > 0 and < 6 One time Monthly January 1, 2016 > 6 and < 12 Annually Monthly January 1, 2016 > 12 and < 50 Quarterly Monthly January 1, 2015 > 50 Monthly January 1, 2015 XVII.F.5. If a component is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor the component until it becomes feasible to do so. XVII.F.6 Leaks requiring repair: Leaks must be identified utilizing the methods listed in Section XVII.F.6. Only leaks detected pursuant to Section XVII.F.6. require repair under Section XVII.F.7. XVII.F.6.a. For EPA Method 21 monitoring, or other Division approved quantitative instrument based monitoring, at facilities constructed before May 1, 2014, a leak is any concentration of hydrocarbon above 2,000 parts per million (ppm) not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation, except for well production facilities where a leak is defined as any concentration of hydrocarbon above 500 ppm not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation. XVII.F.6.c. For infra-red camera and AVO monitoring, or other Division approved non- quantitative instrument based monitoring, a leak is any detectable emissions not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation. XVII.F.6.e. For leaks identified using an approved instrument monitoring method or AVO, owners or operators have the option of either repairing the leak in accordance with the repair schedule set forth in Section XVII.F.7. or conducting follow-up monitoring using EPA Method 21 within five (5) working days of the leak detection. If the follow-up EPA Method 21 monitoring shows that the emission is a leak as defined in Section XVII.F.6., the leak must be repaired and remonitored in accordance with Section XVII.F.7. AIRS ID: 123/9C09 Page 6 of 16 olor Depa en 3 P Ii ealth and Environment it Pollution Control Division XVII.F.7. Rep 'cam - r • e � � � =ter �4 .�. XVII.F.7.a. First attempt to repair a leak must be made no later than five (5) working days after discovery, unless parts are unavailable, the equipment requires shutdown to complete repair, or other good cause exists. If pads are unavailable, they must be ordered promptly and the repair must be made within fifteen (15) working days of receipt of the parts. If shutdown is required, the leak must be repaired during the next scheduled shutdown. If delay is attributable to other good cause, repairs must be completed within fifteen (15) working days after the cause of delay ceases to exist. XVII.F.7.b. Within fifteen (15) working days of completion of a repair, the leak must be remonitored to verify the repair was effective. XVII.F.7.c. Leaks discovered pursuant to the leak detection methods of Section XVII.F.6. shall not be subject to enforcement by the Division unless the owner or operator fails to perform the required repairs in accordance with Section XVII.F.7. XVII.F.8. Recordkeeping: The owner or operator of each facility subject to the leak detection and repair requirements in Section XVII.F. must maintain the following records for a period of two (2) years and make them available to the Division upon request. XVII.F.8.a. Documentation of the initial approved instrument monitoring method inspection for new well production facilities; XVII.F.8.b. The date and site information for each inspection; XVII.F.8.c. A list of the leaking components and the monitoring method(s) used to determine the presence of the leak; XVII.F.8.d. The date of first attempt to repair the leak and, if necessary, any additional attempt to repair the leak; XVII.F.8.e. The date the leak was repaired; XVII.F.8.f. The delayed repair list, including the basis for placing leaks on the list; XVII.F.8.g. The date the leak was remonitored to verify the effectiveness of the repair, and the results of the remonitoring; and XVII.F.8.h. A list of components that are designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.F.5., an explanation stating why the component is so designated, and the plan for monitoring such component(s). XVII.F.9. Reporting: The owner or operator of each facility subject to the leak detection and repair requirements in Section XVII.F. must submit reports as specified in Section XVII.F.9. 24. Point 007: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). Upon the compliance dated specified in Regulation No. 7, Section XVII.F.4., the provisions of Section XVII.F. shall apply in lieu of RACT requirements established pursuant to Regulation Number 3, Part B, Section III.D.2. This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: AIRS ID: 123/9C09 Page 7 of 16 olor DepFlow thioa. Direct cti a shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection must be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 25. AIRS Points 008, 009 and 010: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 26. AIRS Point 007:Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the AIRS ID: 123/9C09 Page 8 of 16 olor Depa en P .li "' ealth and Environment y it Pollution Control Division number of co t a ed " liquir - ice, "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 27. AIRS Point 008: Within one hundred and eighty (180) days after commencement of operation, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare when the flare is receiving gas from the separator. (Reference: Regulation No. 1, Section I I.A.1 &4) 28. AIRS Point 009: The operator shall complete an initial site specific extended gas analysis of the natural gas vented from the low-pressure separator at this site in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4- trimethylpentane content (weight fraction) of this emission stream used in the permit application. Results of testing shall be used to determine site-specific emission factors using Division approved methods. Results of site-specific sampling and analysis shall be submitted to the Division as part of the self-certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. Periodic Testing Requirements 29. AIRS Point 007: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 30. AIRS Point 010: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section IV.A and without applying for a revision to this permit or obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. 31. AIRS Point 010: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 32. AIRS Point 010: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 33. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30'" whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO„) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per AIRS ID: 123/9C09 Page 9 of 16 olor epa en P li ealth and Environment it Pollution Control Division year, jJ a e f one n per year or more or five percent,whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per, year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 34. Federal regulatory program requirements(i.e. PSD, NANSR)shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 35. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 36. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide"final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. 37. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. AIRS ID: 123/9C09 Page 10 of 16 olor Depa en P •li x ealth and Environment it Pollution Control Division 38. Unless specifies ed g spea,4'5. onditions contained in this permit have been determined by the APCD to be necessary to assure compliance with the provisions of Section 25-7-114.5(7)(a), C.R.S. 39. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 40. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 41. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122 (civil penalties), -122.1 (criminal penalties), C.R.S. By: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9O09 Page 11 of 16 olor epa en P li ealth and Environment 1 it Pollution Control Division Notes to Permit Holder me o e a . 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice(APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpanename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWraooer 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) _ Benzene 71432 147 No 147 n-Hexane 110543 746 Yes 746 006 Toluene 108883 338 Yes 338 Ethylbenzene 100414 74 No 74 Xylenes 1330207 274 Yes 274 2,2,4- 540841 90 No 90 trimethylpentane Benzene 71432 74 No 74 n-Hexane 110543 374 Yes 374 007 Toluene 108883 135 No 135 Ethylbenzene 100414 29 No 29 Xylenes 1330207 102 No 102 Benzene 71432 496 Yes 25 n-Hexane 110543 3,012 Yes 151 008 Toluene 108883 383 Yes 19 Ethylbenzene 100414 47 No 2 Xylenes 1330207 118 No 6 009 Benzene 71432 341 Yes 17 AIRS ID: 123/9O09 Page 12 of 16 3 olor / •epa en! . P .Ii ' ealth and Environment °it Pollution Control Division 102 Toluene 108883 227 No 11 Ethylbenzene 100414 27 No 1 Xylenes 1330207 52 No 3 Benzene 71432 204 No 10 n-Hexane 110543 1,237 Yes 62 010 Toluene 108883 157 No 8 Ethylbenzene 100414 19 No 1 Xylenes 1330207 49 No 2 5) The emission levels contained in this permit are based on the following emission factors: Point 006: Emission Factors- Uncontrol led Pollutant lb/BBL loaded Source VOC 0.1868 AP-42 Benzene 0.0021 AP-42 n-Hexane 0.0106 AP-42 Toluene 0.0048 AP-42 Ethylbenzene 0.0011 AP-42 Xylenes 0.0039 AP-42 2,2,4- 0.0013 AP-42 trimethylpentane The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46*S*P*M/T S =0.6 (Submerged loading: dedicated normal service) P (true vapor pressure)=4.71 psia M (vapor molecular weight) =66.2 lb/Ib-mol T(temperature of liquid loaded)= 524 'R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 007: Component Gas Heavy Oil Light Oil Water/Oil Connectors 946 0 338 329 Flanges 49 0 8 10 Open-ended Lines 27 0 3 1 Pump Seals 4 0 0 1 Valves 129 0 45 32 Other 66 0 7 10 VOC Content(wt. 0.2723 1 0.9977 1 AIRS ID: 123/9C09 Page 13 of 16 olor- ■epa en . P .li ealth and Environment it Pollution Control Division fraction �- Benzene Content(wt. 0.0006 0 0.0112 0.0012 fraction Toluene Content(wt. 0.0005 0 0.0258 0.0003 fraction Ethylbenzene (wt. 0.0001 0 0.0057 0.0001 fraction Xylenes Content(wt. 0.0002 0 0.0209 0.0001 fraction n-hexane Content(wt. 0.0039 0 0.057 0.0001 fraction *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors(kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R-95-017 Table 2-4 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 008: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx --- 0.068 0.068 AP-42 (Ib/MMBTU) CO --- 0.37 0.37 AP-42 (lb/MMBTU) VOC 27.3 16,328 816.40 Gas Analysis Benzene 0.06 38.751 1.9375 Gas Analysis Toluene 0.05 29.906 1.4953 Gas Analysis Ethylbenzene 0.006 3.6417 0.1821 Gas Analysis Xylenes 0.015 9.2444 0.4622 Gas Analysis n-hexane 0.39 235.35 11.767 Gas Analysis Emission factors for CO and NOx found in AP-42 Table 13.5-1.A HHV of 1,304 BTU/scf was used for calculations. AIRS ID: 123/9C09 Page 14 of 16 olor ° Depa r~ en'`. P' .h ealth and Environment •it Pollution Control Division Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx(lb/MMBTU) 0.068 0.068 AP-42 CO(Ib/MMBTU) 0.37 0.37 AP-42 VOC 56.8 49,638 2,481.9 Gas Analysis Benzene 0.12 105.12 5.2561 Gas Analysis Toluene 0.08 69.781 3.4891 Gas Analysis Ethylbenzene 0.01 8.4040 0.4202 Gas Analysis Xylenes 0.02 15.968 0.7984 Gas Analysis n-hexane 0.72 630.09 31.505 Gas Analysis • Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 9/11/2013 of the gas vented from low pressure separators at State Antelope J-F-28HNB, which is a different site, to estimate VOC and HAP content of the stream and a Promax model to estimate stream flow. The controlled VOC and HAP emissions factors for point 009 are based on a flare control efficiency of 95%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,880 BTU/scf was used for calculations. Point 010: Emission Emission Factors - Factors - Uncontrolled Controlled Pollutant lb/MMscf vented Ib/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (Ib/MMBTU) VOC 16,328 816.40 Gas Analysis Benzene 38.751 1.9375 Gas Analysis Toluene 29.906 1.4953 Gas Analysis Ethylbenzene 3.6417 0.1821 Gas Analysis Xylenes 9.2444 0.4622 Gas Analysis n-hexane 235.35 11.767 Gas Analysis The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10-Displacement Equation (10.4-3)." Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,304 BTU/scf was used for calculations. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: AIRS ID: 123/9C09 Page 15 of 16 olor- 1 eepa en . P 'Ii ealth and Environment it Pollution Control Division Applicable Status Requirement Operating Permit Synthetic Minor of:VOC NANSR Synthetic Minor of:VOC MACT HH Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfropoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart 7777—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification. AIRS ID: 12319C09 Page 16 of 16 Division Information l Engineer: Carissa Money Control Engineer: Chris Laplante Review Date: 09/11/2014 Application Date: 02/21/2014 Facility Identifiers Permit No. 14WE0462 County It 123 Weld AIRS Facility# 9C09 Facility Type: exploration and production facility 0 Located in the 8-hour non-attainment area? 0 True Minor Synthetic Minor for: 1 VOC F NOx F CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Seventy Holes K-3 Production Facility Source Location: Lot 1 of Section 3,Township 4N, Range 62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street,Suite 1500 Address y,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@honanzacrk.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Seventy Holes K-3 Production Facility,located in the Lot 1 of Section 3,Township 4N,Range 62W,Weld County,Colorado. Point Name Type Control Action Truck Newly 006 Loadout None reported ruck source Newly 007 FUG Fugitives None reported source Newly 008 FL-1 Separator Venting Flare reported Emergency flare when pipeline nc source Newly 009 Sep-1 Separator Venting Flare reported source Newly 010 P-1 Pump Flare reported source 006 Truck Condensate Loadout Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2,Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 4.71 psia Sales Oil Analysis documenting RVP 6.8 and AP- M Molecular Weight of Val 66.2 lb/lb-mole Sales oil analysis for RVP 6.8 and interpolating w T Liquid Temperature 524 deg.R EPA Tanks Met Data for Denver,CO L 4.449 lb/10^3 gal 1.87E-01 lb/bbl Annual requested Throughput 70080 BBL/yr 2943360 gal/yr Annual requested V0C emissions 13094 lb/yr 6.55 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0112 n-hexane 0.0570 Toluene 0.0258 Xylenes 0.0209 Ethylbenzen 0.0057 2,2,4-TMP 0.0069 Source: Pressurized oil analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.1868 lb/bbl 6.5 tpy 6.5 tpy AP-42 Benzene 0.0021 lb/bbl 147 lb/yr 147 lb/yr AP-42 n-Hexane 0.0106 lb/bbl 746 lb/yr 746 lb/yr AP-42 Toluene 0.0048 lb/bbl 338 lb/yr 338 lb/yr AP-42 Xylenes 0.0039 lb/bbl 274 lb/yr 274 lb/yr AP-42 Ethylbenzen 0.0011 lb/bbl 74 lb/yr 74 lb/yr AP-42 2,2,4-TMP 0.0013 lb/bbl 90 lb/yr 90 lb/yr AP-42 Regulatory Review !Regulation 7-Volatile Organic Compounds This facility is not considered a bulk plant(in Reg.7)because it does not distribute gasoline. 14WE0462 123/9C09 007 Fugitive equipment leaks Regulation 7 Information Operating Hours' 5760 hours/year Emission Factor Source EPA-053/R-06-017 Table 2-4 Control Efficiency Source' None Calculations Emission Factor(lag/hr- Emissions Service Component Type CountSource) Control(NO Pollutant Mass Fraction tlpy) Table 2-4 Table 2d Reg.3 Connectors 906 300E-0J 100E-05 00% VOC O2723 3 7605751 Flanges 49 3.90E-04 570E-06 00% Benzene 0000607 00009353 Open-Ended Lines 27 2,00E-03 1.50E-05 00% Toluene O000099 00068914 Gas Pump Seals 4 2401.03 3.50E-00 0 0% Ethybenzene 0.000061 0.0008424 Valves 129 4.50E-03 2.50E-05 0 0% Xylenes 0000154 0.0021268 Other 66 600E-03 120E-00 0 n-Hexane 0003931 00542887 Connectors 7 7.50E-06 7500-06 0 VOC 1 0 Flanges 7 390E-07 390E-07 00% Benzene 0 Open-Ended Lines 5 11.40E-047.20E-0600% Toluene 0 Heavy Cl Pump Seals 7 0.00E+00 0.00Ew0 0.0% Ettylbenzene 0 Valves 0 800E-06 800E-06 0.0% %ylenes 0 Other 0 320E-05 320E-05 00% n-Hexane 0 connectors 338 2.1➢E-04 750E-06 0 VOC 0.9977 23175116 Flanges 5 1.10E-04 240E-06 0.0% Benzene 0.5112 0025016 Open-Ended Cures 3 1.4➢E-03 1.40E-05 00% Toluene 0.3250 00599296 Light Oil Pump Seals 0 1.30E-02 3.10E-00 0.O% Ethyl enzene 00057 0.0132403 Valves 45 2.50E-03 190E-05 00% xylenes 00209 0.0485477 olner 7 750E-03 110E-00 0 n-Hexane 0057 0.1324027 Connectors 329 1.10004 107E-05 00% VOC 1 1730905 Flanges 10 290E-06 290E-06 00% Benzene 00012 00020771 walenoll Open-Ended Lines I 2.50E-0439.0E-06 Owns Toluene 0om 00005193 Pump Seals 1 2.4➢E-05 240E-05 00% Etnylbenzene 00001 00001731 Valves 32 9.80E-05 9.70E-06 00% xylenes 00001 00001731 Olber 10 1.40102 5.90E 05 00% n-Hexane 00001 00001731 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source VOC 7.81 thy 78 tpy EPA-45315-05-017 Table 2-4 Benzene 70 lb/yr 0.04 74 Iblyr EPAA53/R-95-017 Table 2-4 Toluene 131 lb/yr 0.07 13116/yr EPAA53/R-95-017 Table 2-4 Elhylbenzene 29 lb/yr 0.01 29!Myr EPAA53/R-95-017 Table 2-4 %ylenes 10216/yr 005 102 Ib/yr EPA-45315-95-017 Table 2-4 n-Hexane 370 lb/yr 0.19 370 Iblyr EPA-453/R-95-017 Table 2-4 Regulatory Applicability The dale of interest for determining whether the source is new or modified is therefore November 20,2007 One date Of Reg 3 the 8-hour ozone NA area designation).Since the site was built after the date above(operation began 11/20020131.thus source is considered neat or modified"Operator has agreed on the Division's standard conditions. VOC and HAP concentrations for gas service ate based on sales gas sample collected 12/17/20131mm 51015 Seventy Holes M-0-3HNB Since site-specific and vothin 1 year of application date.noinitial sampling required. 0dW00462 123/9009 One emergency flare with a minimum combustion efficiency of 95%. The flare is not enclosed.The emergency flare is 008 used during periods when the pipeline is not available. Equipment Description This source vents natural gas from: a well head separator when the sales gas pipeline is not available or during emergencies Emissions from this source are: routed to a flare 'Natural gas venting from a wet head separator when the sales gas pipeline is not available or dutinq emergencies.Emissions from this source are routed to Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=O•MW•Xx/C Ex=emissions of pollutant x 0=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas•MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(O) 12.8 MMscf/yr 1461.187215 scf/hr MW 22.7 Ibfb-mc4 0.035068493 MMscf/d mole% MW lbx/Ibmol mass fraction Ibllr lb/yr tpy Helium 0.01 4.0026 0.000 0.000 0.00 13.52 0.01 C02 2.16 44.01 0.951 0.042 3.66 32105.24 16.05 N2 0.97 28.013 0.272 0.012 1.05 9177.03 4.59 methane 73.02 16.041 11.713 0.516 45.16 395576.48 197.79 ethane 11.88 30.063 3.571 0.157 13.77 120600.76 60.30 propane 7.62 44.092 3.360 0.148 12.95 113471.17 58.74 isobutane 0.71 58.118 0.414 0.018 1.60 13989.05 6.99 n-butane 220 58.118 1.280 0.056 4.94 43239.06 21.62 isopentane 0.39 72.114 0.281 0.012 1.08 9474.14 4.14 n-pentane 0.49 72.114 0.353 0.016 1.36 11912.09 5.96 cyclopentane 0,04 70.13 0.025 0.001 0.10 847.93 0.42 n-Hexane 0.10 86.18 0.089 0.00393 0.34 3012.43 1.51 cyclohexane 0.03 84.16 0.022 0.001 0.08 741.85 0.37 Other hexanes 0.18 86.18 0.153 0.007 0.59 5172.07 2.59 heptanes 0.09 100.21 0.089 0.004 0.34 3001.96 1.50 methylcyclohexane 0,02 98.19 0.021 0.001 0.08 693.08 0.35 224-TMP 0.00 114.23 0.000 0.000 0.00 0.00 0.00 Benzene 0.02 78.12 0.015 0.00065 0.06 496.01 0.25 Toluene - 0.01 92.15 0.011 0.00050 0.04 382.80 0.19 Ethylbenzene 0.06 108.17 0.001 0.00008 0.01 48.81 0.02 Xylenes 0.00 106.17 0.004 0.00015 0.01 118.33 0.06 CB*Heavies 0.05 137.4837288 0.071 0.003 0.27 2400.56 1.20 VOC mass frac 0.273 Total VOC(Uncontrolled) 104.50 Notes Mole%,MW,and mass fractions are based on sales gas analysis collected 12/17/2013 from State Seventy Holes K-O-3HNB Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. 14WE0462 123/9009 One emergency flare with a minimum combustion efficiency of 95%. The flare is not enclosed.The emergency flare is 008 used during periods when the pipeline is not available. Flaring Information Equipment Description Flare to combust produced gas when ipeline is not available at this wellhead facility. Manufacturer TBD Model TBD Serial Number TAD Gas Heating Value 1304 Btu/scf Throughput 16691.2 MMBtu/Vr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress gas to sales line. Make TBD Model TBD Requested Control 95.00% Annual Bypass Tin 0.00% Backup Flare Overall Control I 95.00%' Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBW 0.37 Ph CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOL 16328 Ib/MMscf 81640 lb/MMscf 104.5 tpy 5.2 spy Gas Analysis Nox 007 Ib/MMBTU 0.07 lb/MMBTU 0.6 toy 0.6 spy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 3.1 toy 3.1 tpy AP-42 Benzene 38.751 lb/MMscf 1.9375 Ih/MMscf 496 lb/yr 25 lb/yr Gas Analysis n-Hexane 235.35 lb/MMscf 11.767 Ib/MMscf 3012 lb/yr 151 lb/yr Gas Analysis Toluene 29.906 Ib/MMscf 1.4953 lb/MMscf 383 lb/yr 19 lb/yr Gas Analysis Xylenes 92444 Ib/MMscf 0.462216/MMscf 118 lb/yr 6 lb/yr Gas Analysis Ethylbenzene 3.641716/MMscf 0.1521 lb/MMscf 47 lb/yr 2 lb/yr Gas Analysis Regulatory Applicability AOCC Regulation I This source is subject to the opacity requirements for flares in Section ll A.5'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AOCC Regulation 2 Section LA applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits. For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." 14WE0462 123/9C05 One low-pressure separator controlled by a VRU and two enclosed flares.Each flare has a minimum combustion 009 efficiency of 95%. Equipment Description This source vents natural gas from: a wet head separator Emissions from this source are: routed to a flare [Natural gas venting from a wet head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q•MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rale/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mot)al 60F and 1 atm Throughput(CO 32485584 MMscf/yr l 370.84 scf/br MW 33.1 Ibfl d I b-ro 0.00890016 MMscf/d mole% MW Ibxfbmol mass fraction Ib/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.61 44.01 1.149 0.035 1.12 9845.63 4.92 N2 0.11 28.013 0.031 0.001 0.03 264.12 0.13 methane 38.48 16.041 5.849 0.177 5.72 50136.68 25.07 ethane 24.32 30.063 7.311 0.221 7.15 62669.25 31.33 propane 22.81 44.092 10.059 0.304 9.84 86217.91 43.11 isabutane 2.37 58.118 1.376 0.042 1.35 11791.28 5.90 n-butane 7.25 58.118 4.216 0.127 4.13 38135.97 18.07 iscpentane 1.19 72.114 0.856 0.026 0.84 7340.15 3.67 n-pentane 1.48 72.114 1.064 0.032 1.04 9124.03 4.56 cydopentane 0.11 70.13 0.075 0.002 0.07 846.20 0.32 n-Hexane 0.28 86.18 0.239 0.00721 0.23 2048.89 1.02 cyclohexane 0.07 84.16 0.059 0.002 0.08 504.24 0.25 Other hexanes 0.48 86.18 0.411 0.012 0.40 3523.52 1.76 heptanes 0.21 100.21 0.210 0.006 0.21 1602.05 0.90 methylcyclohexane 0.05 98.19 0.050 0.002 0.05 425.88 0.21 224-TMP 0.00 11423 0.000 0.00000 0.00 0.98 0.00 Benzene 0.05 78.12 0.040 0.00120 0.04 341.49 0.17 Toluene 0.03 92.15 0.028 0.00080 0.03 226.69 0.11 ' EV646enxene 0.00 106.17 0003 0.00010 0.00 27.30 0.01 Xylenes 0.01 106.17 0.006 0.00018 0.01 51.87 0.03 C8+Heavies 0.11 116 0.122 0.004 0.12 1046.98 0.52 VOC mass frac 0.568 Total VOC(uncontrolled) 80.63 Notes Mole%,MW,and mass fractions are based on LP separator gas analysis collected 9/11/2013 from a different site,State Antelope J-F-28HN6.Source will r Emissions are based on 8760 hours of operation per year. Typically I calculate the average MW of C8+based an the average MW on the analysis for the gas.This method resulted in minimal emissions increase Source used MW of 116 for CB+.Since there is minimal difference in emissions,I used the source's values. 140610462 123/0009 One low-pressure separator controlled by a VRU and two enclosed flares.Each flare has a minimum combustion 009 efficiency of 95%. Flaring Information Equipment Description Flare to combust LP separator qas Manufacturer Leed Model L30-0100 Serial Number 21461&21462 Gas Heating Value 1880 Btu/scf Throughput 6107.289792 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress qas to sales line. Make Model Requested Control Efficiency Annual Bypass Time Backup J Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 jib NOX/MMBW 0.37 (lb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 496381b/MMscf 2481.9 lb/MMscf 80.6 tpy 4.0 tpy Gas Analysis Noy 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.2 tpy 0.2 tpy AP 42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.1 spy 1.1 spy AP-42 Benzene 105.121b/MMscf 5.2561 Ib/MMscf 341 lb/yr 171b/yr Gas Analysis n-Hexane 630.091b/MMscf 31.5051b/MMscf 2047 lb/yr 102 lb/yr Gas Analysis Toluene 69.78116/MMscf 3.4891 lb/MMscf 227 lb/yr 11 lb/yr Gas Analysis Xylenes 15.9681b/MMscf 0.7984 lb/MMscf 521b/yr 3 lb/yr Gas Analysis Ethylbenxene 8.404016/MMscf 0.420216/MMscf 271b/yr 1 lb/yr Gas Analysis Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." 14WE0462 123/9[09 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1F,Serial number 4016694).The pneumatic pump is controlled by 010 an enclosed flare with a minimum combustion efficiency of 95%. Pump Information Manufactur Sandpiper Model Number:G1F Serial Pump Number:4016694 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used ' consumptio Control Flare 95.00%Efficiency Calculations EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-31 Ex=Q'MW')0/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=5G of gas*MW of air Xx=mass fraction of x in gas • C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Q 600 scf/hr MW 22.7 lb/lb-mai Hours of Op. 6760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy CO2 2.18 44 0.0419 CO2 1.505 13180.217 6.590 nitrogen 0.97 28 0.0120 nitrogen 0.430 3766.569 1.883 methane 73.02 16.04 0.5159 methane 18.541 162423.468 81.212 ethane 11.88, 30.07 0.1573 ethane 5.654 49533.219 24.767 propane 7.62 44.09 0.1480 propane 5.319 46591.985 23.296 isobutane 071 58.12 0.0182 isobutane 0.656 5744.451 2.872 n-butane 2.20 58.12 0.0564 n-butane 2.027 17755.648 8.878 isopentane 0.39 72.15 0.0124 isopentane 0.444 3892.262 1.946 n-pentane 0.49 72.15 0.0155 n-pentane 0.559 4893.844 2.447 cyclopentane 0.04 70.15 0.0011 cyclopentane 0.040 348.279 0.174 n-hexane 0.10 86.18 0.0039 n-hexane 0.141 1236.981 0.618 cyclohexane 0.03 84.18 0.0010 cyclohexane 0.035 304.695 0.152 Other hexanes 0.18 86.18 0.0067 Other hexane, 0.242 2123.783 1.062 heptanes 0.09 100.21 0.0039 heptanes 0.141 1232.681 0.616 methylcyclohexa 0.02 98.19 0.0009 methylcyclohe 0.032 284.597 0.142 224-TMP 0.00 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 0.02 78.11 0.0006 Benzene 0.023 203.648 0.102 Toluene 0.01 92.14 0.0005 Toluene 0.018 157.170 0.079 Ethylbenzene 0.00 106.17 0.0001 Ethylbenzene 0.002 19.141 0.010 Xylenes 0.00 106.17 0.0002 Xylenes 0.006 48.588 0.024 CB+Heavies 0.05 116 0.0026 C8+Heavies 0.095 831.696 0.416 Mass Fraction VOC: 0.2721 Total VOC 42.835 Heating Value I 1304 BTU/scf I Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMOW 0.37 I lb COIMA8W 14WE0462 123/9c09 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1 F,Serial number 4016694).The pneumatic pump is controlled by 010 an enclosed flare with a minimum combustion efficiency of 95%. Notes Mole%,MW,and mass fractions are based on sales gas analysis collected 12/17/2013 from State Seventy Holes K-O-3HNB Typically I calculate the average MW of C8+based on the average MW on the analysis for the gas.This method resulted in minimal em Source used MW of 116 for C8+.Since there is minimal difference in emissions,I used the source's values. Emissions Summary Table Pollutant Uncontrolled Emission Fat Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 16299.36 lb/MMscf 814.97 lb/MMscf 42.8 tpy 2.1 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 1.3 tpy 1.3 tpy AP-42 Benzene 3875 lb/MMscf 1.94 lb/MMscf 204 lb/yr 10 lb/yr Gas Analysis i n-Hexane 235.35 lb/MMscf 11.77 lb/MMsc£ 1237 lb/yr 62 lb/yr Gas Analysis Toluene 29.90 lb/MMscf 1.50 lb/MMscf 157 lb/yr 8 lb/yr Gas Analysis Xylenes 9.24 lb/MMscf 0.46 lb/MMscf 49 lb/yr 2 lb/yr Gas Analysis Ethylbenzene 3.64 lb/MMscf 0.18 Ib/MMscf 19 lb/yr 1 lb/yr Gas Analysis 14WE0462 123/9C09 II -2 a 0 o N N N N N N N N y y N N U y y o a a o a o a 0 y o o o a o m m a m o o a o a a a o 0 0 2 > Z >- >- 2 > 2 > 2 > 222 Y Z> >>) Z Z Y z Y >- >- Z Z 2 ,e e e e e e e e e e e e e a N a e N N ja N e e e a Y) N Y] V) i(I rA 0 0 0 00 0 0 0 0 0 O o 0000g 0 0 W g m w m o+ O O 0. 0 rn w m U GIll T LO pp ‘10y n ma p Coo n N O m m m n N O 0 0 CI O O m e.- 0 0 ' V O N N INm in e en m m 7 t") N N H a N _ O N O CO ,- A n0') n N O m n m 7 N 7 N O on N O N f0 e •Q •r n O CO N o o E o. U o' W `. 9 o a O O 'N h ' 0 0 E c UQWG 4 4 4 4 4 4 NNNNNN m a m 0 0 a a N .0 .0 .0 .0 .0 .0 moncomoncy 7 H H H H H H 0 n n n n n n CO 0 0 0 U Lon N N YI IA In m 0 9 W 0 m 0 y0 N a a y a 0 N 0 N N LL o COth CC K T T T VT J, T T ≥. T T O en en en cotC) en co o co o N 0 0 a O N CCCy. O N AN N NN N NN 4 4 4 4 4 4 a N N Q Q Q Q Q < N N Q Q Q Q 4 '0 4 4 4 4 4 4 4 0 0 0 Q Q Q o 4 e 0 0 0 e e co cool coo E a Q Q a a Q w w a w w w 0 ch. 0 0 0 0 00 0 co co on co on cu < Q 000 a 0 oncoococon m 00 m1 ¢ rn a o `o8'8'8 13 co - I 0 U 0 '00 C a O O O O O N 0 m y ono co N N m co 0 N in 0 0 0 0 0 0 0 0 0 0 2222222222222222 .y 0000000 2222222 2g 2 2 2 2 2 2 2 2 E a Z Z B 3 `n :810 .11Z 3 3 3 n o 3 3 3 3 W m IO p I O I O co m m n Y I C O N e CO m n N 0 e CO in ' N 0 C) N 0 0) VI m o e m t0 CO 0 m 0 CO a e O N o 0 0 0 0)0 O I.-- Lei 0 en N m O O N O n o 0 e o 0 0 0 0 0 o aim aim ai c o m ai ai Vi 0 05 N N e 0 CO g .. C {p J LL m C a c 0 co Q N -it U an 0- L C C_ C_ 0 l0 o N a c c to' a s a co a co m w s m x m g E a0 y a x d m x m g c i•)3 -7 2 O O _ S t a 4 O 0 0 2 "5, a O x a 2 S.a U x 2 x 2 S, m N `0) > m o S.NO a = o t 5.000 = 0£5.000 a = m t >. crud a > m C H w x N > m CI- w x > z U m c H W x > z U m CI- Lux m 2 m a " ° �,E co N 0 10 10 N 0 N ca o 0 0 0 0 CO0 00 00 0 CO O c') m m CC Q U 0 CO i 4t CO N-0 E 0 0 0 a II fl a w n Z �'o- Y Z > 2 > Z Z Z w o o m o) rn e e e rn O O N N h h m rn U W a 0 N .° m O) 0 a a N N (N N C] O N co '- N 0 0 Na 0 O O o N5 o a E a U K W t a ti m 0 o To y o u E U Q w 0 'o 0) LL T T T J a T Q N EEE N a y < V V Q Q < Q Q N N N N N y W U' Q Q U U 0 U' U J J U m to U U O 0 O O 'E a a a a a a B a W m m I� ,- 1() (O N N C) U) C) a•O C y „ O d o Lei O. 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