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Home My WebLink About20143790.tiff COPHE COLORADO CO ,� Department of Public • Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150O St PO Box 758 Greeley, CO 80632 December 2, 2014 Dear Sir or Madam: On December 3, 2014, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company, LLC - State Antelope 14-2 Production Facility. 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 beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health e Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 4300 Cherry Creek Drive S., Denver,CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe ' 1i John W. Hickenlooper,Governor I Larry Wolk,MD,MSPH,Executive Director and Chief Medical Officer A,:• ;'.`, '•{, �j �� \lR7�•f T �ny�n 12I 20i l02r10-1 W PLr Plcl/ �f2 CDPHE Air Pollution Control Division CO �, Notice of a Proposed Project or Activity Warranting Public ' Comment Website Title: Bonanza Creek Energy Operating Company, LLC - State Antelope 14-2 Production Facility - Weld County Notice Period Begins: December 3, 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 Antelope 14-2 Production Facility Oil and Gas Production Facility SWSW SEC 2 T5N R62W Weld County The proposed project or activity is as follows: Applicant proposes to receive a permit for the construction of an oil and gas exploration and 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 14WE1298 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: Christopher Kester Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us ®V COLORADO 1 I peps in MfiDL:. HW U+F S-..::.nin.e+ STATE OF COLORADO •LO- • •• D ' • -T` •F P = C HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION " � TELEPHONE: (303) 692-3150 ' Vie ' CONSTRUCTION PERMIT PERMIT NO: 14WE1298 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 Antelope 14-2 Production Facility, located in the SWSW SEC 2 T5N R62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Condensate Eight(8) 400 bbl Condensate Storage Tanks; Emissions from the Tank 007 Tanks are controlled by two enclosed flares with minimum Battery destruction efficiencies of 95%. Two (2) 400 bbl and One (1) 60 bbl produced water storage tanks; PW Tanks 008 Emissions from the 400 bbl tanks are controlled by two enclosed flares with minimum destruction efficiencies of 95%. The 60 bbl tank is uncontrolled Loadout of Condensate; Emissions from the loadout are controlled Truck by a vapor balance system with a minimum collection efficiency of Loadout 009 70% that routes emissions to two enclosed flares with a minimum destruction efficiency of 95%. FUG 010 Facility Wide Fugitive Equipment Leaks One (1) Candlestick Flare to be used in case of emergency; Flare FL-2 012 has a minimum destruction efficiency of 95%. This flare is not enclosed. One (1) Vapor Recovery Tower (VRT); Emissions from the VRT VRT-1 013 are controlled by two enclosed flares with minimum destruction efficiencies of 95% when gas compressors are down. One (1) Pneumatic Pump use for water transfer; Emissions from P-1 014 the Pneumatic Pump are controlled by two enclosed flares with minimum destruction efficiencies of 95%. AIRS ID: 12319C99 Page 1 of 18 olor Depa en li vim it Pollution el ControlandEn Division Facility AIRS Equipment Point Description ID • Sep-1, Sep- Three (3) Low Pressure Separators; Emissions from the Low 2, and Sep 015 Pressure Separators are controlled by two enclosed flares with 3 minimum destruction efficiencies of 95%when the gas compressors are down. 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: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit or commencement of operations (whichever is later), by submittinst a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ao/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. Within one hundred and eighty days (180) after issuance of this permit or commencement of operations (whichever is later), 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). 3. 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; (iii) 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.) 4. 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.) 5. Points 013 and 015: Within one hundred and eighty (180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flow rate of natural gas vented from the separators and vapor recovery tower. The operator shall used the gas flow rate listed in the application for actual flow rate until the flow meter is installed, not to exceed one hundred and eighty(180) days after issuance of this permit. AIRS ID: 123/9C99 Page 2 of 18 olor- Depa en • P •li ''Health and Environment it Pollution Control Division 6. The operator - -in -'.. >e -1 '•n le - -ued 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 7. 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 x Condensate 007 0.10 2.47 0.55 Point Tank Battery PW Tanks 008 --- 2.32 --- Point Truck Loadout 009 0.02 4.50 0.10 Point FUG 010 --- 17.14 --- Fugitive FL-2 012 0.68 6.74 3.70 Point VRT-1 013 0.08 2.48 0.45 Point P-1 014 0.24 2.36 1.30 Point Sep-1, Sep-2, 015 0.34 7.30 1.84 Point and Sep-3 See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. 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. 8. Point 010: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas and liquids analyses, 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. AIRS ID: 12319C99 Page 3 of 18 olor epa entHealth and Environment ollution Control Division 9. The emission th sh aintained 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 Control Device Pollutants Equipment ID Point Controlled Condensate Two(2) Enclosed Flares.The Flares have a Tank Battery 007 minimum destruction efficiency of 95% and VOC and HAPs constant pilot lights. Two(2) Enclosed Flares. The Flares have a PW Tanks 008 minimum destruction efficiency of 95%and VOC and HAPs constant pilot lights. Two(2) Enclosed Flares. The Flares have a Truck Loadout 009 minimum destruction efficiency of 95% and VOC and HAPs constant pilot lights. Candlestick Flare with a minimum FL-2 012 destruction efficiency of 95%and a constant VOC and HAPs pilot light. Two(2) Enclosed Flares. The Flares have a VRT-1 013 minimum destruction efficiency of 95% and VOC and HAPs constant pilot lights. Two(2) Enclosed Flares. The Flares have a P-1 014 minimum destruction efficiency of 95%and VOC and HAPs constant pilot lights. Two(2) Enclosed Flares. The Flares have a Sep-1, Sep-2, 015 minimum destruction efficiency of 95% and VOC and HAPs and Sep-3 constant pilot lights. PROCESS LIMITATIONS AND RECORDS 10. 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 Process Parameter Annual Limit Equipment ID Point Condensate 007 Condensate Throughput 197,100 BBL Tank Battery PW Tanks 008 Produced Water Throughput 354,780 BBL Truck Loadout 009 Oil Loaded 197,100 BBL FUG 010 NA FL-2 012 Vented Gas 15 MMSCF VRT-1 013 Gas Vented from VRT 0.85 MMSCF P-1 014 Gas Vented from Pneumatic Pump 5.3 MMSCF Sep-1, Sep-2, 015 Gas Vented from Low Pressure 5 MMSCF and Sep-3 Separators 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 AIRS ID: 123/9C99 Page 4 of 18 olor Depa en . .li `Health and Environment •it Pollution Control Division month and - - o - c 3=- rd - ' .r at 'cal field office with site responsibility, for Division review. Points 013 and 015: The operator shall continuously monitor and record the volumetric flowrate of natural gas vented from the separators and VRT using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented from the separators. The operator shall use monthly throughput records to demonstrate compliance with the process limits and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 11. Points 007, 008, 009, 012, 013, 014, 015: 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) 12. 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.) 13. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 14. Point 007: 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.) 15. Point 007: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 16. Point 007: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 17. Points 007, 008, 013, 015: The flare covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). If a flare or other combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XVII. AIRS ID: 123/9C99 Page 5 of 18 Depa en li Health and Environment it Pollution Control Division 18. Point 007: TDolor t red is permit are subject to Regulation 7, Section XVII emission control requirements. These requirements include, but are not limited to: Section XVII.C. - Emission reduction from condensate storage tanks at oil and gas exploration and production operations, natural gas compressor stations, natural gas drip stations and natural gas processing plants. XVII.C.1. Beginning May 1, 2008, owners or operators of all atmospheric condensate storage tanks with uncontrolled actual emissions of volatile organic compounds equal to or greater than 20 tons per year based on a rolling twelve-month total shall operate air pollution control equipment that has an average control efficiency of at least 95%for VOCs on such tanks. XVII.C.3. Monitoring:. The owner or operator of any condensate storage tank that is required to control volatile organic compound emissions pursuant to this section XVII.C. shall visually inspect or monitor the Air Pollution Control Equipment to ensure that it is operating at least as often as condensate is loaded out from the tank, unless a more frequent inspection or monitoring schedule is followed. In addition, if a flare or other combustion device is used, the owner or operator shall visually inspect the device for visible emissions at least as often as condensate is loaded out from the tank. XVII.C.4. Recordkeeping: The owner or operator of each condensate storage tank shall maintain the following records for a period of five years: XVII.C.4.a. Monthly condensate production from the tank. XVII.C.4.b For any condensate storage tank required to be controlled pursuant to this section XVII.C., the date, time and duration of any period where the air pollution control equipment is not operating. The duration of a period of non-operation shall be from the time that the air pollution control equipment was last observed to be operating until the time the equipment recommences operation. XVII.C.4.c. For tanks where a flare or other combustion device is being used, the date and time of any instances where visible emissions are observed from the device. 19. Point 009: 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) 20. Point 009: 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. AIRS ID: 12319C99 Page 6 of 18 olor- Depa en . • •li Health and Environment it Pollution Control Division c. The o .pe. s ' _ ' pet <-- equi. ^, and operations on site at the time of the inspection to ensure compliance with above conditions. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. Point 009: 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. 22. Point 010: 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. 23. Point 010: 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). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. a. Conduct Audible, Visual, and Olfactory Inspections (AVOs) on a semi-annual basis of all pumps, valves, connectors, and pressure relief devices on the pad. The first semi-annual AVO will be conducted within 180 days of permit issuance. b. For each leak found in the AVO inspection, a gas detector shall 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 (iii) below. c. Repair Components with detectable leaks above the limit within 15 days. o If a leak is detected but it is not possible to repair without a process unit shutdown, repair of this equipment will be performed before the end of the next process unit shutdown. o Records will be kept to document the delay in repair along with the estimated time the component will be repaired in. d. Re-Screen repaired components to determine if the leak is repaired e. If the rescreening shows that the leak was not repaired then another attempt to repair the leak will be made as soon as possible, but no later than 15 days after the rescreening. f. Steps c and d will be repeated until the rescreening shows no leak g. Leaking components will be documented along with the date the leak is detected, date the leak is repaired, and date that the leak is rescreened. h. The following records will be maintained and kept for two years at Bonanza Creek Energy's Kersey Field Office: AIRS ID: 123/9C99 Page 7 of 18 olor Depa en li ealth and Environment it Pollution Control Division o Li po iated ; o List of currently leaking components; o List of repaired components along with the reapir method and associated repair dates; o List of successful repairs, repair delays, and post-repair screenings and associated dates. 24. Point 010: The owner or operator shall follow the Directed Inspection and Maintenance (DI&M) program and record keeping format as approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your DI&M plan are subject to Division approval. 25. Point 012: The open flare covered by this permit has been approved as an alternative emissions control device under Regulation No. 7, Section XVII.B.2.e. The open flare shall have no visible emissions during normal operations and be designed so that an observer can, by means of visual observation from the outside of the open flare or by other convenient means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XVII. The owner/operator must equip the open flare with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. (Regulation No. 7, Section XVII.B.) OPERATING & MAINTENANCE REQUIREMENTS 26. Points: 007, 008, 009, 012, 013, 014, 015: 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.) 27. Point 009: The owner or operator of a loadout at which vapor balancing is used to control emissions shall: a. Install and operate the vapor collection and return equipment to collect vapors during loading of tank compartments of outbound transport trucks and route these vapors to the flare b. Include devices to prevent the release of vapor from vapor recovery hoses not in use. c. Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. d. Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. e. Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. f. Inspect pressure relief devices (PRD) annually for proper operation and replace as necessary. PRDs shall be set to release at a pressure that will ensure flashing, working and breathing losses are routed to the control device under normal operating conditions. AIRS ID: 123/9C99 Page 8 of 18 olor. Depa en . • .Ii Health and Environment A it Pollution Control Division g. Docu al. . . --. : -f t seals. PRD with an indication of status, a description of any problems found, and their resolution. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 28. Points 007, 008, 009, 012, 013, 014, 015: The owner or operator shall demonstrate compliance with opacity standards, using EPA Method 22 to determine the presence or absence of visible emissions. "Visible Emissions" means observations of smoke for any period or periods of duration greater than or equal to one (1) minute in any fifteen (15) minute period during normal operation. (Reference: Regulation No. 7, Section XVII.A.II) 29. Point 010: 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 number of components that are operated in "heavy liquid service", "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. Periodic Testing Requirements 30. Point 010: 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. These extended gas analyses shall be used in the compliance demonstration for each point on the permit as required in the Emission Limits and Records section of this permit. 31. Points 012, 013, 015: On an annual basis, the operator shall complete a site specific extended gas analysis of the natural gas produced at this site that is routed to the flare in order to verify the VOC and hazardous air pollutants (HAP) 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. ALTERNATE OPERATING SCENARIOS 32. Point 014: 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. 33. Point 014: 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. 34. Point 014: 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 35. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: AIRS ID: 123/9C99 Page 9 of 18 olor Depa en li ealth and Environment Da it Pollution Control Division ForRAlcirDePaa 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 (NOX) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per year, a change in annual actual emissions of one (1)ton 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. 36. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) 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 37. 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. 38. 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. AIRS ID: 12319C99 Page 10 of 18 olor. Depa . en P .Ii Health and Environment it Pollution Control Division 39. This permit i-„ in 1{- - t - - y an- pleteness 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. 40. Unless specifically stated otherwise, the general and specific conditions 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. 41. 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. 42. 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. 43. 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: Christopher Kester Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company AIRS ID: 12319C99 Page 11 of 18 Depa en Ii ealthllution and EnviroDivisionnment it Po ControlNotes to Permit HolderDolor o 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 Patorn , Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner 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: httD://www.colorado.nov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper 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# ilb/yr) reportable? Tririve(Ibtyr)ilv6`C5 e ym, 5 ea'rn 5 rh 51- E�,�.. €, 6fima� .. ,�Y-` - o Si 8&HtSPtt6v Peigeg o n sig 3 . a� � -, 1. T w a 3Alaanriv io mmat, y C Lt,� e �r wag"; �y ` eA ,ei$gLy'5°y 'y/ L ,.„., �..., ism c., ve dh gc. ,}5 �. 3 +.a Iil 5"'a gLMl P�� E . :7 fi 1"1 Benzene 71432 2484 Yes 124 008 n-Hexane 110543 7805 Yes 390 � � 6e,: 5 6 :tail1432 219lligh . No �i 56 7"3'T., p_ e �nm� r1 2 '� ee 2 110543 ,�,a1 ' e5 6r� i�'. Benzene 71432 168 - No -- n-Hexane 110543 983 Yes 010 Toluene 108883 324 Yes --- Ethylbenzene 100414 78 No Benzene1330207 ", Pqn1Sain .FAEggUniafraill4alits +��.. 4$ i ' 65 mf'C ! .i p5o Lt m.5h,665 ''I( °R2 " 5 x n N I e 5 »6� - 5"6 e 6 gyre aesifi"`b e. �a cx , �sl tl a®� e4 ®tom®� t 6Ezt:`fi`m' °6 fie, ss 6�- -.,§ e r Toluene ua56s w9 - f 556- pi,--- 6 _p„ ,y 6 `°?' € r - ,mr,.F �rm„m�m.,m r:, r�,mm,ym,5m'smat 5a,..Ke=4,n ,.c,a_n u.. efi6eo®4a -lei: 5 AIRS ID: 123/9C99 Page 12 of 18 olor Depa en P Ii Health and Environment Til) it Pollution Control Division Ethylbenzene 100414 63 No 3 Xylenes 1330207 177 No 9 Benzene 71432 1207 Yes 60 n-Hexane 110543 7308 Yes 365 013 Toluene 108883 980 Yes 49 Ethylbenzene 100414 94 No 5 Xylenes 1330207 320 Yes 16 Benzene 71432 250 Yes 13 n-Hexane 110543 1490 Yes 75 014 Toluene 108883 190 No 10 Ethylbenzene 100414 22 No I Xylenes 1330207 63 No 3 Benzene 71432 1200 Yes 60 n-Hexane 110543 6900 Yes 345 015 Toluene 108883 810 Yes 41 Ethylbenzene 100414 74 No 4 Xylenes 1330207 192 No 10 5) The emission levels contained in this permit are based on the following emission factors: Point 007: Emission Factors Uncontrolled Pollutant (Ib/BBL Source Condensate Throughput) VOC 0.5 ProMax Simulation n-Hexane 0.026 ProMax Simulation Benzene 0.004 ProMax Simulation Toluene 0.004 ProMax Simulation 2,2,4-TMP 0.002 ProMax Simulation Note: The controlled emissions for this point are based on the flare control efficiency of 95% AIRS ID: 123/9C99 Page 13 of 18 olor Depa en Ii Health and Environment it Pollution Control Division Point 008: Emission Factors Pollutant Uncontrolled Source lb/BBL Produced Water Throughput VOC 0.262 CDPHE n-Hexane 0.022 CDPHE Benzene 0.007 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 009: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.136 AP-42 n-Hexane 0.0075 AP-42 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= 1 (Submerged loading: dedicated vapor balance) P (true vapor pressure)=2.48 psia M (vapor molecular weight) =58.92 Ib/Ib-mol T(temperature of liquid loaded) = 523.67°R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors by the VOC emission factor. AIRS ID: 123/9C99 Page 14 of 18 olor Depa en • P .li Health and Environment it Pollution Control Division i „ a Point 010: Component Gas Heavy Oil Light Oil Water/Oil Connectors 2282 0 954 0 Flanges 137 0 32 0 Open-ended Lines 77 0 8 0 I Pump Seals 12 0 0 0 Valves 333 0 133 0 Other 159 0 24 0 VOC Content(wt 0.2921 0 0.9977 0 fraction) Benzene Content(wt. 0.0008 0 0.0082 0 fraction) Toluene Content(wt. 0.0006 0 0.0202 0 fraction) Ethylbenzene(wt. 0.00007 0 0.0052 0 fraction) Xylenes Content(wt. 0.0002 0 0.0203 0 fraction) n-hexane Content(wt. 0.0046 0 0.0473 0 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: Standard EFs-EPA-453/R-95-017 Table 2-4 Note that the emission limits included in this permit are derived by multiplying the equipment counts in the table above by a factor of 1.1 to accommodate other minor changes to the facility and to provide a conservative estimate of facility-wide emissions. 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 and liquids analyses. AIRS ID: 123/9C99 Page 15 of 18 R: AePFltjl oDHealth and Environment Pollution Control Division Point 012: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled Ib/MMscf Ib/MMscf NO,(lb/MMBTU) - 0.068 --- AP-42 CO(lb/MMBTU) — 0.37 -- AP-42 VOC 29.21 17,980 900 Sales Gas Analysis Benzene 0.08 47 2.4 Sales Gas Analysis Toluene 0.06 36 1.8 Sales Gas Analysis Ethylbenzene 0.007 4 0.2 Sales Gas Analysis Xylenes 0.02 12 0.6 Sales Gas Analysis n-hexane 0.46 283 14 Sales Gas Analysis Point 013: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NO,(lb/MMBTU) --- 0.068 — AP-42 CO(Ib/MMBTU) --- 0.37 - AP-42 VOC 84.88 117,043 5852 ProMax Benzene 1.03 1,423 71 ProMax Toluene 0.84 1,156 58 ProMax Ethylbenzene 0.08 111 6 ProMax Xylenes 0.27 377 19 ProMax n-hexane 6.26 8,628 431 ProMax Point 014: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NO,(lb/MMBTU) — 0.068 --- AP-42 CO - 0.37 AP-42 (lb/MMBTU) VOC 29.21 17,980 900 Sales Gas Analysis Benzene 0.08 47 2.4 Sales Gas Analysis Toluene 0.06 36 1.8 Sales Gas Analysis Ethylbenzene 0.007 4 0.2 Sales Gas Analysis Xylenes 0.02 12 0.6 Sales Gas Analysis n-hexane 0.46 283 14 Sales Gas Analysis AIRS ID: 12319C99 Page 16 of 18 olor Depa en .li Health and Environment it Pollution Control Division Point 015: Weight Emission Emission Fraction of Factors Factors Source Pollutant Gas (%) Uncontrolled Controlled lb/MMscf lb/MMscf NO, 0.068 --- AP-42 (lb/MMBTU) CO 0.37 --- AP-42 (Ib/MMBTU) VOC 62.77 58,550 2928 LP Gas Analysis Benzene 0.26 239 12 LP Gas Analysis Toluene 0.17 162 8 LP Gas Analysis Ethylbenzene 0.02 15 1 LP Gas Analysis Xylenes 0.04 38 2 LP Gas Analysis n-hexane 1.48 1380 69 LP Gas Analysis 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: Applicable Status Requirement Operating Permit Synthetic Minor/Major Source of: VOC, CO, NO,, HAP NANSR Synthetic Minor/Major Source of: VOC, CO, NO,, HAP MACT HH Major Source Requirements: Not Applicable 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://ecfr.qpoaccess.qov/ poaccess.qov/ AIRS ID: 123/9O99 Page 17 of 18 pa en li ealth and Environment it Pollution Control Division Part 60: StandaDolor e S ourc 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: 12319C99 Page 18 of 18 Division Information Engineer: Christopher Kester Control Engineer: Stefanie Rucker Review Date: 09/18/2014 Application Date: 07/30/2014 Facility Identifiers Permit No. 14WE1298 AIRS County it 123 Weld Facility d 9C99 Facility Type: exploration and production facility 0 Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: P VOC P NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company Source Name: State Antelope 14-2 Production Facility Source Location: SWSW SEC 2 T5N R62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company Mailing Address 2: 410 17th Street,Suite 1500 Address City,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@BonanzaCrk.com IRequested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Antelope 14-2 Production Facility,located in the SWSW SEC 2 T5N R62W,Weld County,Colorado. Point Name Type Control Action Condensate Newly 007 Tank Battery Condensate Tanks Flare reported source Newly 008 PW Tanks Water Tanks Flare reported source Newly 009 Truck Loadout Loadout Flare reported source Newly 010 FUG Fugitives None reported source Newly 012 FL-2 Separator Venting Flare reported source Newly 013 VRT-1 Separator Venting Flare reported source Newly 014 P-1 Separator Venting Flare reported source Sep-1, Sep-2, Newly 015 and Sep-3 Separator Venting Flare reported source Preliminary Analysis - 09/23/2014 - 14WE1298 - 123/9C99 007 One (1) above ground 300 bbl atmospheric condensate storage tank Lequsted Throughput I 197100Ibb1 Emissions from Combustion (verified) Nox 0.1 tpy Control Flare I CO 0.55 tpy Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.5 lb/bbl 49.275 tpy 2.46375 tpy E&P TANK Benzene 0.004 lb/bbl 788.4 lb/yr 39.42 lb/yr E&P TANK n-Hexane 0.026 lb/bbl 5124.6 lb/yr 256.23 lb/yr E&P TANK Toluene 0.00425 lb/bbl 837.675 lb/yr 41.88375 lb/yr E&P TANK 224 TMP 0.002 lb/bbl 394.2 lb/yr 19.71 lb/yr E&P TANK Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20%opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases 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. (only needed if using flare) Regulation 2—Odor Section I.A-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. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons (471 bbl) NSPS OOOO: for storage vessels in the natural gas production,transmission, and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. Regulation 7—Volatile Organic Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is subject to the emission control requirements for condensate tanks since it is located in an non attainment area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Subject to these requirements Preliminary Analysis - 09/23/2014 - 14WE1298 - 123/9C99 008 One(1)above ground 300 bbl produced water storage tank Emissions Calculations Requsted Throughput 354780 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 46.47618 tpy 2.323809 tpy CDPHE Benzene 0.007 lb/bbl 2483.46 lb/yr 124.173 lb/yr CDPHE n-Hexane 0.022 lb/bbl 7805.16 lb/yr 390.258 lb/yr CDPHE Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity.This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes.The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60,Appendix A(July, 1992)) in all subsections of Section II.A and B of this regulation. Section IIA.5-Smokeless Flare or Flares for the Combustion of Waste Gases 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. (only needed if using flare) Regulation 2-Odor Section I.A- 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. Preliminary Analysis - 09/23/2014 - 14WE1298 - 123/9C99 009 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 1 AP-42 P True Vapor Pressure 2.48 psia Sales Oil Analysis M Molecular Weight of Vap 59.74 lb/lb-mole Sales Oil Analysis T Liquid Temperature 523.67 deg. R Field Data Loading Loss Eq multiplied by VOC wt% of L 3.28 lb/10^3 gal 93.05% 1.38E-01 lb/bbl Annual requested Throughput 197100 BBL/yr 8278200 gal/yr Annual requested VOC emissions 27154 lb/yr 13.58 tpy Control: Flare Efficiency: 66.50% NCRPs Component Mass Fraction Benzene 0.0081 n-hexane 0.0541 Toluene 0.0053 Xylenes 0.0014 224 tmp 0.002594 Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.1378 lb/bbl 13.58 tpy 4.55 tpy AP-42 Benzene 0.0011 lb/bbl 219.21 lb/yr 73.44 lb/yr AP-42 n-Hexane 0.0075 lb/bbl 1470.02 lb/yr 492.46 lb/yr AP-42 Toluene 0.0007 lb/bbl 142.61 lb/yr 47.77 lb/yr AP-42 Xylenes 0.0002 lb/bbl 36.66 lb/yr 12.28 lb/yr AP-42 224 tmp 0.0004 lb/bbl 70.44 lb/yr 23.60 lb/yr AP-43 Regulatory Review 'Regulation 7-Volatile Organic Compounds This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. Preliminary Analysis-09/23/2014-14WE1298-123/909 010 Fugitive equipment leak. Regulation 7 information Operating Hours 8760 hours/year Emission Factor Source Standard EFs-EPA-453/R-95-017 Table 2-4 Control Efficiency Source: None Calculations Emission Factor ggew- Emissions Service Component Type Count source) Control(%)Pollutant Mass Fraction )spy) Table 24 Table 24 Reg.3 Connectors 2252 2.00E-04 1.00E-05 0.0% VOC 0.2921 10.126744 Flanges 137 3.90E-0e 5.70E-06 0.0% Benzene 0.000767 0.0265909 Open-Ended Lines 77 2.00E-03 150E-05 0.0% Toluene 0.00058 0.0201079 Gas Pump Seals 12 240E-03 3.50E-04 0.0% Ethylbenzene 0.000088 0.0023575 Valves 333 4.50E-03 250E-05 0.0% Xylanes 0.000191 0.0066217 Other 159 8.80E-03 1.20E-0s 0.0% n-Hexane 0.004591 0.1591643 Connectors 7.50E-06 7.50E-06 0.0% VOC Flanges 3.90E-07 3.90E-07 0.0% Benzene Heave Oil Open-Ended Lines 1.40E-04 7.20E-06 0.0% Toluene Pump Seals 0.00E+00 0.00E+00 0.0% Ethylbenzene Valves 8.40E-06 840E-06 0.0% Xylenes Other 3.20E-05 3.20E-05 0.0% n.Meyane Connectors 954 2.10E-01 7.50E-06 0.0% VOC 0.9977 7.0092686 Flanges 32 1.10E-04 2.40E-06 0.0% Benzene 0.008179 0.057461 Light Oil Open-Ended Lines 8 1.40E-03 1.40E-05 0.0% Toluene 0.020204 0.1419417 Pump Seals 0 1.30E-02 5.10E-0e 0.0% Eth)lbenzene 0.005187 0.0364409 Valves 133 250E-03 1.90E-05 0.0% Xylenes 0.020337 0.1428761 Other 24 7.50E-03 1.10E-04 0.0% n-Hexane 0.04727 0.3320919 Connectors 1.10E-01 1.00E-05 0.0% VOC Flanges 2.90E-06 2.90E-06 0.0% Benzene Waler/Oll Open-Ended Linea 250E-04 3.50E-06 0.0% Toluene Pump Seals 2.40E-05 3.40E-05 0.0% Emylbenzene Valves 9.80E-05 9.70E-06 0.0% Xylenes Other 140E-02 5.90E-05 0.0% n-He,ne EMISSION'S Summary Table _ PoIIMaM Uncontrolled Emissions Controlled Emissions Source VOC 17.14 tpy 17.14 My Standard Era-EPA-453/R-95-017 Table 2-4 Benzene 168.10 lb/yr 168.10 lb/yr Standard EFs EPA-453/R-95-017 Table 2-4 Toluene 324.10 IbM 324.10 IOM Standard EFs-EPA453R-95-017 Table 2-4 EtbAbenzene 77.60 IbM 77.80 Ibyr Standard EFs-EPA45319-95017 Table 2-4 %Stenos 299.00 IbM 299.00 lb/yr Standard EFs EPA453/R-95O17 Table 2-4 n-Hexane 982.51 lb/yr 982.51 IbM Standard EFs-EPA453R-95017 Table 2-4 Regulatory Applicability Reg.3 DI&M Will sa8hy RACT Requirements Preliminary Analysis-09/23/2014-14WE1298-123/9C99 Sales Gas routed to Candlestick Flare in the event of an emergency.Flare has a minimum combustion efficiency 012 of 95%. The flare is enclosed. FL-2 Equipment Description This source vents natural gas from: a high pressure separator in the event of an emergency(normally sales gas) Emissions from this source are: routed to a flare Natural gas venting from a high pressure separator in the event of an emergency(normally sales gas).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=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) 15 MMscf/yr 1712.328767 scfmr MW 23.3 lb/lb-mol 0.04109589 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.01 4.0026 0.000 0.000 0.00 15.84 0.01 CO2 2.56 44.01 1.127 0.048 5.09 44590.61 22.30 N2 0.67 28.013 0.188 0.008 0.85 7428.25 3.71 methane 70.96 16.041 11.382 0.489 51.42 450478.26 225.24 ethane 12.69 30.063 3.815 0.164 17.24 150980.91 75.49 propane 8.19 44.092 3.611 0.155 16.32 142920.90 71.46 isobutane 0.81 58.118 0.472 0.020 2.13 18661.40 9.33 n-butane 2.46 58.118 1.431 0.061 6.47 56653 55 28.33 isopentane 0.44 72.114 0.314 0.013 1.42 12415.41 6.21 n-pentane 0.54 72.114 0.389 0.017 1.76 15397.96 7.70 cyclopentane 0.05 70.13 0.032 0.001 0.14 1249.02 0.62 n-Hexane 0.12 86.18 0.107 0.005 0.48 4239.65 2.12 cyclohexane 0.03 84.16 0.029 0001 0.13 1135.83 0.57 Other hexanes 0.21 86.18 0.185 0.008 0.83 7305.97 3.65 heptanes 0.11 100.21 0.108 0.005 0.49 4263.55 2.13 ' methylcyclohexane 0.03 98.19 0.028 0.001 0.13 1115.32 0.56 224-TMP D.00 114.23 0.000 0.000 0.00 4.52 0.00 i Benzene 0.02 78.12 0.018 0.001 0.08 708.03 0.35 Toluene 0.01 92.15 0.014 0.001 0.06 536.12 0.27 Ethylbenzene 0.00 106.17 0.002 0.000 0.01 63.03 ___0.03 Xyienes 0.00 106.17 0.004 0.000 0.02 176.48 0.09 Ca+Heavies 0.06 137.4837288 0.082 0.004 0.37 3232.14 1.62 99.98 VOC mass fraction: 0.293 Total VOC(Uncontrolled) 135.04 Notes Mole%,MW,and mass fractions from Sales gas analysis of Antelope D-X-2HNC. Emissions are based an 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Rare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1333 Btu/sd Throughput 19995 MMBtu/yr Overall Control 95.00% • Combustion emission factor source: AP-42:Chapter 13.5 0.07 jib NOX/MMBtu 0.37 jib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18005.26 Ib/MMsd 900.26 b/MMscf 135.04 tpy 6.75 tpy Gas Analysis NOx 0.07 Ib/MMBTU 0.07 b/MMBTU 0.68 tpy 0.68 tpy AP-42 CO 0.37 bb/MMBTU 0.37 b/MMBTU 3.70 tpy 3.70 tpy AP-42 Benzene 47.20 lb/mmscf 2.36 b/MMscf 708.03 lb/yr 35.40 lb/yr Gas Analysis n-Hexane 282.64 lb/MMscf 14.13 b/MMscf 4239.65 lb/yr 211.98 lb/yr Gas Analysis Toluene 35.74 lb/MMsd 1.79 b/MMsd 536.12 lb/yr 26.81 lb/yr Gas Analysis Xylenes 11.77 lb/MMsd 0.59 b/MMsd 176.48 lb/yr 8.82 lb/yr Gas Analysis Ethylbenzene 4.20 lb/MMsd 0.21 b/MMscf 63.03 lb/yr 3.15 lb/yr Gas Analysis Regulatory Applicability AOCC 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.' . AOCC Regulation Z 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." Preliminary Analysis-09/23/2014- 14WE1298-123/9C99 Two Enclosed Flares are used to control gas from one(1)Vapor Recovery Tower when the gas 013 compressors are down.Flare has a minimum combustion efficiency of 95%. VRT-1 Equipment Description This source vents natural gas from: Vapor Recovery Tower when gas compressors are down Emissions from this source are: routed to a flare 'Natural gas venting from Vapor Recovery Tower when gas compressors are down.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=a'MW'Xx IC Ex=emissions of pollutant x o=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(CO 0.848 MMscf/yr 96.80365297 scf/hr MW 52.3 lb/lb-mol 0002323288 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0000 0.000 0.00 0.00 000 CO2 1.27 44.01 0.559 0.011 0.14 1251.66 0.63 N2 0.11 28.013 0.031 0.001 0.01 68.32 0.03 methane 9.11 16.041 1.461 0.028 0.37 3269.69 1.63 ethane 19.46 30.063 5.850 0.112 1.49 13089.76 6.54 propane 26.99 44.092 11.900 0.228 3.04 26626.82 13.31 isobutane 3.47 58118 2.015 0.039 0.51 4508.39 2.25 n-butane 12.78 58.118 7.428 0.142 1.90 16620.17 8.31 isopentane 2.66 72.114 1.918 0.037 0.49 4291.98 2.15 n-pentane 3.44 72.114 2.481 0.047 0.63 5550.53 2.78 cyclopentane 1.61 70.13 1.132 0.022 0.29 2532.22 1.27 n-Hexane 3.79 86.18 3.266 0.06245 0.83 7308.06 3.65 cyclohexane 1.17 84.16 0.984 0.019 0.25 2202.74 1.10 Other hexanes . 7.50 86.18 6.466 0.124 1.65 14467.65 7.23 heptanes 2.75 100.21 2.761 0.053 0.71 6176.72 3.09 methylcyclohexane 0.93 98.19 0.910 0.017 0.23 2036.39 1.02 224-TMP 0.17 114.23 0.196 0.004 0.05 438.23 0.22 Benzene 0.69 78.12 0.539 0.010314 0.14 1206.97 0.60 Toluene 0.48 92.15 0.438 0.008374 0.11 979.89 0.49 Ethylbenzene 0.04 106.17 0.042 0.000807 0.01 94.39 0.05 Xylenes 0.13 106.17 0.143 0.002734 0.04 319.92 0.16 C8t Heavies 1.44 147 2.120 0.040528 0.54 4742.54 2.37 100.00 VOC mass fracti. 0.855 Total VOC(Uncontrolled) 50.05 Notes Mole%,MW,and mass fractions from VRT Gas Stream in a ProMax Simulation Emissions are based on 8760 hours of operation per year. Flaring Information Equipment Description Manufacturer LEED Model 48"L30-0010 Serial Number 21835 8 21619 Gas Heating Value 2901 Btu/scf Throughput 2460.048 MMBtu/yr Overall Control 95.00%] Combustion emission factor source: AP-42:Chapter 13.5 0.07 llb NOX/MMBtu 0.37 Ilb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 118046.72 lb/MMscf 5902.34 lb/MMscf 50.05 tpy 2.50 tpy ProMax Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.08 tpy 0.08 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 0.46 tpy 0.46 Spy AP-42 Benzene 1423.31 lb/MMscf 71.17 lb/MMscf 1206.97 lb/yr 60.35 lb/yr ProMax n-Hexane 8618.00 Ib/MMscf 430.90 lb/MMscf 7308.06 lb/yr 365.40 lb/yr ProMax Toluene 1155.53 lb/MMscf 57.78 lb/MMscf 979.89 lb/yr 48.99 lb/yr ProMax Xylenes 377.26 lb/MMscf 18.86 lb/MMscf 319.92 lb/yr 16.00 lb/yr ProMax Ethylbenzene 111.31 lb/MMscf 5.57 lb/MMscf 94.39 lb/yr 4.72 lb/yr ProMax 224 tmp - 516.80 lb/MMscf 25.84 lb/MMscf 438.25 lb/yr 21.91 lb/yr ProMax 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 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." Preliminary Analysis-09/23/2014-14WE1298-123/9C99 014 One(1)Sandpiper Pnuematic Pump for Water Transfer is controlled by P-1 Equipment Description This source vents natural gas from: Pnuematic Pump Emissions from this source are: routed to a flare Natural gas venting from Pnuematic Pump.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=0*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rateNolume 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-mot)at 60F and 1 atm Throughput(0) 5.3 MMscf/yr 605.0228311 scf/hr MW 23.3 Ib/lb-mol 0.014520548 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.01 4.0026 0.000 0.000 0.00 5.60 0.00 CO2 2.56 44.01 1.127 0.048 1.80 15755.35 7.88 N2 0.67 28.013 0.188 0.008 0.30 2624.65 1.31 methane 70.96 16.041 11.382 0.489 18.17 159168 99 79.58 ethane 12.69 30.063 3.815 0.164 6.09 53346.59 26.67 propane 8.19 44.092 3.611 0.155 5.76 50498.72 25.25 isobutane 0.81 58.118 0.472 0.020 0.75 6593.69 3.30 n-butane 2.46 58.118 1.431 0.061 2.29 20017.59 10.01 isopentane 0.44 72.114 0.314 0.013 0.50 438678 2.19 n-pentane 054 72.114 0.389 0.017 0.62 5440.61 2.72 cyclopentane 0.05 70.13 0032 0.001 0.05 441.32 0.22 n-Hexane 0.12 86.18 0107 0005 0.17 1498.01 0.75 cyclohexane 0.03 84.16 0029 0001 005 401.33 0.20 Other hexanes 0.21 86.18 0.185 0.008 0.29 2581.44 1.29 heptanes 0.11 100.21 0.108 0.005 0.17 1506.46 0.75 methylcyclohexane 0.03 98.19 0.028 0.001 0.04 394.08 0.20 224-TMP 0.00 114.23 0.000 0.000 0.00 1.60 0.00 Benzene 0.02 78.12 0.018 0.001 0.03 250.17 0.13 Toluene 0.01 92.15 0.014 0.001 0.02 189.43 0.09 Ethylbenzene 0.00 106.17 0.002 0.000 0.00 22.27 0.01, Xylenes 0.00 106.17 0.004 0.000 0.01 62.36 0.03 C8+Heavies 0.06 13]4837288 0.082 0.004 0.13 1142.02 0.57 VOC mass fraction: 0.293 Total VOC(Uncontrolled) 47.71 Notes Mole%,MW,and mass fractions from Sales gas analysis of Antelope D-X-2HNC. 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. • Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer LEED Model 48"L30-0010 Serial Number 21835&21619 Gas Heating Value 1333 Btu/sd Throughput 7064.9 MMBtu/yr Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOXIMMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18005.26 lb/MMscf 900.26 lb/MMscf 47.71 tpy 2.39 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.24 tpy 0.24 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.31 tpy 1.31 tpy AP-42 Benzene 47.20 lb/MMscf 2.36 lb/MMscf 250.17 lb/yr 12.51 lb/yr Gas Analysis n-Hexane 282.64 Ib/MMsd 14.13 lb/MMscf 1498.01 lb/yr 74.90 lb/yr Gas Analysis Toluene 35.74 lb/MMscf 1.79 lb/MMscf 189.43 lb/yr 9.47 lb/yr GarAnalysis Xylenes 11.77 lb/MMscf 0.59 lb/MMscf 62.36 lb/yr 3.12 lb/yr Gas Analysis Ethylbenzene 4.20 lb/MMsd 0.21 lb/MMscf 22.27 lb/yr 1.11 lb/yr Gas Analysis Regulatory Applicability AOCC Regulation 1 This source is subject to the opacity requirements for flares in Section IIA.5'No owner or operator of a smokeless flare or other flare AOCQ 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." Preliminary Analysis-09/23/2014-14W E1298-123/9C99 Separator Emissions routed to enclosed flare when gas compressors are down.Flare has a minimum 015 destruction efficiency of 95% Sep-1,Sep-2,and Sep-3 Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well 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 rate/volume of gas processed MW=Molecular weight of gas=SG of gas`MW of air f Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 5 MMscf/yr 570.7762557 scf/hr MW 35.4 Ib/Ib-mol 0.01369863 MMscf/d mole% MW lbz/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.01 4.0026 0.000 0.000 0.00 5.28 0.00 CO2 2.83 44.01 1.245 0.035 1.88 16431.17 8.22 N2 0.10 28.013 0.028 0.001 0.04 369.56 0.18 methane 36.60 16.041 5.871 0.166 8.84 77451.58 38.73 ethane 20.11 30.063 6.046 0.171 9.10 79757.77 39.88 propane 20.54 44.092 9.057 0.256 13.64 119483.50 59.74 isobutane 2.63 58.118 1.528 0.043 2.30 20161.89 10.08 n-butane 9.19 58.118 5.342, 0.151 8.05 70481.49 35.24 isopentane 2.07 72.114 1.496 0.042 2.25 19738.12 9.87 n-pentane 2.75 72.114 1.982 0.056 2.98 26147.51 13.07 cyclopentane 0.20 70.13 0.141 0.004 0.21 1855.95 0.93 n-Hexane 0.61 86.18 0.524 0.015 0.79 6911.45 3.46 cyclohexane 0.16 84.16 0.137 0.004 0.21 1810.88 0.91 Other hexanes 1.07 86.18 0.923 0.026 1.39 12172 O7 6.09 heptanes 0.52 100.21 0.520 0.015 0.78 6857.38 3.43 methylcyclohexane 0.13 98.19 0.128 0.004 0.19 1687.88 0.84 224-TMP 0.00 114.23 0.001 0.000 0.00 19.59 0.01 Benzene 0.12 78.12 0.091 0.003 0.14 1195.50 0.60 Toluene 0.07 92.15 0.062 0.002 0.09 812.09 0.41 Ethylbenzene 0.01 106.17 0.006 0.000 0.01 74.23 0.04 Xylenes 0.01 106.17 0.015 0.000 0.02 191.89 0.10 C8*Heavies 0.25 137.4837288 0.342 0.010 0.52 4518.10 2.26 99.98 VOC mass tract 0.630 Total VOC(Uncontrolled) 147.06 Notes Mole%,MW,and mass fractions from Low Pressure gas analysis of Antelope D-X-2HNC. 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. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer LEED Model 48"L30-0010 Serial Number 21635&21619 Gas Heating Value 1998 Btu/scf Throughput I 9990 MMBtu/yr • Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBtu 0.37 COIMMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 58823.91 Ib/MMscf 2941.20 Ih/MMscf 147.06 tpy 7.35 tpy Gas Analysis Nos 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.34 tpy 0.34 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 lb/MMBTU 1.85 tpy 1.85 tpy AP-42 Benzene 239.10 lb/MMscf 11.96 lb/MMscf 1195.50 lb/yr 59.78 lb/yr Gas Analysis n-Hexane 1382.29 lb/MMscf 69.11 lb/MMscf 6911.45 lb/yr 345.57 lb/yr Gas Analysis Toluene 182.42 lb/MMscf 8.12 lb/MMscf 812.09 lb/yr 40.60 lb/yr Gas Analysis Xylenes 38.38 lb/MMscf 1.92 lb/MMscf 191.89 lb/yr 9.59 lb/yr Gas Analysis Ethylbenzene 14.85 lb/MMscf 0.74 lb/MMscf 74.23 lb/yr 3.71 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 IA 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." Air Pollutant Emission Notice(APEN)—and—Application for Construction Permit �• OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY Current Status(Check all that apply) Reason for APEN Submittal(Check all that apply) ��C ` AIRS ID#I: 123/9C99 (IX02 O APEN update only E New or previously unreported battery O Modification to existing sources \,S i t ❑ Previously grandfathered battery2 ❑ Registration for coverage under general permit no.GPkeiree--' O Synthetic minor facility &cancellation request for individual permit°: E Located in the 8-hr Ozone Control Areal E Application for or Modification of an individual permit O Registered under general permit no.GPOI O Administrative permit amendment' ❑ Permitted under individual permit: ❑ . Other: 14LI1,[18 For individual permit applications,check if you want': 0 A copy of the preliminary analysis conducted by the Division E To review a draft of the permit prior to issuance Company Name9: Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address10: 410 17th Street,Suite 1500 City: Denver State: CO Zip: 80202 E-mail: pyoung@BonanzaCrkcom Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name 1: State Antelope 14-2 Production Facility(COGCC#435952) Number of tanks: 8-400 bbl Location"(QQ Sec.Twp.Range.): SW/SW,Sec 2,T5N,R62W County: Weld Total tank capacity[bbl]: 3,200 Calendar year for which"Actual"data applies": NA Year(s)tank(s)were placed in service": 2014 Control Description's: Two(2)Leed L30-0010(SN:21635&21619) Control EBiciency'6: 95% Condensate Throughput"[bbl/year] Requested': 197,100 Maximum for PTE calculation': 197,100 Actual20: 164,250 While Controls Operational31 164,250 Other equipment at facility": Heated separators,produced water tanks,natural gas-fired engines,pneumatic pump,vapor recovery tower Comments: 2-yr APEN update not required(uncontrolled VOC emissions<80 tpy) Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit ❑Check if the Division is to calculate emissions. E Check if site-specific emission factors provided to calculate emissions". Emission Factor Battery Requested Emissions' Actual Emissions30 Pollutant31 [lb/bbl] PTE2s Uncontrolled26 Controlled27 Uncont olled26 Controlled") VOC[tons/year] 0.50 " 49.3 49.3 2.47 'III 41.1 2.06 NOx[tons/year] 0.10/ 0.09 CO[tons/year] 0.55 - 0.47 Benzene[lbs/year] 0.004� 842.6 842.6 - 42.1 - 702.2 35.1 n-Hexane[lbs/year] 0.026 ' 5,129.2 5,129.2 - 256.5 4,274.3 213.7 Wells serviced by this tank or tank battery28 API#: 05-123.38880 Name: State Antelope D-X-2HNC E Newly Reported Well Apt#: 05-123.38879 Name: State Antelope 14-44-2HNC E Newly Reported Well API#. 05-123-38878 Name: State Antelope D14-X44-2HNC E Newly Reported Well API#: Name: O Newly Reported Well API#: Name ❑Newly Reported Well API#: Name: ❑Newly Reported Well API#: Name: ❑Newly Reported Well The signature below indicates that I have knowledge of the facts herein set forth and that the same are true,accurate,and complete to the best of my knowledge and belief If this is a re istration for coverage under general permit GPO],I further certify that this source is and will be operated in full lian�each conditi e�,� ral permit GPOI. 7/a9 /aory Signature of Legally Aiorized Person(not a vendor or consultant) Date David 1.Lille Vice President,Rocky Mtn.Asset Mgmt. Type or Print Name of Person Signing Above Official Title Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-B 1 O is (303)692-3150 S250 General Permit fee for each new GP 4300 Cherry Creek Drive South 315447 registration to: Denver,CO 80246-1530 FORM APCD-205 Page 1 oft FornrAPCD-205-E&PCondensateTankAPEN.docx To Cu a is • o ..-, O Q o co T la -N a a a) u a ?3 u w c E Z v p C3 CD 13 O Oi ° - a) W U -,. N N a N O 0 O C Q L 0 75 N N -p o Cy r c 'y o c Q E L ° '92 as � N 2 Q, 0 cn r C > W a M $ W ) Y CO _ CO " o J U 7 co N C ., 0 O Cr) -r. O c Z V h ;:Z. o N 1� C O V N CO co l C U in O O D Z Cl) � r o a a d a ® —r� J. ` L O O CO— € 7 d C U 3 0 N u) o 7 ≥ o a E E H C U Z Z E G al CO p) a) X LLJ c O lC W O O to p- .c d CL 0 Z E -N < U O cTi N i— o v- a) a) C J• c U C -Co > J sa _iw 7 n a . O ; >, C E C O N w C `o d W v 0 0 0. 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