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Home My WebLink About20150901.tiff A CDPHE • COLORADO Co ,1:%. 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 1150O St PO Box 758 Greeley, RECEIVED Greeleele y, CO 80632 March 27, 2015 APR 0 1 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On April 1, 2015, the Air Pollution Control Division wilt begin a 30-day public notice period for Bonanza Creek Energy Operating Company - Antelope B-33. 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 a 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 2015-0901 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov;cdphe John W. Hiccenlooper. Governor ; Larry Wolk.MD,MSPH, Executive Director and Chief Medical Officer lit7i ,,, CDPHE Air Pollution Control Division CO s Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company - Antelope B-33 - Weld County Notice Period Begins: April 1, 2015 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 Facility: Antelope 8-33 Oil and gas exploration and production facility SWNW Sec 33 T5N R62W Weld County The proposed project or activity is as follows: Source proposes to operate 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): • 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 13WE2759 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 • V COLORADO /� • itt STATE OF COLORADO COLORADO DEPA T •F PU=LIC HEALTH AND ENVIRONMENT 0c coto. AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692.3150 /876 � CONSTRUCTION PERMIT PERMIT NO: 1 3W O2759 Issuance 2 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 Antelope B-33 Production Facility, located in the SWNW Section 33, Township 5N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Fourteen (14) 500 bbl above ground atmospheric condensate CNDTK-1 002 storage tanks controlled by six enclosed flares. Each flare has a minimum control efficiency of 95%. Two (2)400 bbl above ground produced water storage tanks PW 003 controlled by six enclosed flares. Each flare has a minimum control efficiency of 95%. Hydrocarbon Loadout to Tanker Trucks. Loadout is controlled TLO 004 by using dedicated vapor balance service and six enclosed flares. Collection system is 70% efficient and each flare has a minimum control efficiency of 95%. One (1) pneumatic water transfer pump, rated at 600 scf/hr P-1 006 (Sandpiper, Model G1F, Serial number 2004238). The pneumatic pump is controlled by six enclosed flares. Each flare has a minimum control efficiency of 95%. SEP-1 to Nine low-pressure separators controlled by six enclosed flares SEP-9 007 during VRU downtime. Each flare has a minimum control efficiency of 95%. One emergency flare used to combust separator gas during FL-2 013 emergencies or when the pipeline is not available. Flare has a minimum control efficiency of 95%. The flare is not enclosed. AIRS ID: 123/9B84 Page 1 of 18 olor. Depa en . P •li ealth and Environment it Pollution Control Division Facility AIRS Equipment Point Description ID Two vapor recovery towers (VRTs) controlled by six enclosed VRT-1 and 014 flares during VRU downtime. Each flare has a minimum control VRT-2 efficiency of 95%. Point 006: 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 seq), 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. AIRS Point 013: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submittinq 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 013: 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 013: 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 002 — 007, 014: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submittinq 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 002 — 007, 014: 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 AIRS ID: 123/9B84 Page 2 of 18 olora°i Depa ' en P li ealth and Environment ti 1 fir Pollution Control Division compliance w.=a ,ai- .n ' to ate c nce 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; (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, Pad B, III.F.4.) 7. 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.) 8. 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 9. 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 CNDTK-1 002 --- 3.5 --- Point PW 003 2.6 Point TLO 004 --- 10.4 --- Point P-1 006 --- 2.3 1.3 Point SEP-1 to SEP-9 007 --- 11.5 2.5 Point FL-2 013 --- 5.8 3.7 Point VRT-1 and VRT 014 --- 4.1 --- Point -2 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. AIRS ID: 123/9B84 Page 3 of 18 6 olor Depa en • P .li " ealth and Environment •it Pollution Control Division The permit h. I c- ' -t' .io - onth - • eep 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. 10. 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 CNDTK-1 002 Enclosed Flare VOC PW 003 Enclosed Flare VOC TLO 004 Vapor balance and Enclosed Flare VOC P-1 006 Enclosed Flare VOC SEP-1 to 007 Enclosed Flare VOC SEP-9 FL-2 013 Open Flare VOC VRT-1 and 014 Enclosed Flare VOC VRT-2 PROCESS LIMITATIONS AND RECORDS 11. 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 CNDTK-1 002 Condensate Throughput 512,460 BBL PW 003 Produced Water Throughput 398,580 BBL TLO 004 Condensate Loaded 512,460 BBL P-1 006 Natural Gas Consumed 5.3 MMSCF SEP-1 to 007 Total Gas Vented from All Low-Pressure 6.1 MMSCF SEP-9 Separators during VRU Downtime FL-2 013 Total Gas Vented from All Separators to 15.0 MMSCF Emergency Flare VRT-1 and 014 Total Gas Vented from both Vapor Recovery 1,5 MMSCF VRT-2 Towers (VRTs)during VRU Downtime 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: 123/9B84 Page 4 of 18 olor Depa en P li ealth and Environment it Pollution Control Division month and k o c rd r at cal field office with site responsibility, for Division review. 12. AIRS Points 007 and 014: The owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from all low pressure separators and both VRTs during VRU downtime using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented to the enclosed flares from all low-pressure separators and VRTs during VRU downtime. The owner or operator shall use monthly throughput records and calculation methods detailed in the O&M Plan to demonstrate compliance with the limits specified in Condition 11 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 13. 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) 14. 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.2.b shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 5.) 15. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 16. AIRS Point 002: 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. AIRS Point 002: 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. 18. AIRS Point 002: The condensate storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: XVII.C.1.a. 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. 19. AIRS Points 002, 003, 007, and 014: The flare(s) covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: XVII.B.2.b If a combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible AIRS ID: 123/9B84 Page 5 of 18 olor- sepa en . P .9ealth and Environment a •it Pollution Control Division liremissi `^"'' g • =•a do ;I --- desi- -• 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. XVII.B.2.d Auto-igniters: All combustion devices used to control emissions of hydrocarbons must be equipped with and operate an auto-igniter as follows: XVII.B.2.d.(i)All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device. XVII.B.2.d.(ii) All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 20. AIRS Points 002 and 003: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98%for hydrocarbons. XVII.C.1.b.(i)(a) Control requirements of Section XVII.C.1.b. must be achieved within ninety (90) days of the date that the storage tank commences operation. XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section XVII.C.1.b.(i), whichever comes later, owners or operators of storage tanks subject to Section XVII.C.1. must conduct audio, visual, olfactory ("AVO") and additional visual inspections of the storage tank and any associated equipment (e.g. separator, air pollution control equipment, or other pressure reducing equipment) at the same frequency as liquids are loaded out from the storage tank. These inspections are not required more frequently than every seven (7) days but must be conducted at least every thirty one (31) days. Monitoring is not required for storage tanks or associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i) Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; XVII.C.1.d.(ii) Visual inspection or monitoring of the air pollution control equipment to ensure that it is operating, including that the pilot light is lit on combustion devices used as air pollution control equipment; XVII.C.1.d.(iii) If a combustion device is used, visual inspection of the auto-igniter and valves for piping of gas to the pilot light to ensure they are functioning properly; AIRS ID: 123/9B84 Page 6 of 18 olor. rt Depa eni. P li ealth and Environment Lr Pollution Control Division XVII.Cos is.,:;.• s+s;P. F, of- _, olluti trol equipment to ensure that the valves for the piping from the storage tank to the air pollution control equipment are open; and XVII.C.1.d.(v) If a combustion device is used, inspection of the device for the presence or absence of smoke. If smoke is observed, either the equipment must be immediately shut-in to investigate the potential cause for smoke and perform repairs, as necessary, or EPA Method 22 must be conducted to determine whether visible emissions are present for a period of at least one (1) minute in fifteen (15) minutes. XVII.C.1.e. If storage tanks or associated equipment is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor such equipment until it becomes feasible to do so. XVII.C.2. Capture and monitoring requirements for storage tanks that are fitted with air pollution control equipment as required by Sections XII.D. or XV II.C.1. XVII.C.2.a. Owners or operators of storage tanks must route all hydrocarbon emissions to air pollution control equipment, and must operate without venting hydrocarbon emissions from the thief hatch (or other access point to the tank) or pressure relief device during normal operation, unless venting is reasonably required for maintenance, gauging, or safety of personnel and equipment. Compliance must be achieved in accordance with the schedule in Section XVII.C.2.b.(ii). XVII.C.2.b. Owners or operators of storage tanks subject to the control requirements of Sections XII.D.2., XVII.C.1.a, or XVII.C.1.b. must develop, certify, and implement a documented Storage Tank Emission Management System ("STEM") plan to identify, evaluate, and employ appropriate control technologies, monitoring practices, operational practices, and/or other strategies designed to meet the requirements set forth in Section XVII.C.2.a. Owners or operators must update the STEM plan as necessary to achieve or maintain compliance. Owners or operators are not required to develop and implement STEM for storage tanks containing only stabilized liquids. The minimum elements of STEM are listed below. XVII.C.2.b.(i) STEM must include selected control technologies, monitoring practices, operational practices, and/or other strategies; procedures for evaluating ongoing storage tank emission capture performance; and monitoring in accordance with approved instrument monitoring methods following the applicable schedule in Section XVII.C.2.b.(ii) and Inspection Frequency in Table 1. XVII.C.2.b.(ii) Owners or operators must achieve the requirements of Sections XVII.C.2.a. and XVII.C.2.b. and begin implementing the required approved instrument monitoring method in accordance with the following schedule: XVII.C.2.b.(ii)(a) A storage tank constructed on or after May 1, 2014, must comply with the requirements of Section XVII.C.2.a. by the date the storage tank commences operation. The storage tank must comply with Section XVII.C.2.b. and implement the approved instrument monitoring AIRS ID: 123/9684 Page 7 of 18 i olor- Depa en'' . P •li ealth and Environment it Pollution Control Division =s' in = -io in - -e •#) da - the date that the storage tank commences operation. XVII.C.2.b.(ii)(d) Following the first approved instrument monitoring method inspection, owners or operators must continue conducting approved instrument monitoring method inspections in accordance with the Inspection Frequency in Table 1. Table 1 —Storage Tank Inspections Threshold: Storage Tank Approved Instrument Phase-In Uncontrolled Actual VOC Monitoring Method Inspection Schedule Emissions(tpy) Frequency > 6 and < 12 Annually January 1, 2016 > 12 and < 50 Quarterly July 1, 2015 > 50 Monthly January 1, 2015 XVII.C.2.b.(iii) Owners or operators are not required to monitor storage tanks and associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. XVII.C.2.b.(iv) STEM must include a certification by the owner or operator that the selected STEM strategy(ies) are designed to minimize emissions from storage tanks and associated equipment at the facility(ies), including thief hatches and pressure relief devices. XVII.C.3. Recordkeeping XVII.C.3. The owner or operator of each storage tank subject to Sections XII.D. or XVII.C. must maintain records of STEM, if applicable, including the plan, any updates, and the certification, and make them available to the Division upon request. In addition, for a period of two (2) years, the owner or operator must maintain records of any required monitoring and make them available to the Division upon request, including: XVII.C.3.a. The AIRS ID for the storage tank. XVII.C.3.b. The date and duration of any period where the thief hatch, pressure relief device, or other access point are found to be venting hydrocarbon emissions, except for venting that is reasonably required for maintenance, gauging, or safety of personnel and equipment. XVII.C.3.c. The date and duration of any period where the air pollution control equipment is not operating. XVII.C.3.d. Where a combustion device is being used, the date and result of any EPA Method 22 test or investigation pursuant to Section XVII.C.1.d.(v). XVII.C.3.e. The timing of and efforts made to eliminate venting, restore operation of air pollution control equipment, and mitigate visible emissions. • AIRS ID: 12319B84 Page 8 of 18 olor Depa en P li ealth and Environment ' it Pollution Control Division XVII.C.3.f. A ui t ter stor nk that is designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.C.1.e., an explanation stating why the equipment is so designated, and the plan for monitoring such equipment. 21. AIRS Point 004: 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) 22. AIRS Point 004: 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 22 (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. 23. AIRS Point 004: 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. 24. AIRS Points 007 and 014: The separation equipment, including low pressure separators and vapor recovery towers, covered by this permit is subject to Regulation 7, Section XVII.G emission control requirements. On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. 25. AIRS Point 013: The emergency flare, which receives gas from the separators during emergencies, is an approved alternative emissions control equipment per Regulation No. 7, Section XVI1.B.2.e. The emergency flare shall comply with all applicable requirements in Regulation No. 7, Section XVII.B General Provisions (State only enforceable), except the flare is not required to be enclosed. OPERATING & MAINTENANCE REQUIREMENTS 26. 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. AIRS Point 004: The owner or operator of a loadout at which vapor balancing is used to control emissions shall: AIRS ID: 123/9B84 Page 9 of 18 olor. Depa . en . P ell ealth and Environment -it Pollution Control Division a. Install - -rat- T- ill- ` + retu--"-:-uipment to coiled vapors during loading of tank compartments of outbound transport trucks and return these vapors to the stationary source storage tanks. 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. g. Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 28. AIRS Point 014: The operator shall complete an initial site specific extended gas analysis of the gas vented from the vapor recovery towers at this site in order to verify 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. ALTERNATE OPERATING SCENARIOS 29. Point 006: 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. 30. Point 006: 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 31. Point 006: 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 32. All previous versions of this permit are cancelled upon issuance of this permit. 33. This permit replaces the following permits and/or points, which are cancelled upon issuance of this permit. AIRS ID: 123/9884 Page 10 of 18 olor Depa en P li ealth and Environment Air Pollution Control Division Existin n Permit No. Emission Point New Permit No. GP01 123/9684/002 13WE2759 Issuance 2 GP05 123/9684/003 13WE2759 Issuance 2 34. 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: 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 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. 35. 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 36. 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. 37. 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 AIRS ID: 123/9684 Page 11 of 18 olor eepa en` • P .Ii ealth and Environment •it Pollution Control Division authorization G -t s .. ur..-` - AP • 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. 38. 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. 39. 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. 40. 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. 41. 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. 42. 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 AIRS ID: 123/9B84 Page 12 of 18 olor. Depa en P li ealth and Environment it Pollution Control Division Issuance 2 is -"1.v;n o o co IRS Point 002 from GP01 to this permit. Also added tanks, increased throughput and emissions. Modification to convert Point 003 from GP05 to this permit. Also add tank, increase throughput, and increase emissions. Modification to Point 004 to increase throughput and emissions and to add control. Cancellation of Point 005. Modification to Point 006 to increase emissions. Modification to Point 007 to add LP separators, account for VRU as process control, increase emissions, and increase throughput. Adding new points 013 and 014. Issuance 1 June 5, 2014 Issued to Bonanza Creek Energy Operating Company LLC for Points 004-007 AIRS ID: 12319B84 Page 13 of 18 olor. Depa en •- P •li ealth and Environment •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&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# (Ib/yr) reportable? (Ib/yr) Benzene 71432 1,108 Yes 55 n-Hexane 110543 6,168 Yes 308 Toluene 108883 179 No 9 002 Ethylbenzene 100414 354 Yes 18 Xylenes 1330207 319 Yes 16 2'2'4 540841 453 Yes 23 trimethylpentane Benzene 71432 2,790 Yes 140 003 n-Hexane 110543 8,769 Yes 438 Benzene 71432 568 Yes 190 n-Hexane 110543 3,935 Yes 1,318 004 Toluene 108883 348 Yes 117 Ethylbenzene 100414 15 No 5 Xylenes 1330207 115 No 39 Benzene 71432 237 No 12 n-Hexane 110543 1,432 Yes 72 006 Toluene 108883 187 No 9 Ethylbenzene 100414 35 No 2 AIRS ID: 123/9B84 Page 14 of 18 . olor- Depa ens. Pgi,fili ' ealth and Environment it Pollution Control Division 4 Benzene 71432 1,069 Yes 53 n-Hexane 110543 6,688 Yes 334 Toluene 108883 725 Yes 36 007 Ethylbenzene 100414 120 No 6 Xylenes 1330207 240 No 12 trimethylpentane2,2,4- 540841 368 Yes 18 Benzene 71432 615 Yes 31 n-Hexane 110543 3,366 Yes 168 013 Toluene 108883 427 Yes 21 Ethylbenzene 100414 67 No 3 Xylenes 1330207 328 Yes 16 Benzene 71432 1,862 Yes 93 n-Hexane 110543 10,314 Yes 516 Toluene 108883 569 Yes 28 014 Ethylbenzene 100414 296 Yes 15 Xylenes 1330207 505 Yes 25 2'2'4 540841 602 Yes 30 trimethylpentane 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Uncontrolled Controlled lb/BBL lb/BBL Condensate Condensate Pollutant Throughput Throughput Source VOC 0.2760 0.0138 Promax n-Hexane 0.0120 0.0006 Promax Benzene 0.0022 0.0001 Promax Toluene 0.0004 0.00002 Promax Ethylbenzene 0.0007 0.00003 Promax Xylenes 0.0006 0.00003 Promax I 2,2,4- 0.0009 0.00004 Promax trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. A HHV of 2,730 BTU/scf was used for combustion calculations. Point 003: Uncontrolled Controlled lb/BBL Produced lb/BBL Produced Pollutant Water Throughput Water Throughput Source AIRS ID: 123/9684 Page 15 of 18 olorl Depa en . P •li ealth and Environment s it Pollution Control Division o d; lb/BBL Produced lb/BBL Produced Pollutant Water Throughput Water Throughput Source VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 004: Uncontrolled Controlled Pollutant lb/BBL loaded lb/BBL loaded Source VOC 0.1207 0.0404 AP-42 Benzene 0.0011 0.0004 AP-42 n-Hexane 0.0077 0.0026 AP-42 Toluene 0.0007 0.0002 AP-42 Ethylbenzene 0.00003 0.00001 AP-42 Xylenes 0.0002 0.00008 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 service) P (true vapor pressure)=2.22 psia M (vapor molecular weight) =58.64 Ib/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 006: Uncontrolled Controlled Pollutant lb/MMscf vented Ib/MMscf vented Source NOx (lb/MMBTU) 0.068 0.068 AP-42 CO (lb/MMBTU) 0.37 0.37 AP-42 VOC 17,515 875.77 Gas Analysis Benzene 45.135 2.2568 Gas Analysis n-Hexane 272.41 13.621 Gas Analysis Toluene 35.495 1.7747 Gas Analysis Ethylbenzene 6.7232 0.3362 Gas Analysis Xylenes 14.567 0.7283 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 1,329 BTU/scf was used for combustion calculations. Point 007: Weight Fraction of Uncontrolled Controlled Pollutant Gas(%) lb/MMscf Ib/MMscf Source NOx(lb/MMBTU) -- 0.068 0.068 AP-42 CO (lb/MMBTU) --- 0.37 0.37 AP-42 VOC 71.0 74,906 3,745.3 Gas Analysis AIRS ID: 123/9884 Page 16 of 18 olor. Depa en P li ealth and Environment it Pollution Control Division ei.,u - Fraction of Uncontrolled Controlled Pollutant Gas (%) Ib/MMscf lb/MMscf Source Benzene 0.17 174.38 8.7189 Gas Analysis Toluene 0.11 118.17 5.9083 Gas Analysis Ethylbenzene 0.02 19.609 0.9805 Gas Analysis Xylenes 0.04 39.218 1.9609 Gas Analysis n-hexane 1.03 1,090.8 54.539 Gas Analysis 2,2,4- 0.06 59.978 2.9989 Gas Analysis trimethylpentane Note: The uncontrolled VOC and HAP emissions were calculated using weighted average of low pressure separator gas samples collected 8/11/2014 from Antelope 11-41-33HNC, Antelope B11-V41-33HNC and 11/6/2014 from State Antelope P-32 to estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 2,232 BTU/scf was used for calculations. Point 013: Weight Fraction of Uncontrolled Controlled Pollutant Gas (%) lb/MMscf lb/MMscf Source NOx (lb/MMBTU) --- 0.068 0.068 AP-42 CO (lb/MMBTU) --- 0.37 0.37 AP-42 VOC 25.6 15,575 778.73 Gas Analysis Benzene 0.07 41.018 2.0509 Gas Analysis Toluene 0.05 28.447 1.4224 Gas Analysis Ethylbenzene 0.01 4.4821 0.2241 Gas Analysis Xylenes 0.04 21.850 1.0925 Gas Analysis n-hexane 0.37 224.43 11.222 Gas Analysis Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,326 BTU/scf was used for calculations. Point 014: Weight Fraction of Uncontrolled Controlled Pollutant Gas(%) lb/MMscf lb/MMscf Source NOx (Ib/MMBTU) _ --- 0.068 0.068 AP-42 CO (Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 83.2 109,089 5,454.5 Gas Analysis Benzene 0.94 1,231.4 61.568 Gas Analysis Toluene 0.29 376.62 18.831 Gas Analysis Ethylbenzene 0.15 195.81 9.7906 Gas Analysis Xylenes 0.25 333.92 16.696 Gas Analysis n-hexane 5.20 6,821.6 341.08 Gas Analysis 2,2,4- 0.30 397.85 19.892 Gas Analysis trimethylpentane Note: The uncontrolled VOC and HAP emissions were calculated based on a Promax model to estimate the VOC and HAP content of the stream and stream flow. AIRS ID: 123/9684 Page 17 of 18 II olor. Depa en`. P •li ealth and Environment •it Pollution Control Division Emission factor .� ., ^ ' d • -r.i.• • • on ii • •r',.le 13 • HHV of 2,758 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: Applicable Status Requirement Operating Permit Synthetic Minor Source of: NOx, CO,VOC, HAPs NANSR Synthetic Minor Source of: NOx,VOC 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.oPoaccess.o ov/ 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: 123/9B84 Page 18 of 18 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 03/19/2015 Application Date: 12/24/2014 Facility Identifiers Permit No. 13WE2759 Potentially located in ozone nonattainment area AIRS County# 123 Weld Facility# 9884 Facility Type: exploration and production facility E Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: lZ VOC f NOx P CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Antelope B-33 Production Facility Source Location: SWNW Section 33,Township 5N, Range 62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street,Suite 1500 Address ity,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@bonanzacrk.com Requested Action Self Certification Required? Yes Issuance Number: 2 Source Description: Oil and gas exploration and production facility known as the Antelope B-33 Production Facility,located in the SWNW Section 33,Township 5N, Range 62W,Weld County,Colorado. Point Name Type Control Action Cancelling GP01 and adding to facility-wide 002 CNDTK-1 Condensate Tanks Flare permit.Adding tanks, increasing throughput and emissions Cancelling GP05 and adding to facility-wide 003 PW Water Tanks Flare permit. Increasing throughput and emissions 004 TLO Loadout Flare Modifying by increasing throughput and adding control Existing point-In first application(9/2014 and 12/2014),source requested to increase counts and emission limit from 3.7 to 30.6 tpy. 005 FUG Fugitives None On 3/26/2015, source requested to cancel fugitives since subject to Reg 7 and now APEN-exempt 006 P-1 Pump Flare Modifying by increasing emission limit based on updated gas analysis SEP-1 to Modifying by adding 8 LP separators, 007 SEP 9 Separator Venting Flare modifying process control, increasing throughput and emissions 013 FL-2 Separator Venting Flare New point-emergency flare VRT-1 and 014 Separator Venting Flare New point VRT-2 Points 001,008-011 are engines covered by GP02 or permit-exempt *Points 012 and 015 were for temporary flares that have already been removed Fourteen(14)500 bbl above ground atmospheric condensate storage tanks controlled by six 002 enclosed flares.Each flare has a minimum control efficiency of 95%. Requsted Throughput 512460 bbl Control Flare Efficiency 95.00%l Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2760 lb/bbl 70.7 tpy 3.5 tpy Promax Benzene 0.0022 lb/bbl 1108 lb/yr 55 lb/yr Promax n-Hexane 0.0120 lb/bbl 6168 lb/yr 308 lb/yr Promax Toluene 0.0004 lb/bbl 179 lb/yr 9 lb/yr Promax Ethylbenze 0.000716/661 354 lb/yr 18 lb/yr Promax Xylenes 0.0006 lb/bbl 319 lb/yr 16 lb/yr Promax 224-TMP 0.0009 lb/bbl 453 lb/yr 23 lb/yr Promax Nox 0.068 Ib/Mmhtu 0.1 tpy 0.1 tpy AP-42 Table 13.5 CO 0.37 lb/Mmbtu 0.8 tpy 0.8 tpy AP-42 Table 13.5 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. 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. The 500 bbl tanks are above the minimum capacity threshold of-471 bbl. However,the tanks are located at the wellhead site,store condensate,and are prior to custody transfer:thus,the tanks are exempt from NSPS Kb (60.110b(d)(4)) NSPS 0000: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()manic 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 the nonattainment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject to this requirement since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions are greater than 6 tpy. 13WE2759.CP2 E2759.CP2 123/9B84 Two(2)400 bbl above ground produced water storage tanks controlled by six 003 enclosed flares. Each flare has a minimum control efficiency of 95%. Emissions Calculations Requsted Throughput 398580 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 52.2 tpy 2.6 tpy CDPHE Benzene 0.007 lb/bbl 2790 lb/yr 140 lb/yr CDPHE n-Hexane 0.022 lb/bbl 8769 lb/yr 438 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. 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 7—Volatile Organic Compounds XVII.C.1.b Applicant is subject since actual uncontrolled emissions are greater than 6 tpy. 13WE2759.CP2 123/9884 Hydrocarbon Loadout to Tanker Trucks. Loadout is controlled by using dedicated vapor balance service and six enclosed flares.Collection system is 70%efficient and each flare has a minimum 004 control efficiency of 95%. 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 factor for submerged loading, dedicated vi P True Vapor Pressure 2.22 psia Calculated TVP of liquid based on oil analysis an M Molecular Weight of Vaf 58.64 lb/lb-mole Calculated MW of liquid based on oil analysis an T Liquid Temperature 523.67 deg. R EPA Tanks Met Data for Denver, CO L 2.87 lb/10A3 gal 1.21E-01 lb/bbl Annual requested Throughput 512460 BBL/yr 21523320 gal/yr Annual requested VOC emissions 61874 lb/yr 30.94 tpy Control: Flare Efficiency: 66.50% Source assumes 95%control efficiency and 70%collection efficiency NCRPs Component Mass Fraction VOC 0.9281 Benzene 0.0092 n-hexane 0.0636 Toluene 0.0056 Ethylbenzen 0.0002 Xylenes 0.0019 Source: Sales oil composition and Eq 1-22 of AP-42 Ch 7 Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.1207 lb/bbl 30.9 tpy 10.4 tpy AP-42 Benzene 0.0011 lb/bbl 568 lb/yr 190 lb/yr AP-42 n-Hexane 0.0077 lb/bbl 3935 lb/yr 1318 lb/yr AP-42 Toluene 0.0007 lb/bbl 348 lb/yr 117 lb/yr AP-42 Ethylbenzen 0.00003 lb/bbl 15 lb/yr 5 lb/yr AP-42 Xylenes 0.0002 lb/bbl 115 lb/yr 39 lb/yr AP-42 13WE2759.CP2 123/9884 Hydrocarbon Loadout to Tanker Trucks.Loadout is controlled by using dedicated vapor balance service and six enclosed flares.Collection system is 70%efficient and each flare has a minimum 004 control efficiency of 95%. Regulatory Review 'Regulation 3-APEN and Permitting Requirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day of crude oil on an annual av No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3, Part B,Section II Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3, Part B,Section II 13WE2759.CP2 123/9884 005 Fugitive VOC equipment leaks AS OF 11112015,MI5 SITE IS SUBJECT TO REG?.XVII F.UNDER REG 7 XVII.F.SOURCE CAN USE TABLE 2A EMISSION FACTORS WITH TABLE 2-8.FUGITIVE EMSSiCNS ARE NOW APEN-EXEMPT SOURCE REQUESTED TO CANCEL APES Regulation 7 Information Operating Hours 8750 noure/year Emission Factor Source Sever ng EFs-EPA-r53/R-95-0 I?Table 22 Coned Efficiency Source Nore Calculations Emission Factor Stolbr- Emissions Service Component Type Count source) Control(%)Pollutant Mass Fraction (tpy) Table 2-4 Table 2E- Reg.3 Conneclms 4098 200E-O4 1.00E-05 OOe VOC 1.2869 02664140 Flanges Ig5 390E-04 5.70E-06 00% Benzene O9007 000065 Open-Ended Lnes 135 500E-03 150E-05 00°6 Toluene 00006 00005572 Gas Pump Seals 0 2,40E-03 3500-04 00% Etholbenzene 00001 9266E-05 Valves 050 4.50520 2.50E-05 200 Xylenes O0002 00001657 other 275 600E-03 120E-0a 0.reMlexane 00045 3.0041787 Connectors 750E-06 750E06 'J3% VOC e Flanges 190E-07 390E-07 33°x., Benzene 0 Heavy Co Open-Ended Lines 1.4SE-4 720E-06 3.3% Toluene a Pump Seals 0.00Et00 0.005500 03% Elhylberoene 0 Valves 8.405-06 8.405-06 04% Xylenes 0 Other 320E-05 320E-05 0CP5 Mlexane a CCnneclam 1735 210E-04 970E-06 110% VOC 39973 0.2532007 Flar0er 56 110E-04 540E-06 U U% Benzene 0007 00017772 ognl oil Open-Ended Urns 55 1.40E-03 1.40E-05 00':, Toluene 33181 00045953 Pump Seals 0 130E-02 vOE V' 00M Ethylbenzene 33035 000080% Valves 243 250E-03 1.905 C5 U 5% sHlenes 10180 00047223 Other 41 760E-03 150E-04 00% e-Hexane 00383 30097230 Connectors 1.10E-04 10CE0s 0 0' VOCFl 1 0 pen 9.90E-065 230E-06 3 0% Benzene 0 Walebod Open-Ended alslined 2saE 04 3-soEL6 33% Toluene o Pump Seals 240E-Bs 240E-0s a... HnNbenzene o Valves 960E-0s 920E-06 33% Xylenes 3 Other 140E 02 5.90E05 33% n•Rexane 0 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source too VOC 0.52 tpy 052 toy Screening EFs•EPA-455R-04-017 Table 2-9 Benzene 5 Iblyr 5 Iblyr Screening EFs-EPA-4SVR-05-017 Table 2- 000 Toluene 10 Iblyr 1016/yr Screening EFs-EPA-463/R-05-017 Table 2- 541 Elnylbenzene 21brir 2 lb/yr Screening EFs-EPA-4631R-05-017 Table 2- 150 Xylenes • 15 lb/yr 10 Iblyr Screening EFs•EPA4531R-95-017 Table 2- 000 Mlexane i 201Wyr 281Nyr Screening EFs-EPA-4531R-95.017 Table 2- 0 0 VOC and HAP concentrations for gas service are based on weighted average of different sales gas samples collected 8/2312013. 111412013.0/11/2014,and 11/6/2014 from the different'sells al this site. Regulatory Applicability Reg.3 Review Regulation 3.Pan B.Section 111.0.2 to determine is RACT is required? IFS Reg 6 Review 40 CFR.Part 60,Subpart KKK to determine I applicable to this souks? No [Review 40 CFR.Part 50 Subpart 0000 to determine if 605330 ardor 605305 is applicable, No Reg.7 Review SectlpnXVII F to determine is TSAR is applicable? Yes 13WE2750 CPS 123/9004 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1 F,Serial number 2004238).The pneumatic pump is controlled by 006 six enclosed flares.Each flare has a minimum control efficiency of 95%. Pump Information Manufactur Sandpiper Model Number:G1F Serial Pump Number:2004238 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(10.4-3) Ex=O'MW'Xx/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 eeo scf/hr MW 23.14 lb/lb-mai Hours or Op. 8760 bwrsryr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy CO2 22509 44 0.0428 CO2 1.568 13734.885 6.867 nitrogen 07677 28 0.0093 nitrogen 0.340 2981.026 1.491 methane 714481 16.04 0.4953 methane 18.143 158931.944 79.466 ethane 127601 30.07 0.1658 ethane 6.074 53211.273 26.606 propane 79712 44.09 0.1519 propane 5.564 48739.374 24.370 isobutane o 7782 58.12 0.0195 isobutane 0.716 6272.389 3.136 n-butane 24244 58.12 0.0609 n-butane 2.231 19540.966 9.770 isopentane 04363 72.15 0.0136 isopentane 0.498 4365.537 2.183 n-pentane 05552 72.15 0.0173 n-pentane 0.634 5555.229 2.778 cyclopentane 30471 70.15 0.0014 cyclopentane 0.052 458.210 0.229 n-hexane 31198 86.18 0.0045 n-hexane 0.163 1431.790 0.716 cyclohexane 00374 84.18 0.0014 cyclohexane 0.050 436.613 0.218 Other hexanes 0.1932 86.18 0.0072 Other hexane 0.264 2309.031 1.155 heptanes O0830 100.21 0.0036 heptanes 0.132 1160.416 0.580 methylcyclohexa 00265 98.19 0.0011 methylcycloh9 0.041 360.852 0.180 224-TMP 70034 114.22 0.0002 224-TMP 0.006 53.856 0.027 Benzene 00219 78.11 0.0007 Benzene 0.02] 237.229 0.119 Toluene 0.0148 92.14 0.0006 Toluene 0.021 186.559 0.093 Ethylbenzene 00024 106.17 0.0001 Ethylbenzene 0.004 35.337 0.018 Xylenes 0.0052 106.17 0.0002 Xylenes 0.009 76.563 0.038 C8+Heavies 0.0531 114.23 0.0026 C8+Heavies 0.096 841.184 0.421 Mass Fraction VOC: 0.2869 Total VOC 46.031 Heating Value I 1329 BTU/scf combusioc omission factor source AP-42:Chapter 13.5 007 I lb NOLMMBIu 037 lb CO/MMBIu 1 13WE2759.CP2 123/9884 One(Il pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model O1F.Serial number 2004238).The pneumatic pump is controlled by 006 six enclosed flares.Each flare has a minimum contra,efiioency of 95%. Notes Mole 5,MW.and mass fractions are based on weighted average of 7 gas samples collected from different weds at this site.Samples collected in 20 Emissions are based on 8760 hours of operation per year. Assume MW of 08+s 11423 Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 17515 lh/MMscf 875.7716/MMscf 46.0 tpy 2.3 tpy Gas Analysts Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.3 tpy 1.3 spy AP-42 Benzene 45135 lb/MMscf 2.257 lb/MMscf 237 lb/yr 12 lb/yr Gas Analysis n-Hexane 272.41 lb/MMscf 13.621 lb/MMscf 1432 lb/yr 72 lb/yr Gas Analysis Toluene 35.495 lb/MMscf 1.7747 lb/MMscf 187 lb/yr 9 lb/yr Gas Analysis Ethylbenzene 8723216/MMscf 0.3362 lb/MMscf 35 lb/yr 2 lb/yr Gas Analysis Xylenes 14.567 lb/MMscf 0.72831b/MMscf 77 lb/yr 41h/yr Gas Analysis 13WE2759.CP2 123/9684 Nine low-pressure separators controlled by six enclosed flares during VRU downtime.Each flare has a 007 minimum control efficiency of 95%. Equipment Description This source vents natural gas from: low-pressure separators during VRU downtime Emissions from this source are: routed to a flare INatural gas venting from low-pressure separators during VRU downtime.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 C=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/Ib-mol)at 60F and 1 atm MW Throughput(O) 39961 lb/ba-molr 1 0.0167991841softhr MMscf/d mole% MW Ibx/lbmol mass fraction lb/hr Ib/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 000 CO2 2.01 44.01 0.884 0.022 1.63 14301.67 7.15 N2 1.91 28013 0.535 0.013 0.99 8654.54 4.33 methane 24.02 16.041 3.854 0.096 7.12 62348.73 31.17 ethane 20.08 30.063 6.036 0.151 11.15 97656.49 48.83 propane 27.78 44.092 12.248 0.307 22.62 198156.75 99.08 isobutane 3.80 58.118 2.207 0.055 4.08 35703.93 17.85 n-butane 12.91 58.118 7.503 0.188 13.86 121386.95 60.69 isopenlane 2.33 72.114 1.682 0.042 3.11 27205.25 13.60 n-pentane 2.87 72.114 2.073 0.052 3.83 33538.13 16.77 cyclopentane 0.20 70.13 0.142 0.004 0.26 2289.84 1.14 n-Hexane 0.48 86.18 0.413 0.0103 0.76 6688.34 3.34 cyclohexane 0.15 84.16 0.127 0.003 0.23 2049.20 1.02 Other hexanes 0.81 86.18 0.697 0.017 1.29 11281.08 5.64 heptanes 0.24 100.21 0.243 0.006 0.45 3931.56 1.97 methecyclahexane 0.09 98.19 0.088 0.002 0.16 1423.37 0.71 224-TMP 002 114.23 0.023 0.0006 0.04 367.77 0.18 Benzene 0.08 78.12 0.066 00017 0.12 1069.24 0.53 Toluene 0.05 92.15 0.045 0.0011 0.08 724.56 0.36 Ethylbenzene 0.01 106.17 0.007 0.0002 0.01 120.24 0.06 Xylenes 0.01 106.17 0.015 0.0004 0.03 240.48 0.12 08+Heavies 0.14 580 0.811 0.020 1.50 13127.67 6.56 VOC mass frac 0.7104 Total VOC(Uncontrolled) 229.65 Notes Mole%,MW,and mass fractions are based on average of LP separator gas samples collected 8/11/2014 from Antelope 11-41-33HNC,Antelope 811-V41-f Flowrate is based on Promax model,assuming 15%VRU downtime and applying a 20%safety factor 13WE2759.CP2 12319B84 Nine low-pressure separators controlled by sin enclosed flares during VRU downtime.Each flare has a 007 minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Abutec and LEED Model Serial Number 20044-003.20044-010.20044-001,20044-012,20674,20663 Gas Healing Value 2232 Btu/scf Throughput 13685.95922 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress low-pressure separator gas 10 sales line.The VRU is considered pad of the process and not included as an air pollution control device Make Model Requested Control Efficiency Annual Bypass Time Backup ] Flare 'Overall Control I 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBIu 0.37 [lb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOc 74906 lb/MMscf 3745.3 lb/MMscf 229.7 tpy 11.5 tpy Gas Analysts Nov 0.07 lb/MMBTU 0.0716/MMBTU 0.5 tpy 0.5 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 2.5 spy 2.5 tpy AP-42 Benzene 174.38lb/MMscf 8.7189 lb/MMscf 1069 lb/yr 53 lb/yr Gas Analysis n-Hexane 1090.8 lb/MMscf 54.539 lb/MMscf 6688 lb/yr 334 lb/yr Gas Analysis Toluene 118.17 lb/MMscf 5.9083 lb/MMscf 725 lb/yr 36 lb/yr Gas Analysts Ethvlbenzene 19.609 lb/MMscf 0.9805 lb/MMscf 1.20 lb/yr 6 lb/yr Gas Analysis Xylenes 39.218 lb/MMscf 19609 lb/MMscf 240 lb/yr 12 lb/yr Gas Analysis 224-TMP 59.978 lb/MMscf 2.9989 lb/MMscf 368 lb/yr 18 lb/yr Gas Analysis Regulatory Applicability AOCC Regulation 1 This source is subject to the opacity requirements for flares in Section ILA.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 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." AOCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 13WE2759.CP2 123/9884 One emergency flare used to combust separator gas during emergencies or when the pipeline is not 013 available.Flare has a minimum control efficiency of 95%. The flare is not enclosed. 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 INatural gas venting from a well head separator when the sales gas pipeline is not available or during emergencies.Emissions from this source are routed to Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equaflon(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 H.SG of gas'MW of air Xx=mass traction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(0) 15 MMscfNr 1712.328767 scf/hr MW 2307 Ibllb-mot 0.04109589 MMscf/d - mole% MW Ibxllbmol mass fraction lb/hr lb/yr tpy Helium 000 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 1.77 44.01 0.778 0.034 3.51 3078668 15.39 N2 8.75 28.013 2.452 0.106 11.08 97038.44 48.52 methane 57.97 16.041 9.299 0.403 42.01 368040.01 184.02 ethane 11.51 30.063 3461 0.150 15.64 136994.47 68.50 propane 6.25 44.092 2.754 0.119 12.44 109002.06 54.50 isobutane 094 58.118 0.549 0,024 2.48 21713.74 10.86 n-butane 1.96 58.118 1.137 0.049 5.14 45012.31 22.51 isopentane 0.40 72.114 0.291 0.013 1.31 11510.65 5.76 n-pentane 0.44 72.114 0.319 0014 1.44 12632.32 6.32 cyclopentane 0.05 70.13 0.032 0.001 0.15 1279.55 0.64 n-Hexane 0.10 86.18 0.085 0.0037 0.38 3366.48 1.68 cyclopexane 004 84.16 0.035 0.002 0.16 1402.30 0.70 Other hexanes 0.17 86.18 0.148 0.006 0.67 5863.20 2.93 hectares 0.09 100.21 0.085 0.004 0.38 3371.18 1.69 methylcyclohexane 0.02 98.19 0.021 0.001 0.09 812.20 0.41 224-IMP 000 114.23 0.001 0.000 0.01 58.77 0.03 Benzene 0 02 78.12 0.016 0.0007 0.07 615.27 0.31 Toluene 0.01 92.15 0.011 0.0005 0.05 426.71 0.21 Ethylbenzene 000 106.17 0.002 0.0001 0.01 67.23 0.03 Xylenes 0.01 106.17 0.008 00004 0.04 327.75 0.16 C8t Heavies 0.06 685 0.408 0.018 1.84 16158.05 8.08 VOC mass frac 0.256 Total VOC(Uncontrolled) 116.81 Notes Mole%,MW,and mass fractions are based on weighted average of 4 gas samples collected from different wells at this site.Samples collected 8/20/2013,8/11/2014 and 11 13WE2759.cp2 123/9984 One emergency flare used to combust separator gas during emergencies or when the pipeline is not 013 available.Flare has a minimum control efficiency of 95% The flare is not enclosed. Flaring Information Equipment Description Flare to combust separator gas when ipeline is not available or during emergencies. Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1326 Btu/scf Throughput 19890 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup I Flare Overall Control I 9500%j Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBtu 0.37 lib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor uncontrolled Emissions Controlled Emissions Source VOC 155751b/MMscf 778.73 lb/MMscf 116.8 tpy 5.8 tpy Gas Analysis Nor 0.071b/MMBTU 0.0716/MMBTU 0.7 tpy 0.7 tpy AP-42 CO 0.371b/MMBTU 0.371b/MMBTU 3.7 toy 3.7 spy AP-42 Benzene 41.018 lb/MMscf 2.0509 lb/MMscf 615 lb/yr 311b/yr Gas Analysts n-Hexane 224.43 lb/MMscf 11.2216 lb/MMscf 3366 lb/yr 168 lb/yr Gas Analysis Toluene 28.447 lb/MMscf 1.4224 lb/MMscf 427 lb/yr 2116/yr Gas Analysis Ethylbenzene 4.4821 lb/MMscf 0.7241 lb/MMscf 67 lb/yr 3lb/yr Gas Analysis Xylenes 21.850 lb/MMscf 1.0925 lb/MMscf 3281h/yr 16 lb/yr Gas Analysis Regulatory Applicability AOCC Regulation 1 This source is subject to the opacity requirements for flares in Section ILA5:'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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? Yes This separator is subject to Reg 7,Section XVILG.and control requirements of Reg 7,Section XVII.B.2 However,since this flare is used for emergency purposes,net used routinely.and must control high pressure,high volume flow intermittently,the emergency flare will be approved as an alternative control device per Reg 7,Sec XVII.B.2.e.The flare will have t0 meet Reg 7,Sec XVII.B except that it is not required to be enclosed 13WE2759.CP7 123/9884 Two vapor recovery towers(VRTs)controlled by six enclosed flares during VRU downtime.Each flare has a minimum 014 control efficiency of 95%. Equipment Description This source vents natural gas from: vapor recovery towers when the VRU is down Emissions from this source are: routed to a flare Natural gas venting from vapor recovery towers when the VRU is 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) Es=Q•MW*Xx/C Ex=emissions of pollutant s Q=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/Ib-mot)at 60F and 1 atm Throughput(CO 1.5 MMscf/r 172.6056 sct/hr MW 4971bIb-rod 0.004142534 MMscf/d mole% MW Ibsibmol mass fraction lb/hr lb/yr tpy Helium 000 4.0026 0.0000.000 0.00 0.00 0.00 CO2 151 44.01 0.664 0.013 0.30 2649.65 1.32 N2 036 28.013 0100 0002 0.05 397.19 0.20 methane 10.51 16.041 1.686 0.034 077 6725.70 3.36 ethane 1964 30.063 5.906 0.119 269 23560.37 11.78 propane 28.84 44.092 12.716 0.256 5.79 50731.16 25.37 Isobutane 3.59 58.118 2.084 0.042 0.95 8314.82 4.16 n-butane 13.38 58.118 7.773 0.156 3.54 31011.60 15.51 isopentane 2.63 72.114 1.896 0.038 0.86 7563.05 3.78 n-pentane 3.43 72.114 2.474 0.050 1.13 9868.10 4.93 cyclopentane 1.36 70.13 0952 0.019 043 3799.75 1.90 n-Hexane 300 86.18 2.565 0.0520 1.18 1031448 5.16 cydohexane 0.98 84.16 0824 0.017 0.38 3287.74 164 Other hexanes 5.81 86.18 5.011 0.101 2.28 19990.50 10.00 heptanes 2.06 100.21 2.082 0.041 0.94 8225.26 4.11 methylcyclohexane 075 98.19 0.739 0.015 0.34 2947.77 1.47 224-TMP 0.13 114.23 0.151 0.0030 0.07 601.55 030 Benzene 0.60 78.12 0.467 0.0094 0.21 1861.86 0.93 Toluene 0.15 92.15 0.143 0.0029 0.07 56946 0.28 Elhylbenzene 007 106.17 0.074 0.0015 0.03 296.07 0.15 Xylenes 0.12 106.17 0.127 0.0025 0,06 504.89 0.25 08+Heavies 1.09 116.6081422 1268 0.026 058 5057.76 2.53 VOC mass frac 0.832 Total VOC(Uncontrolled) 8247 Notes Mass fractions are based on Promax results for the VRT stream Flowrate is based on Promax results,assuming 15%downtime for VRU and applying 20%safety factor. 13WE2759.CP2 123/9684 Two vapor recovery towers(VRTs)controlled by six enclosed flares during VRU downtime.Each flare has a minimum 014 control efficiency of 95%. Flaring Information Equipment Description Flare to combust VRT gas when the VRU is down. Manufacturer Abutec and LEED Model Serial Number 20044-003.20044-010.20044-001,20044-012.20674,20663 Gas Heating Value 2758 Btu/scf Throughput 4170 165104 I MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress VRT gas to sales line.The VRU is considered part of the process and not included as an air pollution control device. Make Model Requested Control Efficiency Annual Bypass Time Backup I Flare 'Overall Control I 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NCX/MMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncomrol led E musion Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 109089 lb/MMscf 5454.516/MMscf 82.5 tpy 4.1 tpy Gas Analysis Nox 0.0716/MMBTU 0.07 lb/MMBTU 0.1 tpy 0.1 tpy AP-42 CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 0.8 tpy 0.8 spy AP-42 Benzene 1231.4 lb/MMscf 61.568 lb/MMscf 1862 lb/yr 93 lb/yr Gars Analysis n-Hexane 6821.6 lb/MMscf 341.08 lb/MMscf 10314 lb/yr 516 lb/yr Gas Analysis Toluene 376.62 lb/MMscf 18.831 tb/MMscf 569 lb/y/ 28 lb/yr Gas Analysis Ethylbenzene 195.81 lb/MMscf 9.7906 lb/MMscf 296 lb/yr 15 lb/yr Gas Analysis Xylenes 333.92 lb/MMscf 16.696 lb/MMscf 505 lb/yr 25 lb/yr Gas Analysis 224-TMP 397.85 lb/MMscf 19.892 lb/MMscf 602 lb/yr 30 lb/yr Gas Analysis Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section 11 A.5'YNo 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.' ACCC 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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.O.and control requirements of Reg 7,Section 30/11.8.2 13WE2759.CP2 123/9684 AIRS(County/Plant)123/9884 Permit No.13WE2759 Date 3/19/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions CPI. reportable Point# SCC Pollutant or CAS Factor Emisison Factor Source (tpy)' (Myr PTE(tpy)' EOI% 7 VOC 6.5722 lb/1000 qa Promax 2.9 3.5 70.7 95% Yes NOx 0.068 Ib/Mmbtu AP-42 Table 13.5 0.1 0.1 0.1 0% No CO 0.37 Ib/Mmbtu AP-42 Table 13.5 0.6 0.8 0.8 0% No Benzene 0.0515 lb/1000 ga Promo 46 55 1108 95% Yes 002 40400311 n-Hexane 0.2866 lb/1000 qa Promax 257 308 6168 95% Yes Toluene 0.008315/1000 ga Promos 7 9 179 95% No EMylbenzene 0.016415/1000 qa Promos 15 18 354 95% Yes Xylenes I 0.0148 lb/1000 ga Promos 13 16 319 95% Yes 224-UimeIDiipentane 0.0211 15/1000 qa Promax 19 23 453 95% Yes VOC 6.238 1511 000 qa CDPHE 2.6 52.2 95% Yes 003 40400315 Benzene 0.167 lb/1000 ga CDPHE 140 2790 95% Yes n-Hexane 0.52415/1000 qa CDPHE 438 8769 95% Yes VOC 2.8748 15/1000 qa AP-42 10.4 30.9 685%_Yes Benzene 0.0264 lb/1000 ga AP-42 190 568 66.5% Yes 0(14 40600132 n-Hexane 0.1828 lb/1000 qa AP-421318 3935 66.5% Yes Toluene 0.0162 lb/1000 ga AP-42 117 348 66.5% Yes Ethylbenzene 0.000715/1000ga AP-42 5 15 66.5% No Xylenes 0.0053 lb/1000 qa AP-42 39 115 66.5% No VOC 17515 lb/MMsct Gas Analysis 2.3 46.0 95% Yea NOx 006815/MMBTU AP-42 0.2 0.2 0% No CO 0.37 lb/MMBTU AP-42 1.3 1.3 0% Yes Benzene 45.135 lb/MMscf Gas Analysis 12 237 95% No 006 31000299 n-Hexane 272.41 Ib/MMscf Gas Analysis 72 1432 95% Yes Toluene 35.495 lb/MMscf Gas Analysis 9 187 95% No E15ylbenzene 6.7232 lb/MMsof Gas Analysis 2 35 95% No Xylenes 14.567 Ib/MMscf Gas Analysis 4 77 95% No _ ____--- VOC 7491E lb/MMscf Gas Analysis 11.5 229.7 95% Yes NOx 0.068 lb/MMBTU AP-42 0.5 0.5 0% No CO 0.37 lb/MMBTU AP-42 2.5 2.5 0% Yes Benzene 174.38 lb/MMscf Gas Analysis 53 1069 95% Yes 007 31000205 n-Hexane 1090.78 lb/MMscf Gas Analysis 334 6688 95% Yes Toluene 118.17 I5/MMsc1ct Gas Analysis 36 725 95% Yes Elbylbenzene 19.61 IIMMMsct Gas Analysis 6 120 95% No AIRS(County/Plant)123/9084 Permit No.13WE2T59 Date 3/19/2015 Controlled Controlled Actual Requested NCRP 7 Uncontrolled Emission Emissions Emissions Ctrl. reportable Point# SCC Pollutant or GAS Factor Emisison Factor Source (lpyf (tpy)' PTE Rpy)' Eff% Xylenes I 39.22 lb/MMscf Gas Analysts 12 240 95% No 224-VimetM1 entane 59.98 IbiMMscf Gas Analysis 18 368 95% Yes VOC 15575 lb/MMscf Gas Analysis 0.8 116.8 95%% Yes COx 0.068 0. Ib/MMBTU AP-42 0.7 07 0 No CO 1 lblMMscE AP-42 s 3.7 3.7 0% Yes 13 31000205 Benzene 018224. lb/MMscf Gas Analysts 31 3366 95% Yes T-Hexane 2844 lb/MMscf Gas Analysis 2195% Yes Toluene 28.447.45 Ib/MMscf Gas Analysis 21 95% Yes Xyleaenzene 44821 lb/MMscf Gas Analysis 3 67 95% No Xylenes 21.850 lb/MMscf Gas Analysis 16 328 95% Yes VOO 109089 lb/MMscf Gas Analysis 4.1 82.5 95% Yes NOx 0.068 Ib/MMBTU AP-42 0 I 0.1 0% No CO 0.37 Ib/MMBTU AP-42 0.8 0.8 0% No Benzene 12314 lb/MMscf Gas Analysis 93 1862 95% Yes 14 31000205 n-Hexane 5821.6 lb/MMscf Gas Analysis 516 10314 95% Yes Toluene 376.62 lb/MMscf Gas Analysis 28 569 95% Yes Ethylbenzene 195.81 lb/MMscf Gas Analysis 15 296 95% Yes Xylenes I 333.92 lb/MMscf Gas Analysis 25 505 95% Yes 224-trimetbyloenlane 397.851b/MMscf Gas Analysts 30 602 95% Yes `c 3 s d o _ :--: A0 00 > m e Eicti `o ,zO � O cr7 :. a.Z Z Z �.-. c c : omv, ao >w Y c a � � ¢ O -0 Em ❑ W L I❑L®❑ �` T_O `O r1 r� Nl Y_Y i L. Nn. 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GI F S X C F p $= O 9 Y•V 2 % N Fz 6.5 L v c 7 u u u u N u On_ r t a E&P Storage Tank Air Pollutant Emissions Notice (APEN) Addendum Form' Company Name: Bonanza Creek Engery Operating Company LLC Source Name: Antelope B-33 Production Facility(COGCC#432287) Emissions Source AIRS ID2: 123/9B84/003 Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well 05-123-37227 State Antelope U-Y-32HNB ❑ 05-123-39063 Antelope 11-41-33HNB ❑ 05- 123-39067 Antelope A11-U41-33HNC ❑ 05- 123-39065 Antelope B11-V41-33HNC ❑ 05- 123-37054 Antelope B-V-33HNB ❑ 05- 123-37267 State Antelope P-T-32HNB ❑ 05-123-39004 State Antelope 41-44-32HNB 05-123-39279 State Antelope U41-Y44-32HNC 05-123-39003 State Antelope P41-T44-32HNC - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ - - ❑ Footnotes: Attach this addendum to associated APEN form when needed to report additional wells. 2 If this is a newly report source that has not been assigned an AIRS ID by the APCD, enter N/A Form APCD-212 Antelope B-33 Form APCD-212-EP-PWStorageTank-APEN-Addendum.docx r`'OA o ♦ ♦ ° ev'e ,—,>, •♦ ♦ ♦ ♦ m d� m n m m re .Ea°e m dCA ' o ° ens ' •• J m ,A. tY ? n n 0 ^I 0 (1. 25° ro. o. 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