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Home My WebLink About20142108.tiff ,* CQPHE COLORADO CO > Department of Public Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150OSt RECEIVED PO Box 758 Greeley, CO 80632 MAR 2 7 2015 March 24, 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On March 25, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company LLC - State Seventy Holes P-4 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 & 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 lfA.J 0! l0$ Li-1- ol5 Cc �r��' �� a 4300 Cherry Creek Drive S.. Denver, CO 80246-1530 P 303-692.2000 www.colorado.gov/cdphe John W. Hickenlooper,Governor Larry Wolk,MD,MSPH. Executive Director and Chief Medical Officer I CE Air Pollution Control Division co Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company LLC - State Seventy Holes P-4 Production Facility - Weld County Notice Period Begins: March 25, 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 LLC Facility: State Seventy Holes P-4 Production Facility Oil and gas exploration and production facility NWNE Sec 4 T4N 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 14WE0461 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 AVCOLORADO m is rill 1> ri 1. i fraSTATE OF COLORADO doe mm,=x�y s_0 Hth'. c�v4�iW :re CptQRb COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION TELEPHONE: (303) 692-3150 '. CONSTRUCTION PERMIT PERMIT NO: 14WE0461 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 State Seventy Holes P-4 Production Facility, located in the NWNE Section 4, Township 4N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Twelve 750 bbl above ground atmospheric condensate CNDTK-1 003 storage tanks controlled by four enclosed flares. Each flare has a minimum control efficiency of 95%. Two (2) 500 bbl above ground produced water storage tanks PW 004 and two (2) 60 bbl concrete vaults for produced water. The 500 bbl storage tanks are controlled by four enclosed flares. Each flare has a minimum control efficiency of 95%. Hydrocarbon Loadout to Tanker Trucks. Loadout is controlled by using dedicated vapor balance service and four enclosed TLO 005 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 (Sandpiper, Model G1 F, Serial number 2091628). The P-1 007 pneumatic pump is controlled by four enclosed flares. Each flare has a minimum control efficiency of 95%. FL-1 008 Emergency venting to a candlestick flare. Six low-pressure separators controlled by four enclosed flares SEP-1 to 009 during VRU downtime. Each flare has a minimum control SEP-6 efficiency of 95%. Two vapor recovery towers (VRTs) controlled by four VRT-1, 015 enclosed flares during VRU downtime. Each flare has a VRT-2 minimum control efficiency of 95%. AIRS ID: 123/9C0A Page 1 of 18 olor , yDepa en P .li " ealth and Environment it Pollution Control Division Point 007: m •e.A � . ed f=n ther =. sF,. 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. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 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. AIRS Points 009 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 flowrate of natural gas vented from the low pressure separators and vapor recovery towers. The operator shall use 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. 5. 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.) 6. 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 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) AIRS ID: 123/9COA Page 2 of 18 a r a t . olora Depa en,of P IicgHealth and Environment IP 43it . I_ Air Pollution Control Division F A P til rilk E a40 AU t I . Annual Limitsx:l.,a / ,Wf.n41 s La ati s V. Facility AIRS Tons per Year Equipment ID Point NO, VOC CO Emission Type CNDTK-1 003 --- 4.4 --- Point PW 004 2.6 Point TLO 005 9.2 Point P-1 007 --- 2.0 1.2 Point FL-1 008 --- 6.3 3.7 Point SEP-1 to SEP-6 009 --- 17.0 4.7 Point VRT-1,VRT-2 015 -- 2.2 --- Point 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. 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-1 003 Enclosed Flare VOC PW 004 Enclosed Flare (500 bbl tanks only) VOC TLO 005 Vapor balance and Enclosed Flare VOC P-1 007 Enclosed Flare VOC FL-1 008 Open Flare VOC SEP-1 to 009 Enclosed Flare VOC SEP-6 VRT-1, 015 Enclosed Flare VOC VRT-2 AIRS ID: 123/9COA Page 3 of 18 olor Depa en w P .Ii ealth and Environment II it Pollution Control Division PROCESS LIMITATIONS AND RECORDS 9. 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-1 003 Condensate Throughput 350,400 BBL PW 004 Produced Water Throughput 398,580 BBL TLO 005 Condensate Loaded 350,400 BBL P-1 007 Natural Gas Consumed 5.3 MMSCF FL-1 008 Total Gas Vented from All Separators to 15.2 MMSCF Emergency Flare SEP-1 to 009 Total Gas Vented from Six Low-Pressure 13.4 MMSCF SEP-6 Separators during VRU Downtime VRT-1, 015 Total Gas Vented from Two Vapor Recovery 0.8 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 month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 10. AIRS Points 009 and 015: Upon installation of the flow meter required under Condition 4, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from all low pressure separators and VRTs during VRU downtime using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented to the enclosed flare 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 9 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 11. 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 XVI1.B.2.b shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 5.) 13. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) AIRS ID: 123/9COA Page 4 of 18 W s olora Deparen' ' P" liealth and Environment • 4P , it Pollution Control Division 14. AIRS Point 00A he ar ve. `_thisfArrra subj:,., ,.: 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. 15. AIRS Point 003: 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. AIRS Point 003: 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. 17. AIRS Points 003 and 004: 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 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. 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. 18. AIRS Points 003 and 004: 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)(b) Control requirements of Section XVII.C.1.b. must be achieved by May 1, 2015. 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 constructed before May 1, 2014 subject to Section XVII.C.1. must conduct audio, AIRS ID: 123/9COA Page 5 of 18 Ill olor Depa en P •li ealth and Environment r it Pollution Control Division E i visual, ( I ) _ =diti- I insp hm: s 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; XVII.C.1.d.(iv) Visual inspection of the air pollution control 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 XVII.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 AIRS ID: 123/9COA Page 6 of 18 rgaak 2r414., ffi r 3 oloraIDepar( en, hi P'.oli ealth and Environment '€ i a ,ir Pollution Control Division . Atcontairti stabkize ;lkids. 'mum ents 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)(b) A storage tank constructed before May 1, 2014, must comply with the requirements of Sections XVII.C.2.a. and XVII.C.2.b. by May 1, 2015. Approved instrument monitoring method inspections must begin within ninety (90) days of the Phase-In Schedule in Table 1, or within thirty (30) days for storage tanks with uncontrolled actual VOC emissions greater than 50 tons per year. 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 AIRS ID: 123/9C0A Page 7 of 18 olor Depa en • P .li ealth and Environment it Pollution Control Division reque ._ - . :'.iti. =r ' a 'Id • year- `•- 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 XVI I.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. XVII.C.3.f. A list of equipment associated with the storage tank 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. 19. AIRS Point 005: 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. AIRS Point 005: 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 20(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. 21. AIRS Point 005: 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. OPERATING & MAINTENANCE REQUIREMENTS 22. 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.) AIRS ID: 123/9COA Page 8 of 18 w lid olor Depa enhf P Health and Environment ��, �ir Pollution Control Division 23. AIRS Point 0 t,..4,,i.ri:*.wrietw Saler o .g .!•,t at whi&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 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 24. AIRS Point 008: Within 180 days of startup, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare when the flare is receiving gas from the separator. This measurement shall consist of a minimum twenty-four consecutive reading taken at fifteen second intervals over a 6 minute period. (Reference: Regulation No. 1, Section II.A.5). 25. AIRS Point 015: 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 the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4- trimethylpentane content (weight fraction) of this emission stream used in the permit application. Results of testing shall be used to determine site-specific emission factors using Division approved methods. Results of site-specific sampling and analysis shall be submitted to the Division as part of the self-certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. ALTERNATE OPERATING SCENARIOS 26. AIRS Point 007: 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. 27. AIRS Point 007: 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. AIRS ID: 123/9C0A Page 9 of 18 j olor Depa en Pk•li • ealth and Environment 4 it Pollution Control Division 28. AIRS Point p r e d a 't:+erated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 29. All previous versions of this permit are cancelled upon issuance of this permit. 30. This permit replaces the following permits and/or points, which are cancelled upon issuance of this permit. Existing Existing Permit No. Emission Point New Permit No. GP01 123/9C0A/003 14WE0461 GP05 123/9C0A/004 14WE0461 31. 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. 32. 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). AIRS ID: 123/9COA Page 10 of 18 tA az olora' Depar em P i ealth and Environment Eh, �r dr ;fa Air Pollution Control Division a TA rtfF GENERAL TERMS f%�d. • to•jo, waft ..L 33. 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. 34. 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. 35. 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. 36. 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. 37. 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. 38. 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. 39. 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. AIRS ID: 123/9COA Page 11 of 18 olor epa en P li ealth and Environment it Pollution Control Division By: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 2 This Issuance Modification to convert AIRS Point 003 from GP01 to this permit.Also added tanks, increased throughput and emissions. Modification to convert AIRS Point 004 from GP05 to this permit. Also added tank, increased throughput, and increased emissions. Modification to Point 005 to increase throughput and emissions and to add control. Cancellation of Point 006. Modification to Point 007 to decrease emissions. Modification to Point 009 to add 5 LP separators, account for additional process control and increase emissions. Adding new point 015. Issuance 1 September 2, Issued to Bonanza Creek Energy Operating 2014 Company LLC for Points 005-009 • AIRS ID: 123/9C0A Page 12 of 18 fl i p olora'+ Depar nen? P� li Health and Environment ,pp + to- ,as it Pollution Control Division ;,7�—Sr'; 4-1'.1=-4:11 :jai—el il Notes to Permit Holder 3f''NT"' of��FtIs Id guantl "':4-9' 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&childpaqename=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 i Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (lb/yr) reportable? (Ib/yr) Benzene 71432 741 Yes 37 n-Hexane 110543 4,262 j Yes 213 Toluene 108883 537 Yes 27 003 Ethylbenzene 100414 39 No 2 Xylenes 1330207 156 No 8 2,2,4- I540841 345 Yes 17 trimethylpentane Benzene 71432 2,790 Yes 140 004 n-Hexane 110543 8,769 I Yes 438 Benzene 71432 247 No 83 n-Hexane 110543 1,999 Yes 670 005 Toluene • 108883 139 No 46 Ethylbenzene ! 100414 10 No 3 Xylenes 1330207 34 No 11 Benzene 71432 166 i No 8 n-Hexane 110543 948 I Yes 47 007 Toluene 108883 107 No 5 Ethylbenzene 100414 12 No 1 AIRS ID: 123/9COA Page 13 of 18 olor Depa en Px,•li "' ealth and Environment ?' it Pollution Control Division 11".10 Xyl ..0 t s 2 Benzene 71432 617 Yes 31 n-Hexane 110543 3,560 Yes 178 008 Toluene 108883 451 Yes 23 Ethylbenzene 100414 51 No 3 Xylenes 1330207 141 No 7 Benzene 71432 1,461 Yes 73 n-Hexane 110543 8,286 Yes 414 009 Toluene 108883 876 Yes 44 Ethylbenzene 100414 83 No 4 Xylenes 1330207 192 No 10 Benzene 71432 820 Yes 41 n-Hexane 110543 4,650 Yes 233 Toluene 108883 556 Yes 28 015 Ethylbenzene 100414 37 No 2 Xylenes 1330207 138 No 7 2'2'4 540841 204 No 10 trimethylpentane 5) The emission levels contained in this permit are based on the following emission factors: Point 003: Uncontrolled Controlled lb/BBL lb/BBL Condensate Condensate Pollutant Throughput Throughput Source NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42, Table 13.5 CO 0.37 lb/MMBtu 0.37 Ib/MMBtu AP-42, Table 13.5 VOC 0.4990 0.0249 Promax n-Hexane 0.0122 0.0006 Promax Benzene 0.0021 0.0001 Promax Toluene 0.0015 0.0001 Promax Ethylbenzene 0.0001 0.00001 Promax Xylenes 0.0004 0.00002 Promax 2,2,4- 0.0010 0.00005 Promax trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. A HHV of 2,591 BTU/scf was used for combustion calculations. AIRS ID: 123/9C0A Page 14 of 18 ,olorJ Depa ant if Pk li ealth and Environment 144 it Pollution Control Division ygmmv... •tea `7 i V,, Point 004: S5• `r a OA 'AM rallai Emission Factors Emission Factors Uncontrolled Controlled 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 005: Uncontrolled Controlled Pollutant lb/BBL loaded Ib/BBL loaded Source VOC 0.1563 0.0524 AP-42 Benzene 0.0007 0.0002 AP-42 n-Hexane 0.0057 0.0019 AP-42 Toluene 0.0004 0.0001 AP-42 Ethylbenzene 0.00003 0.00001 AP-42 Xylenes 0.0001 0.00003 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) =3.05 psia M (vapor molecular weight) =55.58 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 007: Emission Emission Factors - Factors - Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (Ib/MMBTU) VOC 14,940 747.01 Gas Analysis Benzene 31.533 1.5766 Gas Analysis n-Hexane 180.32 9.0159 Gas Analysis Toluene 20.422 1.0211 Gas Analysis Ethylbenzene 2.2411 0.1121 Xylenes 5.8828 0.2941 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 1,262 BTU/scf was used for combustion calculations. AIRS ID: 123/9C0A Page 15 of 18 i" ' olor Depa en P ell ealth and Environment it Pollution Control Division Point 008: �+.... ,:: > f . 1+.' ...,. _...... Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx ___ 0.068 0.068 AP-42 (lb/MMBTU) CO ___ 0.37 0.37 AP-42 (lb/MMBTU) VOC 27.4 16483.1262 824.1563 Gas Analysis Benzene 0.07 40.6059 2.0303 Gas Analysis Toluene 0.05 29.6631 1.4832 Gas Analysis Ethylbenzene 0.006 3.3616 0.1681 Gas Analysis Xylenes 0.015 9.2444 0.4622 Gas Analysis n-hexane 0.39 234.2095 11.7105 Gas Analysis Note: Emissions were calculated using a higher heating value of 1,318 Btu/scf Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx --- 0.068 0.068 AP-42 (lb/MMBTU) CO(Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 57.2 50,250 2,512.5 Gas Analysis Benzene 0.12 108.63 5.4313 Gas Analysis Toluene 0.07 65.161 3.2581 Gas Analysis Ethylbenzene 0.01 6.1629 0.3081 Gas Analysis Xylenes 0.02 14.287 0.7143 Gas Analysis n-hexane 0.70 616.22 30.811 Gas Analysis Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 7/2/2014 of the gas vented from the low pressure separator from State Seventy Holes F11-J14- 3HNC 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 1,879 BTU/scf was used for calculations. Point 015: Weight Emission Emission Fraction Factors Factors Source Pollutant of Gas (%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx --- 0.068 0.068 AP-42 (lb/MMBTU) CO (lb/MMBTU) --- 0.37 0.37 AP-42 VOC 80.7 100,735 5,036.8 Gas Analysis Benzene 0.79 992.12 49.606 Gas Analysis Toluene 0.54 672.85 33.642 Gas Analysis Ethylbenzene 0.04 44.401 2.2201 Gas Analysis AIRS ID: 123/9COA Page 16 of 18 A olor ipj.,Depa. en' P ' lid ealth and Environmentit Pollution Control Division ii atrafftelghtas apiatiisin lg .. sion Pollutant Fraction Factors Factors Source of Gas (°/u) Uncontrolled Controlled lb/MMscf lb/MMscf Xylenes 0.13 167.07 8.3533 Gas Analysis n-hexane 4.51 5,626.0 281.30 Gas Analysis 2,2,4- 0.20 246.38 12.319 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. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 2,628 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: VOC, CO, HAPs NANSR Synthetic Minor Source of: 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.qpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources • NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart PA—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 ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN —Subpart XXXXXX AIRS ID: 123/9C0A Page 17 of 18 olorA•epa en P +li ealth and Environment it Pollution Control Division 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.00v/pacific/cdphe/air-permit-self-certification AIRS ID: 123/9C0A Page 18 of 18 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 03/05/2015 Application Date: 08/22/2014 Facility Identifiers Permit No. 14W E0461 Potentially located in ozone nonattainment area AIRS County 123 Weld Facility 4 9COA Facility Type: exploration and production facility 0 Located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: F VOC F NOx F CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Seventy Holes P-4 Production Facility Source Location: NWNE Section 4 T4N R62W 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 State Seventy Holes P-4 Production Facility,located in the NWNE Section 4 T4N R62W,Weld County,Colorado. Point Name Type Control Action 003 CNDTK-1 Condensate Tanks Flare Cancelling GP01 and adding to facility-wide permit 004 PW Water Tanks Flare Cancelling GP0S and adding to facility-wide permit 005 TLO Loadout Flare Modifying by increasing throughput and adding control Existing point- In first application(8/2014), source requested to increase counts and emission limit from 7.9 to 29.8 tpy.On 006 FUG Fugitives None 3/12/2015, source requested to cancel fugitives since subject to Reg 7 and now APE N-exempt 007 P-1 Pump Flare Modifying by decreasing emission limit based on updated gas analysis SEP-1 to Separator Venting Flare Modifying by adding 5 LP separators, 009 SEP-6 increasing throughput and emissions VRT-2 VRT- 015 Separator Venting Flare New point 'Pt 008(an emergency flare)is not being modified and will remain in the facility-wide permit. *Pts 10-014 are engines covered by GP02 003 Twelve 750 bbl above ground atmospheric condensate storage tanks controlled by four enclo: Requsted Throughput 350400 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.4990 lb/bbl 87.4 tpy 4.4 tpy Promax Benzene 0.0021 lb/bbl 741 lb/yr 37 lb/yr Promax n-Hexane 0.0122 lb/bbl 4262 lb/yr 213 lb/yr Promax Toluene 0.0015 lb/bbl 537 lb/yr 27 lb/yr Promax Ethylbenze 0.0001 lb/bbl 39 lb/yr 2 lb/yr Promax Xylenes 0.0004 lb/bbl 156 lb/yr 8 lb/yr Promax 2,2,4-TMP 0.0010 lb/bbl 345 lb/yr 17 lb/yr Promax Nox 0.068 lb/Mmbtu 0.2 tpy 0.2 tpy AP-42 Table 1 CO D.37 Ib/Mmbtu 0.9 tpy 0.9 tpy AP-42 Table 1 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. 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 odorfree 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 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 the nonattainment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject to this since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions are greater than 6 tpy. 14WE0461.CP2 123/9COA 004 Two(2)500 bbl above ground produced water storage tanks and two(2)60 bbl conc Emissions Calculations Requsted Throughput 398580 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 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. 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. 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. 14WE0461.CP2 123/9COA 005 Hydrocarbon Loadout to Tanker Trucks.Loadout is controlled by using dedicated vapor balance 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 Saturation Factor 1 AP-42 P True Vapor Pressure 3.05 psia Calculated TVP of liquid based on oil analysis an. M Molecular Weight of Vaf 55.58 lb/lb-mole Calculated MW of liquid based on oil analysis am T Liquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver,CO L 3.72 lb/10^3 gal 1.56E-01 lb/bbl Annual requested Throughput 350400 BBL/yr 14716800 gal/yr Annual requested VOC emissions 54783 lb/yr 27.39 tpy Control: Flare Efficiency: 66.50% Source assumes 95%control efficiency and 70%collection efficiency NCRPs Component Mass Fraction VOC 0.9229 Benzene 0.0045 n-hexane 0.0365 Toluene 0.0025 Ethylbenzen 0.0002 Xylenes 0.0006 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 0.1563 lb/bbl 27.4 tpy 9.2 tpy AP-42 Benzene 0.0007 lb/bbl 247 lb/yr 83 lb/yr AP-42 n-Hexane 0.0057 lb/bbl 1999 lb/yr 670 lb/yr AP-42 Toluene 0.0004 lb/bbl 139 Ib/yr 46 lb/yr AP-42 Ethylbenzen 0.00003 lb/bbl 10 Ih/yr 3 lb/yr AP-42 Xylenes 0.0001 lb/bbl 34 lb/yr 11 lb/yr AP-42 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 1238 BBLs)per day of crude oil on an annual average basis? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section 11.0.1.1 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,Pail B,Section II.D.1.1 14WE0461.CP2 E0461.CP2 123/9C0A 006 Fugitive equipment leaks AS OF 1)12015,THIS SITE IS SUBJECT TO REG 7,)(VII F.UNDER REG 7.27111 F,SOURCE CAN USE TABLE 2-8 EMISSION FACTORS. WITH TABLE 2-8.FUGITIVE EMISSIONS ARE NOW APEN-EXEMPT.SOURCE REQUESTED TO CANCEL APEN Regulation 7 Information Operating Hours. 8760 hours/year Emission Fader Source Screening EFs-EPA-451R-95.017 Table 2-0 Control Efficiency Source: Nene Calculators Emission Factor pglbr- Emissions Service Component Type Count «s1 Control(%)Pollutant Mass Fraction plsq Table 2-4 Table 24 Reg.3 Connectors 40% E00EO4 100E-05 00% VOC 0253894 02385478 Flanges 302 390E-00 5.79E-06 0 0% Benzene 0000535 0.000527 Open-Ended Lines 144 ?WE03 1.50E-05 0 0% Toluene 0000345 0 0003251 Gas Pump Seals 14 ?40E-03 350E-04 00% Elny1Mnzene 0.000036 3382E-05 Valves 500 4.50E-03 2.50E-05 00% Xylenes 0.000099 9 302E-05 Other 279 980E-03 1.20E-04 0 0% n-Hexane 0.003064 0.0028788 Connectors 0 ]50E-06 7.50E-06 0 VOC 1 0 Flanges 0 390E-07 3.90E-01 00% Benzene 0 Open-Ended Lines 0 1,40E-04 7.20E-06 00% Toluene 0 Heavy 011 Pump Seals 0 0.00E-100 000E+00 00% Etbylbenzene 0 Valves 0 BODE06 8.40E-06 30% Xylenes 0 GIber 0 310E-05 330E-05 0.0% n-Hexane 0 Connectors 1876 2.10E-04 9.70E-06 00°% VOC 0997685 02836728 Flanges 66 110E-04 240E-06 0 Benzene 0010164 0.0028899 Open-Ended Lines 12 140E-03 30E-405 0.0°,6 Toluene 0 021017 00065416 Light Oil Pun%Seals 0 1.30E-02 5.10E-04 00% Elhobenzene 0.504404 00012522 Valves 268 250E-03 190E-05 0 0% Xylenes 5019504 00055456 Other 53 7.50E-03 110E-04 0.0% n-Hexane 0055576 0015802 Connectors 1.10E-04 1.0OE-05 00% vac 1 0 Flanges ?90E-06 2.90E-06 0 Benzene 0 Open-Ended',IBS 2.50E-04 3,50E-06 0 Toluene 0 Wa18rlOil Pomp Seals 2.40E-05 140E-05 0 0% Ethylbenzene 0 Valves 9.80E-05 970E-06 0 Xylenes 0 Other 140E 02 5.90E-05 00% n-Hesene 0 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source I WY VOC 0 1py 0.5 toy Screening EFs-EPA-453/R95-017 Table 2-8 Benzene 7 Iblyr 71Myr Screening EFs-EPA-53/R95LP Table 2- 000 Toluene n4 Iblyr 14 lb/yr Screening EFs-EPA-453/R-95-017 Table 2- 0.01 EONbenzene 3 Iblyr 31pryr Screening EFs-EPA-453/RA5-017 Table 2- 0.00 Xylenes 11 Iblyr 11 lb/yr Screening EFs-EPA-455R-95017 Table 2- 0.01 n-Hexane 37 lb/yr 371Nyr Screening EFs-EPA-053/R-95-017 Table 2- 002 VOC and HAP concentrations for gas service are based on weighted average of sales gas samples collected 712/2014 for Stale Seventy Hales A-E-3HNB8FJ-3HNB,7/2/2014 from Stale Seventy Holes F-11-314-3HNC,and 12/17/2013 h0m SIaIe Seventy Holes P-T-0HNB. Since site-specific and elhln 1 year CO appliW lion date,no Initial sampling required. Regulatory Applicability Reg.3 Review Regulation 3,Part B,Section III 0219 determine is RACT is required? Yes Review 40 CFR.Pan 60,Subpad KKK to determine J applicable 10 this source? No Rep.6 Review40 CFR,Pad 50,Subpan 0000 to determine 460.5380 and/or 60.5385 is applicable? No Reg.7 Review Section)(VII.F 10 determine is LOAR is applicable] Yes 14WEO461.CP2 123/nCsA One(1)pneumatic water transfer pump,rated at 600 sot/hr(Sandpiper, Model G1 F,Serial number 2091628).The pneumatic pump is controlled by 007 four enclosed flares.Each fare has a minimum control efficiency of 95%. Pump Information Manufactur Sandpiper Model Number:G1F Serial Pump Number:2091628 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=Q"MW"Xx/C Ex=emissions of pollutant x q=Volumetric flaw rate/volume of gas processed MW=Molecular weight o`gas=$6 of gas"MW of air Xx=mass fraction of a in gas C=molar volume of ideal gas(379 scf/Ib-mall at 60F and 1 atm Q so scf/hr MW 1251 Ib/Ib-mal Hours or Op. 87.60 naumyr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy C02 22119 44 0.0436 C02 1.541 13496.909 6.748 nitrogen av?-2 28 0.0112 nitrogen 0.396 3472.233 1.736 methane 73 9696 16.04 0.5318 methane 18.783 164540.867 82.270 ethane 11 hose 30.07 0.1592 ethane 5.621 49242.144 24.621 propane 7-14F 44.09 0.1446 propane 5.105 44724.026 22.362 isobutane 0 cuts 58.12 0.0174 isobutane 0.615 5388.999 2.694 n-butane zcros 58.12 0.0522 n-butane 1.844 16150.878 8.075 isopentane 5:152 72.15 0.0105 isopentane 0.371 3253.891 1.627 n-pentane mos 72.15 0.0130 n-pentane 0.460 4032.344 2.016 cyclopentane n, ., 70.15 0.0010 cyclopentane 0.036 315.202 0.158 n-hexane 5,753 86.18 0.0031 n-hexane 0.1082 947.754 0.474 cyclohexane ,,,,„7 84.18 0.0007 cyclahexane 0.026 229.981 0.115 Other hexanes 1.960 86.18 0.0053 Other hexane 0.187 1634.966 0.817 heptanes JIB 100.21 0.0027 heptanes 0.095 833.832 0.417 methylcyclohexa u1ca 98.19 0.0006 methylcydohe 0.022 196.086 0098 224-TMP 3 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 8(18., 78.11 0.0005 Benzene 0.0109 165.735 0.083 Toluene oms. 92.14 0.0003 Toluene 0.0123 107.336 0.054 Ethylbenzene 1:018 106.17 0.0000 Ethylbenzene 0.0013 11.779 0.006 Xylenes 1:.021 106.17 0.0001 Xylenes 0.0035 30.920 0.015 C8+Heavies 2.117 114.23 0.0016 08+Heavies 0057 502.176 0.251 Mass Fraction VOL, 0.2538 Total VOC 39.263 Heating Value I 1262 BTU/scf Oomousuon emuss p on factor sou . AP-42:Chapter 13.5 007 I lb NOX/MMBtu 0.27 lb CO/MMBIu 14WE0461.CP2 123/9COA One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1 F,Senal number 2091628).The pneumatic pump is controlled by 007 four enclosed flares.Each flare has a minimum control efficiency of 95%. Notes Mole%concentrations are based on weighted average of sales gas samples collected 7/212014 for Stale Seventy Holes A-E-3HNB&F-J-3HNB,7/2/2i Emissions are based on 8760 hours of operation per year. Assume MW of C8-e is 114.23 Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 14940 lb/MMscf 747.01 lb/MMscf 39.3 tpy 2.0 tpy Gas Analysis Nox 0.071b/MMBTU 0.07 lb/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 lb/MMBTU 1.2 tpy 1.2 tpy AP-42 Benzene 31.533 lb/MMscf 1.5766 lb/MMscf 1661b/yr 8 lb/yr Gas Analysis n-Hexane 180.32 lb/MMscf 9.0159 lb/MMscf 948 lb/yr 47 lb/yr Gas Analysis - Toluene 20.422 lb/MMscf 1.0211 lb/MMscf 107 lb/yr 51b/yr Gas Analysis Xylenes 5.8828 lb/MMscf 0.2941 lb/MMscf 31 lb/yr 21b/yr Gas Analysis Ethylbenzene 2.2411 lb/MMscf 0.1121 lb/MMscf 121b/yr 11b/yr Gas Analysis 14WE0461.CP2 123/9COA Six low-pressure separators controlled by four enclosed flares during VRU downtime.Each flare has a 009 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 tow-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=C'MW'Xx/C Ex=emissions of pollutant x Cl=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 Throughput(0) 13.4 MMscf/yr 1535.004 scf/hr MW 33.3 Ibiib-mot 0.036840096 MMscf/d mole% MW Ibx/Ibmol mass fraction Ib/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 000 0.00 CO2 2.78 44.01 1.215 0.036 4.92 43095.79 21.55 N2 0.13 28.013 0.036 0.001 0.15 1292.04 0.65 methane 36.93 16.041 5.923 0.178 23.99 21016?05 105.08 ethane 23.23 30.063 6.985 0.210 28.29 247812.51 123.91 propane 22.97 44.092 10.127 0.304 41.02 359293.88 179.65 isobutane 242 58.118 1.405 0.042 5.69 49836.07 24.92 n-butane 7.50 58.118 4.357 0.131 17.65 154597.17 77.30 isopentane 121 72.114 0.871 0.026 3.53 30886.82 15.44 n-pentane 147 72.114 1.059 0.032 4.29 37559.52 18.78 cycle pentane 010 70.13 0.069 0.002 0.28 2458.30 1.23 n-Hexane 0.27 86.18 0.234 00070 0.95 8286.10 4.14 cyclohexane 0.07 84.16 0.059 0.002 0.24 2081.20 1.04 Other hexanes 0.49 86.18 0.424 0.013 1.72 15058.69 7.53 heptanes 021 10021 0.208 0.006 0.84 7384.51 369 methylcyclohexane 0.05 98.19 0.050 0.001 0.20 1762.76 0.88 224-TMP 0.00 114.23 0.000 0.000 0.00 8.11 0.00 Benzene 0.05 78.12 0.041 0.0012 0.17 1460.65 0.73 Toluene 0.03 92.15 0.025 0.0007 0.10 876.20 0.44 Ethylbenzene 0.00 106.17 0.002 0.0001 0.01 82.87 0.04 Xylenes 0.31 106.17 0.005 0.0002 0.02 192.11 0.10 C8t Heavies 0.09 116 0.109 0.003 0.44 3868.66 1.93 VOC mass frac 0.572 Total VOC{Uncontrolled)- 337.85 Notes Mole%concentrations based on LP separator gas sample collected 7/2/2014 from State Seventy Holes F I I-J14-3HNC Emissions are based on 5760 hours of operation per year. MW of C8=assumed to be 116 Flowrate is based on Promax results,assuming 30%VRU downtime and applying a 20%safety factor. 14WE0461.CP2 123/9COA Six low-pressure separators controlled by four enclosed flares during VRU downtime.Each flare has a 009 minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Abutec Model 46" Serial Number 10661,10660.10484,100843 Gas Heating Value 1879 Blu/scf Throughput 25266.22724 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress low-pressure separator gas to sales line.The VRU is considered pail of the process and not included as an air pollution control devio Make Model Requested Control Efficiency Manual Bypass Time Backup Flare Overall Control I 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 Ilb NOX/MMBtu 0.37 Ilb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOL 50250 lb/MMscf 2512.5 lb/MMscf 33.78 spy 16.9 tpy Gas Analysis Non 0.07 lb/MMBTU 0.07 lb/MMBTU 0.9 tpy 0.9 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 4.7 tpy 4.7 spy AP-42 Benzene 108.63 lb/MMscf 5.4313 lb/MMscf 1461 lb/yr 73 lb/yr Gas Analysis n-Hexane 616.22 lb/MMscf 30.811 lb/MMscf 8286 lb/yr 414 lb/yr Gas Analysis Toluene 65.161 lb/MMscf 3.2581 lb/MMscf 876 lb/yr 44 lb/yr Gas Araiysis Xylenes 14.287 lb/MMscf 0.7143 lb/MMscf 192 lb/yr 10 lb/yr Gas Analysis Ethylbenzene 6.1629 lb/MMscf 0.3081 lb/MMsd 83 lb/yr 4 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.' 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 recompleled on or after August 1,2014? No This separator is not subject to Reg 7 Section XVII.G 14WE0461.CP2 123/900A Two vapor recovery towers(VRTs)controlled by four enclosed flares during VRU downtime.Each flare 015 has a minimum control efficiency of 95%. Equipment Description This source vents natural gas from: vapor recovery towers(VRTs)during VRU downtime Emissions from this source are routed to a flare [Natural gas venting from vapor recovery towers(VRTs)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 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-mol)at 60F and 1 atm Throughout 10) 0.8 MMscf/yr 94.35255 sct/hr mw 87.3 lb/lb-Awl 0.002264461 MMscf/d mole MW Ibx/Ibmal mass fraction lb/hr lb/yr tpy Helium 000 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 1 42 44.01 0.626 0.013 0.16 1364.62 0.68 N2 0.81 28.013 0.228 0.005 0.06 49642 0.25 methane 10.16 16.041 1.630 0.034 0.41 355547 1.78 ethane 22.05 30.063 6.628 0.140 1.65 1445474 7.23 propane 3199 44.092 14.107 0.298 3.51 30764.38 15.38 isobutane 361 58.118 2.100 0.044 0.52 4579.00 2.29 n-butane 1233 58.118 7.165 0.151 178 15625.32 7.81 Isopentane 211 72.114 1.521 0.032 0.38 3316.47 1.66 n-pentane 72.114 1.886 0.040 0.47 4113.12 2.06 cyclopentane 1.12 70.13 0.788 0.017 0.20 1718.33 0.86 n-Hexane 2.47 86.18 2.132 0.0451 0.53 4650.04 2.33 cyclohexane 073 84.16 0.613 0.013 0.15 1336.00 0.67 Other hexanes 497 86.18 4.287 0.091 1.07 9350.06 4.68 heptanes 156 100.21 1.561 0.033 0.39 340476 1.70 methylcyclohexane O40 98.19 0475 0.010 0.12 103514 0.52 224-TMP 0.011 114.23 0.093 0.0020 0.02 203.64 0.10 Benzene 0.48 78.12 0.376 0.0079 0.09 82002 0.41 Toluene 0.28 92.15 0.255 0.0054 0.06 556.13 0.28 Ethylbenzene 0.02 106.17 0.017 0.0004 0.00 36.70 0.02 Xylenes 0.06 106.17 0.063 0.0013 0.02 138.08 007 O8+Heavies 0e4 116 0.740 0.016 0.18 1613.41 0.81 VOC mass frac 0.807 Total VOC(Uncontrolled) 41.63 Notes Mole%compositions are based on Promax results for the VRT stream Flowrate is based on Promax results assuming 30%downtime for VRU and applying a 20%safety factor. 14WE0461.CP2 123/900A Two vapor recovery lowers(VRTs)controlled by four enclosed flares during VRU downtime.Each flare 015 has a minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust VRT gas during VRU downtime. Manufacturer Abutec Model 48" Serial Number 10661.10660,10484.100843 Gas Heating Value 2628 Btu/scf Throughput 2172.116472 MMBlu/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 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 Ilb NOX/MMEItu 0.37 Ilb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 100735 lb/MMscf 5036.8 lb/MMscf 41.6 tpy 2.1 tOY Gas Analysis Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.1 spy 0.1 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 0.4 toy 0.4 tpy AP-42 Benzene 992.12 lb/MMscf 49.606 lb/MMscf 820 lb/yr 41 lb/yr Gas Analysis n-Hexane 5626.0 lb/MMscf 281.30 lb/MMscf 4650 lb/yr 233 lb/yr Gas Analysis Toluene 672.85 lb/MMscf 33.64216/MMsd 556 lb/yr 28 lb/yr Gas Analysis Xylenes 167.07 lb/MMscf 8.3533 lb/MMscf 138 lb/yr 7 lb/yr Gas Analysis Ethylbensene 44.401 lb/MMscf 2.2201 lb/MMscf 37 lb/yr 2 lb/yr Gas Analysis 224-TMP 246.38 lb/MMscf 12.319 lb/MMscf 204 lb/yr 10 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 Reaulation 2 Section l.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? No This separator is not subject to Reg 7 Section 20/11.0 14WE0461.CP2 123/9COA AIRS(County/Plant)123/9O0A Permit No.14WE0461 Date 3/5/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions CM. reportable Point 8 SCC Pollutant or GAS Factor EmisisOn Factor Source (tpy0 (tpyp PTEitpy)' Elf% 7 VOC 118803 lb/1000 qa Promax 3.6 4.4 874 95% Yes NOx 0.068 lb/Mmblu AP-42 Table 13.5 0.15 0.2 0.2 0% No CO 0.37 lb/Mmbtu AP-42 Table 13.5 0.8 0.9 0.9 0% No Benzene 0.0503 lb/1000 qa Promax 31 37 741 95% Yes 003 40400311 n-Hexane 0.2896 113/1000 ga Promax 178 213 4262 95% Yes Toluene 0.0365 lb/1000 ga Promos 22 27 537 95% Yes Ethyl benzene 0.0027 lb/1000 qa Promos 2 2 39 95% No Xylenes 0.0106 lb/1000 qa Promax 6 8 156 95% No 2.2.4-TMP 0.0235 lb/1000 a Promax 14 17 345 95% Yes VOC 6238 lb/1000 qa ODPHE 2.6 52.2 95% Yes 004 40400315 Benzene 0.167 lb/1000 qe CDPHE 140 2790 95% Yes n-Hexane 0.524'b/1000 qa CDPHE 438 8769 95% Yes is VOC 3.7225 ib/1000 qa AP-42 9.2 27.4 66.5% Yes Benzene 0.0168 lb/1000 qa AP-42 03 247 66.5% No 005 40600132 n-Hexane 0.1359 lb/1000 qa AP-42 670 1999 66.5% Yes Toluene 0.0094 lb/1000 ga AP-42 46 139 66.5% No Etbylbenzene 0.0007 15/1000 ga AP-423 10 56.5% No Xylenes 0.00291511000 aAP12 11 34 66.5% No VOC 14940 IHMMscl Gas Analysis 2.0 39.3 95% Yes NOx 0.060 lb/MMBTU AP-42 0.2 0.2 0% No 0O 0.37 Ib/MMBTU AP-42 1.2 12 0% Yes 007 31000299 Benzene 315331b/MMscf Gas Analysis 8 166 95% No n-Hexane (80.321b/MMsct Gas Analysis 47 948 95% Yes Toluene 20.422 lb/MMsof Gas Analysis 5 107 95% No Ethyl benzene 2.2411 lb/MMscf Gas Analysis 1 12 95% No Xylenes 5.8820 Ib/MMscf Gas Analysis 2 31 95% No VOC 50250 lb/MMscf Gas Analysis 169 337.8 95% Yes NOx 0068 Ib/MMBTU AP-42 0.9 0.9 0% No CO 0.37 lb/MMETU AP-42 4.7 4.7 0% Yes 009 81000205 Benzene 108.63 lb/MMscf Gas Analysis 73 1461 95% Yes n-Hexane 61622 lb/MMscf Gas Analyse 414 8286 95% Yes Toluene 65.161 Ib/MMscf Gas Analysis 44 876 95% Yes Etbylbenzene 6.1629 Ib/MMscf Gas Analysis 4 03 95% No AIRS(County/Plant)123/9COA Permit No.14WE0461 Oate 3/5/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions Ctrl. reportable Point 4 SCC Pollutant or CAS Factor Emisison Factor Source (tpy( (Ipyp PTE(tpy)* EfP Xylenes 14.287 Ib/MMscf Gas Analysis 10 192 95% No VOC 1007351b/MMscf Gas Analysis 2.1 41.6 95% Yes NOx 0.060 lb/MMBTU AP-42 0.1 0.1 0% No CO 0.370 Ib/MMBTU AP-42 0.4 0.4 0% No Benzene 992.121bIMMsc1 Gas Analysis 41 820 95% Yes 15 31000205 n-Hexane 5626.0 Ib/MMscl Gas Analysis 233 4650 95% Yes Toluene 672.85 lb/MMscf Gas Analysis 28 556 95% Yes Elbylbenzene 44.401 7 lb/MMscf Gas Analysis 2 37 95% No 2,2,4-s I 167.07 lblMMscf Gas Analysis — 7 136 95% No 2,2,4-TMP 246.381b/MMsot Gas Analysis 10 204 95% No 0, Iii _ ,>.a< Is 9 c c c > m e Eo '� r, e YYzzz 0 � ` O u a >, u d I. ca „�, a = z O a u ❑❑® - T'o "o' O m rn Qt ® u c,' w N C 'O- NE i`[ Oy NNNZ - y i! 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E p N U E 5 1p. �( 4*4 ea _S V u n m U H t O > _ E u W E ..V- 0 ._ - O C �N '3 W 7, Q n o Qr rt. o .u.. v o a y ` --i o c 't` a T 0.e .0., y o = 06). A c .. > d .c o m C c .E c a U m 0 75y ° ° u m > r, to ° et -, u O I 7,. O m o e` U 4 Ca UUC.) O 1 E R N _ w T. C.Cw U U U U U ° ) `w W ,- e m C -. > Y V , .E m t� w W w W W W � ,+ m Q I t a I ° u 2 C a I Y .-°3 2 .0';' , P° Q, P° 0 0 c 0 n U, .. > > > C T ., d c m' I 0 O se p .y C O O C N o C Y O E E e0. N c C 4 ^� O �,y o d 8Z q C I N m p > m 4' Q F 0 O - H 0 0 0 0 [Y u _ v 'WLJ Lei, c. c.) L — E o > ,Z Uc uNa � T Y p 3 O W v Y ° a, T o ca w O W Y ❑ ❑ y Q ® a OFs_ iC' C •� O W fn W STATE OF COLORADO • John W.Hickenlooper,Governor apcot Larry Wolk,MD,MSPH o Executive Director and Chief Medical Officer Dedicated to protecting and improving the health and environment of the people of Colorado * .* 4300 Cherry Creek Dr.S. Laboratory Services Division .rgje • Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Weld County-Clerk to the Board 1150 O St PO Box 758 Greeley,CO 80632 July 8, 2014 Dear Sir or Madam: On July 14, 2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—State Seventy Holes P-4, in the The Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30)days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health& Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, RECEIVED 1r / JUL 1 1 2014 WELD COUNTY COMMISSIONERS Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure wbucAei1tsD &C' ITLCmmv►kL(FE) —�_u- 11-14 2014-2108 • STATE OF COLORADO John W.Hickenlooper,Governor — Larry Wolk,MD, MSPH EM.OV•coZoExecutive Director and Chief Medical Officer Dedicated to protecting and improving the health and environment of the people of Colorado4300 Cherry Creek Dr.S. Laboratory Services Division �6 x' Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy Operating Company LLC—State Seventy Holes P-4—Weld County Released To: The Greeley Tribune On: July 8, 2014 Published: July 14, 2014 PUBLIC NOTICE OF A PROPOSED PROJECT OR ACTIVITY WARRANTING PUBLIC COMMENT Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: • Applicant: Bonanza Creek Energy Operating Company LLC Facility: State Seventy Holes P-4 Wellpad NWNE Section 4 T4N R62W Weld County The proposed project or activity is as follows: Bonanza Creek is operating a wellhead facility in Weld County. 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 I11.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 14WE0461 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 www.colorado.gov/cdphe/AirPublicNotices 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: Peter Armington Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South,APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us w{p z: ri STATE OF COLORADO •LO- • •• D PART Y •FP = C HEALTH AND ENVIRONMENT �` AIR POLLUTION CONTROL DIVISION 4 TELEPHONE: (303)692-3150 /816+: CONSTRUCTION PERMIT PERMIT NO: 14WE0461 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 State Seventy Holes PA, located in the NWNE Section 4 T4N R62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID TL 005 Truck Condensate Loadout FUG 006 Fugitive equipment leaks P-1 007 One (1) water transfer pump (Sandpiper G1 F serial number: 2091628) rated at 600 scf/hr. FL-1 008 Emergency venting to a candlestick flare. Sep-1 009 Low pressure separator controlled by a VRU with a backup enclosed flare. Point 007: 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. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded ontine 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. AIRS ID: 123/9C04 Page 1 of 13 olor Depa en li Health and Environment it Pollution Control Division 2. Within one hu d ' 80 ance is permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 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. Point 009: Within one-hundred and eighty (180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from the low pressure separator. The operator shall use the gas flow rate 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. 5. 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.) 6. 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 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 Emisgion Type x TL 005 --- 8.0 --- Point FUG 006 --- 7.9 --- Fugitive P-1 007 --- 2.2 1.3 Point FL-1 008 --- 6.3 3.7 Point Sep-1 009 -- 6.6 1.5 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) AIRS ID: 12319C04 Page 2 of 13 olor. Depa en 'f .Ii Health and Environment � it Pollution Control Division from each em' ,k. .. it - r. ' el , *nth t• }. 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 006: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 9. 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 P-1 007 Enclosed Flare VOC FL-1 008 Open Flare VOC Sep-1 009 Enclosed Flare VOC 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 Equipment Point Process Parameter Annual Limit ID TL 005 Oil Loaded 61,320 BBL P-1 007 Natural Gas 5.3 MMSCF FL-1 008 Gas Vented from Separator 15.2 MMSCF Sep-1 009 Gas Vented from Separator 7.8 MMSCF Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 11. Point 009: Upon installation of the flow meter required under Condition 4, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from each low pressure separator using a flow meter. The flow meter shall AIRS ID: 123/9C04 Page 3 of 13 olor Depa en li Health and Environment it Pollution Control Division continuously fl to ec volu ' flow vented from each separator. The owner or operator shall use monthly throughput records to demonstrate compliance with the limits specified in Condition Error! Reference source not found. and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. 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) 13. 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.) 14. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) I 15. Point 005: 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) 16. Point 005: 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 16 (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. 17. Point 005: 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. 18. Point 006: 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. 19. Point 006: 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 AIRS ID: 123/9C04 Page 4 of 13 olor Depa en 'Ii Health and Environment it Pollution Control Division apply Reason- ala o ch CT) _' e 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: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a quarterly basis. The first AVO screening shall occur within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. Hi. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 20. Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING AIRS ID: 123/9C04 Page 5 of 13 olor Depa en li ealth and Environment it Pollution Control Division Initial Testin 21. Point 006: Within one hundred and eighty days (180) after issuance of this permit, the owner or operator shall complete the initial extended gas analysis of gas samples that are representative of volatile organic compound (VOC) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 22. Point 006: 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. 23. Point 008: The owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.1 &4) Periodic Testing Requirements 24. Point 006: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 25. Point 007: 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. 26. Point 007: 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. 27. Point 007: 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 28. 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 AIRS ID: 123/9C04 Page 6 of 13 ll olor r l Depa en P .li I A "Health and Environment s it Pollution Control Division For v. - .a . =s (. •r -. nitr lZ7 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. 29. 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). 30. MACT Subpart HH - National Emission Standards for Hazardous Air Pollutants From Oil and Natural Gas Production Facilities major stationary source requirements shall apply to this stationary source at any such time that this stationary source becomes major solely by virtue of a relaxation in any permit limitation and shall be subject to all appropriate applicable requirements of Subpart HH. (Reference: Regulation No. 8, Part E) GENERAL TERMS AND CONDITIONS 31. 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. 32. 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 AIRS ID: 12319C04 Page 7 of 13 Depa en li HealthPollution and Environment it Control Division obtaining finDolor at ted ' Requirements to Self- Certify for Final Authorization section of this permit. 33. 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. 34. 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. 35. 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. 36. 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. 37. 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: Peter Armington Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 12319C04 Page 8 of 13 m } t olorl Depa en di Health and Environment i it Pollution Control Division � n Notes to Permit Holder .. ime 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 s 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.qov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&paciename=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# (lb/yr) reportable? (Ib/yr) 005 Benzene 71432 193.3 No 193.3 005 n-Hexane 110543 988.8 Yes 988.8 005 Toluene 108883 431.9 Yes 431.9 005 Xylenes 1330207 349 Yes 349 006 Benzene 71432 79.7 No 79.7 006 n-Hexane 110543 396.6 Yes 396.6 006 Toluene 108883 139.7 No 139.7 006 Ethylbenzene 100414 27.8 No 27.8 006 Xylenes 1330207 106.8 No 106.8 007 Benzene 71432 213.4 No 10.7 007 n-Hexane 110543 1231 Yes 61.6 007 Toluene 108883 155.9 No 7.8 007 Ethylbenzene 100414 17.7. No 0.9 007 Xylenes 1330207 48.6 No 2.4 008 Benzene 71432 617.2 Yes 30.9 008 n-Hexane 110543 3560 Yes 178 AIRS ID: 123/9C04 Page 9 of 13 olor Depa en li Health and Environment it Pollution Control Division 008 Tol 8 22.5 008 Ethylbenzene 100414 51.1 No 2.6 008 Xylenes 1330207 140.5 No 7 009 Benzene 71432 29.8 No 0.7 009 n-Hexane 110543 177.9 No 4.4 009 Toluene 108883 13.6 No 0.3 009 Ethylbenzene 100414 1.1 No 0 009 Xylenes 1330207 3.1 No 0.1 5) The emission levels contained in this permit are based on the following emission factors: Point 005: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.2623 AP-42 Benzene 0.0032 AP-42 n-Hexane 0.0161 AP-42 Toluene 0.0071 AP-42 Xylenes 0.0057 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= 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) =6.5 psia M (vapor molecular weight) =67.65 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 liquids the VOC emission factor. Point 006: Component Gas Heavy Oil Light Oil Water/Oil Connectors 946 0 338 329 Flanges 49 0 8 10 Open-ended Lines 27 0 3 1 Pump Seals 4 0 0 1 Valves 129 0 45 32 Other 66 0 7 10 VOC Content(wt. 0.2734 0.3 0.997 1 fraction) Benzene Content(wt. 0.0007 0.001 0.012 0.0012 fraction) Toluene Content(wt. 0.0005 0.001 0.0268 0.0003 AIRS ID: 123/9C04 Page 10 of 13 a olor Depa 1 en P iii Health and Environment •it Pollution Control Division r fraction) ` Ethylbenzene (wt. 0.0001 0.001 0.0053 0.0001 fraction) Xylenes Content(wt. 0.0002 0.02 0.0217 0.0001 fraction) n-hexane Content(wt. 0.0039 0.001 0.0615 0.0001 fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors (kg/hr-component): Water/Oil Component Gas Service Heavy Oil Light Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R-95-017 Table 2-4 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 007: Emission Emission Factors - Factors - Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (Ib/MMBTU) VOC 16431.7021 821.5851 Gas Analysis Benzene 40.6007 2.03 Gas Analysis n-Hexane 234.2095 11.7105 Gas Analysis Toluene 29.6599 1.483 Gas Analysis Xylenes 9.2444 0.4622 Gas Analysis Point 008: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx Ub/MMBTU) --- 0.068 0.068 AP-42 CO (Ib/ (Ib/MMBTU) --- 0.37 0.37 AP-42 AIRS ID: 123/9C04 Page 11 of 13 olor Depa en li Health and Environment it Pollution Control Division t 'on Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled Ib/MMscf lb/MMscf VOC 27.4 16483.1262 824.1563 Gas Analysis Benzene 0.07 40.6059 2.0303 Gas Analysis Toluene 0.05 29.6631 1.4832 Gas Analysis Ethylbenzene 0.006 3.3616 0.1681 Gas Analysis Xylenes 0.015 9.2444 0.4622 Gas Analysis n-hexane 0.39 234.2095 11.7105 Gas Analysis Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx 0.068 0.068 AP-42 (Ib/MMBTU) CO 0.37 0.37 AP-42 (Ib/MMBTU) VOC 69.6 67438.7275 1685.9682 Gas Analysis Benzene 0.16 152.7359 3.8184 Gas Analysis Toluene 0.07 69.538 1.7385 Gas Analysis Ethylbenzene 0.01 5.8828 0.1471 Gas Analysis Xylenes 0.02 15.9675 0.3992 Gas Analysis n-hexane 0.94 912.2801 22.807 Gas Analysis Note: The uncontrolled VOC and HAP emissions for this point were calculated using a Promax model to estimate the VOC and HAP content of the stream vented from the low-pressure separator. The controlled VOC and HAP emissions factors for point 009 are based on the flare control efficiency of 97.5%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 2,092 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: VOC NANSR Synthetic Minor Source of: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.gpoaccess.qov/ AIRS ID: 123/9C04 Page 12 of 13 a; olor J Depa en Pr'tali Health and Environment 'it Pollution Control Division Part 60: Standar." "• - -rfor '1 'e : ' r S t • `'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 777Z—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado qov/cdp he/oilgasperm its AIRS ID: 123/9C04 Page 13 of 13 Division Information Engineer: Peter Arrnington Control Engineer: Stefanie Rucker Review Date: 05/08/2014 Application Date: 02/21/2014 • Facility Identifiers Permit No. 14WE0461 AIRS County# 123 Weld Facility# 9C04 Facility Type: exploration and production facility ❑� Located in the 8-hour non-attainment area? O True Minor Q Synthetic Minor for: VOC r NOx CCO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Seventy Holes P-4 Source Location: NWNE Section 4 T4N R62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address Address 2: 410 17th Street, Suite 1500 /,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 1 Source Description: Oil and gas exploration and production facility known as the State Seventy Holes P-4, located in the NWNE Section 4 T4N R62W, Weld County, Colorado. Point Name Type Control 005 TL Loadout None 006 FUG Fugitives None 007 P-1 Pump Flare 008 FL-1 Separator Venting Flare 009 Sep-1 Separator Venting Flare 005 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 5 Saturation Factor 0.6 AP-42 P True Vapor Pressure 6.47 psia Sales Oil Analysis M Molecular Weight of Vac 67.65 lb/lb-mole AP-42 T Liquid Temperature 524 deg. R Field Data L 6.24 lb/10^3 gal 2.62E-01 lb/bbl Annual requested Throughput 61320 BBL/yr 2575440 gal/yr Annual requested VOC emissions 16083 lb/yr 8.04 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0120 n-hexane 0.0615 Toluene 0.0269 Xylenes 0.0217 Source: Pressurized oil analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2623 lb/bbl 8.04 tpy 8.04 tpy AP-42 Benzene 0.0032 lb/bbl 193.30 lb/yr 193.30 lb/yr AP-42 n-Hexane 0.0161 lb/bbl 988.80 lb/yr 988.80 lb/yr AP-42 Toluene 0.0070 lb/bbl 431.89 lb/yr 431.89 lb/yr AP-42 Xylenes 0.0057 lb/bbl 349.03 lb/yr 349.03 lb/yr AP-42 006 Fugitive equipment leaks Regulation 7 Information Construction Dale: 11/25/13 Processing Date: 5/8/14 For Wellhead Facilities Enter VOC emissions from highest emitting storage lank: 2 tpy (If no storage tanks are present,enter facility-wide VOC emissions) Operating Hours: 0760 hours/year Emission Factor Source Reg.9 Applicability EPA-453/R-95-017 Table 2-8 Reg.3 Emissions Reporing. EPA-453/R-95-017 Table 2-4 Control EHiienny Source: None Calculations Emission Factor lkg/hr- Service Component Type Count source) CmNol(%)Pollutant Mass Fraction Emissions ppyl Table 2-4 Table 25 Reg.3 I Reg.7 Connectors 946 2.40E-04 100E05 00% VOC 02734 3.8754553 0059775 Flanges 49 3.90E-04 5.70E-06 0.0% Benzene 0.0007 0.0099225 Open-Ended Lines 27 2.00E-03 1.50F05 0.0% Toluene 0 0005 0.0070875 Gas Pump Seals 4 240E-03 3.50E-04 00% Ethylbenzene 00001 0.0014175 Valves 129 4.50E-03 2.50E-05 00% XNenes O0002 0.002835 Other E6 8.80E-03 1.20E-04 0 it-Hexane 00039 0.0552826 Connectors 0 7.50E-06 750E-06 00% VOC 0.3 0 0 Flanges 0 3.90E-07 390E-07 00% Benzene 0001 0 Open-Ended Lines 0 1.40E-04 720E-06 00% Toluene 0.001 0 Heavy 011 Pump Seals 0 0.00E+00 0.00E+00 0 Ethylbenzene 0.001 0 Valves 0 840E-06 840E06 0 Xylenes 002 0 Other 0 3.20E05 3.20E05 0.0% n-Hexane 0.001 0 Connectors 338 2.10E04 7.50E-06 0.0% VOC 0997 2.3158856 2315886 Flanges 0 110E-04 240E-06 00% Benzene 0012 0.0278742 Open-Ended Lines 3 140E-03 140E-05 0.0% Toluene 00268 0.0622525 Light Oil Pump Seals 0 1.30E-02 5.10E-04 0.0% Ethylbenzene 00053 0.0123111 Valves 45 2.50E-03 1.90E-05 00% Xylenes 0.0217 0.0504059 Other 7 7.50E-03 1.10E-04 0.0% n-Hexane 00615 0.1428555 Connectors 329 1.10E-041.00E-0500% VOC I 1.730905 1730905 Flanges 10 290E-06 290E-06 00% Benzene 0.0012 0.0020771 Open-Ended Lines 1 2.50E-04 3.50E-06 0.0% Toluene 00.000300005193 Wdlefl011 Pump Seals 1 2.40E-05 2.40E-05 00% Ethylbenzene 0.0001 0.0001731 Valves 32 950E05 9.70E-06 0.0% Xylenes 0.0001 0.0001731 Other 10 1.40E-02 5.90E05 0.0% n-Hexane 0.0001 0.0001731 'Total Fugitive VOC Emissions for Regulation 7 Requirements: I 4.1 tpy Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source VOC 792 tpy 7.92 tpy EPA-453/R-95-017 Table 2-4 Benzene 7975 lb/yr 7975 lb/yr EPA-453/R-95-017 Table 2-4 Toluene 13972 lb/yr 139.72 lb/yr EPA-453/R-95-017 Table 2.4 Ethylbenzene 27.80 lb/yr 27.80 lbM EPA-453/R-E5-017 Table 2.4 Xylenes 10683 lb1yr 106.83 lb/yr EPA-4a3/R-95-017 Table 2.4 n-Hexane 39162 lb/yr 396.62 lb/yr EPA453/R-95-017 Table 2-4 Regulatory Applicability Reg.3 Operator has agreed on the Division's standard conditions for RACT. • One(1)water transfer pump(Sandpiper G1F serial number:2091628)rated 007 at 600 scf/hr. Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number:2091628 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=Q*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/Ib-mol)at 60F and 1 atm Q 600 scf/hr MW 22.8 lb/lb-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW massfraction Component ; lb/hr lb/yr tpy CO2 2.21 44 0.0426 CO2 1.539 13485.315 6.743 nitrogen 0.85 28 0.0104 nitrogen _ 0.377 3300.602 1.650 methane 72.26232 16.04 0.5084 methane 18.350 160743.126 80.372 ethane 12.5411 30.07 0.1654 ethane 5.970 52298.015 26.149 propane 7.8074 44.09 0.1510 propane 5.450 47737.830 23.869 isobutane 0.7214 58.12 0.0184 isobutane 0.664 5814.574 2.907 n-butane 2.196 58.12 0.0560 n-butane 2.021 17700.033 8.850 isopentane 0.3803 72.15 0.0120 isopentane 0.434 3805.212 1.903 n-pentane 0.4783 72.15 0.0151 n-pentane 0.546 4785.781 2.393 cyclopentane 0.0384 70.15 0.0012 cyclopentane 0.043 373.573 0.187 n-hexane 0.103 86.18 0.0039 n-hexane 0.141 1231.005 0.616 cyclohexane 0.027 84.18 0.0010 cyclohexane 0.036 315.202 0.158 Other hexanes 0.1782 86.18 0.0067 Other hexane! 0.240 2105.855 1.053 heptanes 0.0864 100.21 0.0038 heptanes 0.137 1200.718 0.600 methylcyclohexa 0.0209 98.19 0.0009 methylcyclohe 0.032 284.597 0.142 224-TMP o 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 0.0197 78.11 0.0007 Benzene 0.024 213.397 0.107 Toluene 0.0122 92.14 0.0005 Toluene 0.018 155.892 0.078 Ethylbenzene 0.0012 106.17 0.0001 Ethylbenzene 0.002 17.668 0.009 Xylenes 0.0033 106.17 0.0002 Xylenes 0.006 48.588 0.024 C8+Heavies 0.0445 93.189555 0.0018 C8+Heavies 0.066 575.100 0.288 Mass Fraction VOC: 0.2731 Total VOC 43.183 Heating Value I 1318 BTU/scf Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu Notes Mole%,MW,and mass fractions from'. Seventy holes P-T-4HNB gas analysis.dated 12/26/2013 Emissions Sumlfiary Table Pollutant Uncontrolled Emission Fac Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Sol VOC 16431.70 lb/MMscf 821.59 lb/MMscf 43.18 tpy 2.16 tpy Ga Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.24 tpy 0.24 tpy AP CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 1.28 tpy 1.28 tpy AP Benzene 40.60 lb/MMscf 2.03 lb/MMscf 213.40 lb/yr 10.67 lb/yr Ga n-Hexane 234.21 lb/MMscf 11.71 lb/MMscf 1231.01 lb/yr 61.55 lb/yr Ga Toluene 29.66 lb/MMscf 1.48 lb/MMscf 155.89 lb/yr 7.79 lb/yr Ga Xylenes 9.24 lb/MMscf 0.46 lb/MMscf 48.59 lb/yr 2.43 lb/yr Ga Ethylbenzene 3.36 lb/MMscf 0.17 lb/MMscf 17.67 lb/yr 0.88 lb/yr Ga 008 Emergency venting to a candle stick flare. 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=O'MW•Xx/C Ex=emissions of pollutant x Q=Volumetric flow ratelvolume 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-moo at 60F and 1 atm Throughput(0) 15.2 MMad/yr 1735.159817 scf/hr MW 22.8 IbAb-mol 0.041643838 MMscf/d mole% MW IbxAbmol mass fraction Ibmr Ibyr tpy Helium 0 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.21 44.01 0.973 0.043 4.45 39007.49 19.50 N2 0.85 28.013 0.238 0.010 1.09 9549.55 4.77 methane 72.26232 16.041 11.592 0.508 53.07 484887.34 232.44 ethane 12.5411 30.063 3.770 0.165 17.26 151207.15 75.60 propane 7.8074 44.092 3.442 0.151 15.76 138060.87 69.03 isobutane 0.7214 58.118 0.419 0.018 1.92 16814.78 8.41 n-butane 2.196 58.118 1.276 0.056 5.84 51185.55 25.59 isopenlane 0.3803 72.114 0.274 0.012 1.26 10998.93 5.50 n-pentane 0.4783 72.114 0.345 0.01513 1.58 13833.25 6.92 cyclapentane 0.0384 70.13 0.027 0.00118 0.12 1080.04 0.54 n-Hexane 0.103 86.18 0.089 0.00389 0.41 3559.98 1.78 cyclohexane 0.027 84.16 0.023 0.00100 0.10 911.33 0.46 Other hexanes 0.1762 86.18 0.152 0.00688 0.70 6069.99 3.04 heplanes 0.0864 100.21 0.087 0.00380 0.40 3472.40 1.74 methylcyclohexane 0.0209 98.19 0.021 0.00090 0.09 823.03 0.41 224-TMP 0 114.23 0.000 0.00000 0.00 0.00 0.00 Benzene 0.0197 78.12 0.015 0.00067 0.07 617.21 0.31 Toluene 0.0122 92.15 0.011 0.00049 0.05 450.88 0.23 Ethylbentene 0.0012 106.17 0.001 0.00006 0.01 51.10 0.03 Xylenes 0.0033 106.17 0.004 0.00015 0.02 140.51 0.07 C8+Heavies 0.0445 137.4837288 0.061 0.00288 0.28 2453.67 1.23 VOC mass frail 0.274 Total VOC(Uncontrolled) 125.27 Notes Mole%,MW,and mass fractions from State Seventy Holes P-T-4HNB gas analysis. 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 Tornado Model 40' Flare Stack Serial Number 12345678 Gas Heating Value 1318 Btu/scf Throughput 20033.6 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make Model Requested Control 100.00% Annual Bypass Tim 50.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42: Chapter 13.5 0.07 IIb NOX/MMBtu 0.37 jIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Contrailei V0C 16483.13 lb/MMscf 824.16 lb/MMscf 125.27 tpy Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.68 tpy CO 0.37 Ib/MMBTU 0.37 lb/MMBTU 3.71 tpy Benzene 40.61 lb/MMscf 2.03 lb/MMscf 617.21 lb/yr n-Hexane 234.21 lb/MMscf 11.71 lb/MMscf 3559.98 lb/yr 1 Toluene 29.66 lb/MMscf 1.48 lb/MMscf 450.88 lb/yr Xylenes 9.24 lb/MMscf 0.46 lb/MMscf 140.51 lb/yr Ethylbenzene 3.36 lb/MMscf 0.17 lb/MMscf 51.10 lb/yr 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 c 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 lir For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous has been diluted with seven (7) or more volumes of odor free air." Low pressure separator controlled by a VRU with a backup enclosed flare. Flare has a minimum 009 combustion efficiency of 95%. Equipment Description This source vents natural gas from: low pressure separator Emissions from this source are: recompressed Natural gas venting from low pressure separator. Emissions from this source are recompressed. 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 Xx= mass fraction of x in gas C= molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(Q) 7.8 MMscf/yr 890.4109589 scf/hr MW 36.7 Ib/Ib-mol 0.021369863 MMscf/d mole% MW Ibx/bmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 CO2 2.07 44.01 0.911 0.025 2.14 18748.96 N2 0.27 28.013 0.076. 0.002 0.18 1556.61 methane 22.79 16.041 3.656 0.100 8.59 75244.21 ethane 25.74 30.063 7.739 0.211 18.18 159272.25 propane 29.28 44.092 12.908 0.352 30.33 265654.11 1 isobutane 3.28 58.118 1.904 0.052 4.47 39192.48 n-butane 10.39 58.118 6.040 0.165 14.19 124304.28 isopentane 1.87 72.114 1.348 0.037 3.17 27735.62 n-pentane - 2.31 72.114 1.666 0.045 3.91 34280.67 cyclopentane 0.18 70.13 0.125 0.0034 0.29 2574.86 n-Hexane 0.40 86.18 0.346 0.0094 0.81 7115.78 cyclohexane 0.10 84.16 0.081 0.0022 0.19 1669.70 Other hexanes 0.72 86.18 0.625 0.0170 1.47 12853.46 heptanes 0.24 100.21 0.239 0.0065 0.56 4920.81 methylcyclohexane 0.06 98.19 0.056 0.0015 0.13 1149.83 224-TMP 0.00 114.23 0.000 0.0000 0.00 9.40 Benzene 0.07 78.12 0.058 0.0016 0.14 1191.34 Toluene 0.03 92.15 0.026 0.0007 0.06 542.40 Ethylbenzene 0.00 106.17 0.002 0.0001 0.01 45.89 Xylenes 0.01 106.17 0.006 0.0002 0.01 124.55 C8+Heavies 0.09 137.4837288 0.129 0.0035 0.30 2656.88 VOC mass fracl 0.696 Total VOC(Uncontrolled) 2 Notes Mole%, MW, and mass fractions from Seventy Holes 44-41-5HNB L.P. Separator gas analysis. Emissions are based on 8760 hours of operation per year. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0010 48" Serial Number 21459, 19111 Gas Heating Value 2092 Btu/scf Throughput 8158.8 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ230 Requested Control 100.00% Annual Bypass Tim 50.00% Backup Flare Overall Control 97.50% Combustion emission factor source: AP-42: Chapter 13.5 0.07 Ilb NOX/MMBtu 0.37 lib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controller V0C 67438.73 lb/MMscf 1685.97 Ib/MMscf 6.58 tpy Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.28 tpy CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.51 tpy Benzene 152.74 lb/MMscf 3.82 lb/MMscf 29.78 lb/yr n-Hexane 912.28 lb/MMscf 22.81 lb/MMscf 177.89 lb/yr Toluene 69.54 lb/MMscf 1.74 lb/MMscf 13.56 lb/yr Xylenes 15.97 lb/MMscf 0.40 lb/MMscf 3.11 lb/yr Ethylbenzene 5.88 lb/MMscf 0.15 lb/MMscf 1.15 lb/yr 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 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.' 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