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Home My WebLink About20153630.tiff A ctE 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 1150O St PO Box 758 RECEIVED Greeley, CO 80632 NOV 1 6 2015 November 3, 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On November 4, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company, LLC - Crow Valley 7-62-24 2H. 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 Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, r' Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 1,09.1AZZLuce,c(HH 2015-3630 66: I�L; 1�w;f-�L- HAP It-/8 -/S/ 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickenlooper, Governor I Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer k /s/6* s )* r©PHE Air Pollution Control Division co Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - Crow Valley 7-62-24 2H - Weld County Notice Period Begins: November 4, 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: Crow Valley 7-62-24 2H Oil Et Gas Production Facility NENW Sec 24, T7N, R62W Weld County The proposed project or activity is as follows: Applicant will operate and oil and gas production facility including flaring of produced natural gas while emissions are unable to be routed to sales gas pipeline, storage of produced water in 500 bbl tank, storage of condensate in 3 - 500 bbl tanks, and loadout of condensate to tank trucks. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 15WE0998 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: Bradley Eades Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1I STATE OF COLORADO COLOR DO DE ARTmEN r oF PuBLIC HEALTH AND ENVIRONMENT wo o;�, AIR POLLUTION CONTROL DIVISION ( ;O, TELEPHONE: (303) 692-3150 * \t,18767% CONSTRUCTION PERMIT PERMIT NO: 15WE0998 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the Crow Valley 7-62-24 2H Production Facility , located in the NENW Sec. 24, T7N, R62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Three (3) 500 bbl above ground atmospheric fixed roof condensate CNDTK-1 002 storage vessels controlled by enclosed flare. The flare has a minimum control efficiency of 95%. One (1) 500 bbl above ground atmospheric fixed roof produced PW-1 003 water storage tank controlled by an enclosed flare. The flare has a minimum control efficiency of 95%. TLO 004 Hydrocarbon Loadout to Tanker Trucks. Emissions from the loadout are not controlled. One (1) low-pressure gas/liquid separator controlled by an SEP-1 005 enclosed flare when emissions are unable to be routed to sales pipeline. Flare has a minimum control efficiency of 95%. One backup/emergency open flare used to control emissions of FL-2 007 natural gas at this site during emergency/upset conditions. Flare has a minimum control efficiency of 95%. 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 commencement of operation or issuance of this permit, whichever comes later, by submitting a Notice of Startup form to the Division. The AIRS ID: 123/9D57 Page 1 of 15 olor. Depa en . .Ii 'Health and Environment A •it Pollution Control Division Notice of u. . • loaded online at = f 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 commencement of operation or issuance of this permit, whichever comes later, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 4. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 5. Point 007: The following information shall be provided to the Division within fifteen (15) days after issuance of permit. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 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 Emission Type x CNDTK-1 002 --- 1.2 --- Point PW-1 003 --- 1.0 --- Point AIRS ID: 123/9D57 Page 2 of 15 nor— olor ai 'Depa ene( ofP IicHealth and Environment Nir Pollution Control Division BFI a✓`" Y % e TLO ...u004 `..ev -- Point SEP-1 005 --- 9.0 2.0 Point FL-2 007 --- 4.6 2.1 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-1 002 Enclosed Flare VOC, HAP PW-1 003 Enclosed Flare VOC,HAP SEP-1 005 Enclosed Flare VOC,HAP FL-2 007 Open Flare VOC, HAP 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-1 002 Condensate Throughput 35,040 BBL/yr PW-1 003 Produced Water Throughput 148,920 BBL/yr TLO 004 Condensate Loaded 35,040 BBL/yr AIRS ID: 123/9D57 Page 3 of 15 olor. Depa en . ' •li Health T and Environment •it Pollution Control Division SEP-1 'I. G.:: . n L• - Sep- 6.6 MMSCF/yr FL-2 007 Gas flared from Separator 10.0 MMSCF/yr 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. Point 005 and 007: The operator shall continuously monitor and record the volumetric flow rate, using flow meters, of natural gas vented from the high-pressure and low- pressure separators. The flow meters shall continuously measure flow rate and record total volumetric flow vented to each flare. The owner or operator shall use monthly throughput records and calculation methods detailed in the O&M Plan to demonstrate compliance with the process limits 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 XVII.B.2.b shall have no visible emissions. (Reference: Regulation No. 1, Section I I.A.1. &4.) 13. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 14. Point 002: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 15. Point 002 and 003: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. XVII.C.1.b.(i)(a) Control requirements of Section XVII.C.1.b. must be achieved within ninety (90) days of the date that the storage tank commences operation. XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section XVII.C.1.b.(i), whichever comes later, owners or operators of storage tanks subject to Section XVII.C.1. must conduct audio, visual, olfactory ("AVO") and AIRS ID: 123/9D57 Page 4 of 15 rmni olor Depar tvnenf P li Health and Environment it Pollution Control Division additio is'ua inspect' the,•c•--.A r- tank ny 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: 123/9D57 Page 5 of 15 olor. ak Depa en . • .•Ii Health and Environment A • it Pollution Control Division contai _. s e •s. -.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)(a) A storage tank constructed on or after May 1, 2014, must comply with the requirements of Section XVII.C.2.a. by the date the storage tank commences operation. The storage tank must comply with Section XVII.C.2.b. and implement the approved instrument monitoring method inspections within ninety (90) days of the date that the storage tank commences operation. XVII.C.2.b.(ii)(d) Following the first approved instrument monitoring method inspection, owners or operators must continue conducting approved instrument monitoring method inspections in accordance with the Inspection Frequency in Table 1. Table 1 — Storage Tank Inspections Threshold: Storage Tank Approved Instrument Phase-In Schedule Uncontrolled Actual VOC Monitoring Method Emissions (tpy) Inspection 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 AIRS ID: 123/9D57 Page 6 of 15 olor :Depa en P lid-Health and Environment it Pollution Control Division update a td e . `" fib an zathem a. liable to the Division upon request. In addition, for a period of two (2) years, the owner or operator must maintain records of any required monitoring and make them available to the Division upon request, including: XVII.C.3.a. The AIRS ID for the storage tank. XVII.C.3.b. The date and duration of any period where the thief hatch, pressure relief device, or other access point are found to be venting hydrocarbon emissions, except for venting that is reasonably required for maintenance, gauging, or safety of personnel and equipment. XVII.C.3.c. The date and duration of any period where the air pollution control equipment is not operating. XVII.C.3.d. Where a combustion device is being used, the date and result of any EPA Method 22 test or investigation pursuant to Section XVII.C.1.d.(v). XVII.C.3.e. The timing of and efforts made to eliminate venting, restore operation of air pollution control equipment, and mitigate visible emissions. 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. 16. Point 002, 003, and 005: The flare(s) covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: XVII.B.2.b If a combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, 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. XVII.B.2.d Auto-igniters: All combustion devices used to control emissions of hydrocarbons must be equipped with and operate an auto-igniter as follows: XVII.B.2.d.(i) All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device. XVII.B.2.d.(ii) All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 17. Point 004: This source is located in an ozone non-attainment or attainment- maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 18. Point 004: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): AIRS ID: 123/9D57 Page 7 of 15 olor. Depa en . -� 'Ii 'Health and Environment it Pollution Control Division a. Hoses FII . °°'i s, - ,r v. -• al ' -fined - event 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 the conditions (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. 19. Point 004: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 20. Point 005 and 007: The separator(s) covered by this permit is subject to Regulation 7, Section XVII.G. (State Only). On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. 21. Point 007: The open flare covered by this permit has been approved as an alternative emissions control device under Regulation Number 7, Section XVII.B.2.e. The open flare must have no visible emissions during normal operations and be designed so that an observer can, by means of visual observation from the outside of the open flare, or by other convenient means approved by the Division, determine whether it is operating properly. This open flare must be equipped with an operational auto-igniter according to the following schedule: • All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device; OPERATING & MAINTENANCE REQUIREMENTS 22. Point 002, 003, 005, and 007: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 23. Point 002, 003, 005, and 007: The owner or operator shall demonstrate compliance with opacity standards, using EPA Method 22 to determine the presence or absence of visible emissions. "Visible Emissions" means observations of smoke for any period or periods of duration greater than or equal to one (1) minute in any fifteen (15) minute period during normal operation. (Reference: Regulation No. 7, Section XVII.A.lI) AIRS ID: 123/9D57 Page 8 of 15 ` color Depa en If P li ` Health and Environment -:t it Pollution Control Division ADDITIONAL REQU L ,-; N ,a 24. 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 (NOr) 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. 25. 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). 26. 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 27. 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. AIRS ID: 123/9D57 Page 9 of 15 `7` olor. A Depa en . - .li Health and Environment it Pollution Control Division 28. If this permit all ,- - e `' - fin,:. -= atio 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. 29. 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. 30. 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. 31. 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 n apermit are contested by the owner or operator, or the permit, conditions imposed upon p , P P 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. 32. 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 thepermit. Upon notification, annual fee q 9 P billing will terminate. 33. 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: Bradley Eades Permit Engineer AIRS ID: 123/9D57 Page 10 of 15 olora a i Depar42,nent f Pyz Ii Health and Environment it Pollution Control Division 5. fljji Permit Histor i, ..::P _ y Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 12319D57 Page 11 of 15 olor._� Depa en . ' .Ii Health' and Environment ' •it Pollution Control Division Notes to Permit Holder me o •e ` ' a -. 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.qov/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 Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (lb/yr) reportable? (Ib/yr) Benzene 71432 245 No 12 n-Hexane 110543 1647 Yes 82 002 Toluene 108883 210 No 11 Ethylbenzene 100414 35 No 2 Xylenes 1330207 70 No 4 Benzene 71432 1042 Yes 52 003 n-Hexane 110543 3276 Yes 164 Benzene 71432 10 No 10 n-Hexane 110543 114 No 114 004 Toluene 108883 7 No 7 Xylenes 1330207 2 No 2 Benzene 71432 1405 Yes 70 n-Hexane 110543 10965 Yes 548 005 Toluene 108883 1799 Yes 90 Ethylbenzene 100414 520 Yes 26 Xylenes 1330207 847 Yes 42 AIRS ID: 123/9D57 Page 12 of 15 gi 1olor Depa a en f P . Ii&Health and Environment ciy it Pollution Control Division Berms.,. St 4 -1 29 007 n-Hexane 110543 4302 Yes 215 Toluene 108883 824 Yes 41 007 Ethylbenzene 100414 384 Yes 19 Xylenes 1330207 689 Yes 35 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Emission Factors Uncontrolled Pollutant lb/BBL Source Condensate Throughput VOC 1.29 n-Hexane 0.047 Benzene 0.007 ProMax 3.2 Toluene 0.006 Ethylbenzene 0.001 Xylenes 0.002 Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 003: Emission Factors Pollutant Uncontrolled Source lb/BBL Produced Water Throughput VOC 0.262 n-Hexane 0.022 CDPHE Benzene 0.007 Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 004: Emission Factors - Uncontrolled Pollutant lb/BBL loaded Source VOC 0.1558 AP-42 Benzene 0.0003 AP-42 n-Hexane 0.0033 AP-42 Toluene 0.0002 AP-42 Xylenes 0.0001 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 AIRS ID: 123/9D57 Page 13 of 15 olorl,Depa en - •Ii Health and Environment it Pollution Control Division S = 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) =6.45 psia M (vapor molecular weight) =46.7 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 sales oil sample analysis by the VOC emission factor. Point 005: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx --- 129.1 129.1 AP-42/Gas Analysis CO --- 588.4 588.4 AP-42/Gas Analysis VOC 59.71 53991.8 2699.6 Gas Analysis Benzene 0.24 213.2 10.7 Gas Analysis Toluene 0.30 272.8 13.7 Gas Analysis Ethylbenzene 0.09 78.9 78.9 Gas Analysis Xylenes 0.14 128.4 6.4 Gas Analysis n-hexane 1.84 1662.8 83.1 Gas Analysis Note: Emission factors are based on "LP Flash Gas" sample analysis from Crow Valley 7-62-24- 2H sampled 04/10/2015. Point 007: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx --- 89.8 89.8 AP-42/Gas Analysis CO --- 409.2 409.2 AP-42/Gas Analysis VOC 29.64 18278.9 913.9 Gas Analysis Benzene 0.09 57.0 2.9 Gas Analysis Toluene 0.13 82.5 4.1 Gas Analysis Ethylbenzene 0.06 38.5 1.9 Gas Analysis Xylenes 0.11 69.1 3.4 Gas Analysis n-hexane 0.70 430.6 21.5 Gas Analysis Note: Emission factors are based on"Sales Gas" sample analysis from Crow Valley 7-62-24-2H sampled 04/10/2015. 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 AIRS ID: 123/9D57 Page 14 of 15 VLolor_P Depa en u P‘.. li Health and Environment NA. A Z-1 g it Pollution Control Division u Operating Permit ynt: M rc- « VOC, n-Hexane NANSR Synthetic Minor Source of: VOC MACT HH Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60, Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/9D57 Page 15 of 15 Division Information Engineer: Bradley Eades Control Engineer: Christopher Laplante Review Date: 10/13/2015 Application Date: 05/29/2015 Facility Identifiers Permit No. 15WE0998 Potentially located in ozone nonattainment area AIRs County# 123 'Weld Facility# 9D57 Facility Type: exploration and production facility 2 Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: 1 VOC f NOx F CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Crow Valley 7-62-24 2H Production Facility Source Location: NENW Sec. 24, T7N, R62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address Address 2: 410 17th Street,Suite 1400 ty,State Zip: Denver, CO Name: Jerry Dismukes Person To Phone: 303-803-1724 Contact Fax: 000-000-0000 Email: Jdismukes@bonanzacrk.com 'Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Crow Valley 7-62-24 2H Production Facility, located in the NENW Sec. 24,T7N, R62W,Weld County, Colorado. Point Name Type Control Action Newly 002 CNDTK-1 Condensate Tanks Flare reported source Newly 003 PW Water Tanks Flare reported source Newly 004 TLO Loadout None reported source Newly 005 SEP-1 Separator Venting Flare reported source Newly 007 FL-2 Separator Venting Flare reported source 1500 bbl Storage Tank used to store condensate.Tank consists of three(3)500 bbl liquid 002 manifold vessels. Requsted Throughput 35040 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 1.29 lb/bbl 22.6 tpy 1.1 tpy Benzene 0.007 lb/bbl 245.3 lb/yr 12.3 lb/yr Toluene 0.006 lb/bbl 210.2 lb/yr 10.5 lb/yr Ethylbenze 0.001 lb/bbl 35.0 lb/yr 1.8 lb/yr ProMax Xylenes 0.002 lb/bbl 70.1 lb/yr 3.5 lb/yr 224-TMP 0.01 lb/bbl 350.4 lb/yr 17.5 lb/yr n-Hexane 0.047 lb/bbl 1646.9 lb/yr 82.3 lb/yr NOx' 0.0037 lb Nox/Ib VO( 0.0037 lb Nox/Ib VOC CDPHE CO' 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC *Not Reportable 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 6 New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because facility stores condensate prior to custody transfer and has a design capacity less than 1589.9 m^3(10,000 bbl). NSPS OOOO:for storage vessels in the natural gas production,transmission,and processing segments. This source is not subject because each tank has a"legal and practically enforceable limit"less than 6 tpy VOC per vessel with these permit limits. Regulation 7-Volatile Organic Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS Applicant is not currently subject since API gravity of liquid stored(as provided in application)is<40 (Analysis:Crow Valley 7-62-24 2H,Sales Oil,Sampled:04/19/2015)however applicant has requested that the liquid is treated as condensate for permitting since the API gravity flunctuates above and below 40. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject since uncontrolled emissions are projected to to be greater than 6 tpy. Application Notes: *The sales oil analysis submitted with the application indicates a sales oil API gravity of 37.However,applicant is requesting that the permit reflect that the liquid stored is condensate. 003 One (1) above ground 500 bbl produced water storage tank Emissions Calculations Requsted Throughput 148920 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 19.50852 tpy 0.975426 tpy CDPHE Benzene 0.007 lb/bbl 1042.44 lb/yr 52.122 lb/yr CDPHE n-Hexane 0.022 lb/bbl 3276.24 lb/yr 163.812 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 STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject since uncontrolled emissions are projected to to be greater than 6 tpy. 004 Hydrocarbon Loadout to Tanker Trucks Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2, Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 6.45 psia Sales Oil Analysis/Raoult's LawNp(Mpbpwin v1.43) M Molecular Weight of Var 46.7 lb/lb-mole AP-42(Ch.7.1 eqn 1-22) T Liquid Temperature 524 deg. R Field Data C VOC Wt% 0.8634 IbVOC/Ib AP-42(Ch.7.1 eqn 1-22) L 3.71 lb/10^3 gal 1.56E-01 lb/bbl Annual requested Throughput 35040 BBL/yr 1471680 gal/yr Annual requested VOC emissions 5461 lb/yr 2.73 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0018 n-hexane 0.0209 Toluene 0.0013 Xylenes 0.0003 Sales Oil Composition&AP-42 Ch.7 eqn 1-22(CV 7-62-24 2H, "Sales Oil", Sampled:4/10/2015) Source: Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.1558 lb/bbl 2.73 tpy 2.73 tpy AP-42 Benzene 0.0003 lb/bbl 9.6 lb/yr 9.6 lb/yr AP-42 n-Hexane 0.0033 lb/bbl 114 lb/yr 114 lb/yr AP-42 Toluene 0.0002 lb/bbl 7 lb/yr 7 lb/yr AP-42 Xylenes 0.0000 lb/bbl 2 lb/yr 2 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(238 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 II.D.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,Part B,Section II.D.1.1 One low-pressure separator controlled by one enclosed flare.Flare has a minimum control efficiency of 005 95%. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(0) 6.6 MMscf/yr 753.4246575 scf/hr MW 34.2503 Ib/Ib-mol 0.018082192 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.01 4.0026 0.000 0.000 0.00 6.97 0.00 CO2 3.87 44.01 1.701 0.050 3.38 29624.47 14.81 N2 0.35 28.013 0.098 0.003 0.20 1713.73 0.86 methane 40.44 16.041 6.486 0.189 12.89 112956.11 56.48 ethane 18.31 30.063 5.504 0.161 10.94 95849.49 47.92 propane 18.91 44.092 8.337 0.243 16.57 145180.34 72.59 isobutane 2.43 58.118 1.412 0.041 2.81 24580.42 12.29 n-butane 8.08 58.118 4.694 0.137 9.33 81750.86 40.88 isopentane 1.82 72.114 1.312 0.038 2.61 22849.48 11.42 n-pentane 2.47 72.114 1.780 0.052 3.54 31000.95 15.50 cyclopentane 0.32 70.13, 0.223 0.007 0.44 3878.73 1.94 n-Hexane 0.73 86.18 0.630 0.018 1.25 10964.55 5.48 cyclohexane 0.35 84.16 0.293 0.009 0.58 5097.30 2.55 Other hexanes 0.93 86.18 0.798 0.023 1.59 13894 04 6.95 heptanes 0.25 100.21 0.252 0.007 0.50 4387.14 2.19 methylcyclohexane 0.23 98.19 0.222 0.006 0.44 3864.39 1.93 224-TMP 0.10 114.23 0.117 0.003 0.23 2031.00 1.02 Benzene 0.10 78.12 0.081 0.002 0.16 1405.29 0.70 Toluene 0.11 92.15 0.103 0.003 0.21 1798.89 0.90 Ethylbenzene 0.03 106.17 0.030 0.001 0.06 519.53 0.26 Xylenes 0.05 106.17 0.049 0.001 0.10 846.78 0.42 C8+Heavies 0.10 135.2819359 0.129 0.004 0.26 2242.75 1.12 VOC mass frac 0.597 Total VOC(Uncontrolled) 178.15 Notes Mole%,MW,and mass fractions from Crow Valley 7-62-24-2H(LP Flash Gas)analysis collected 04/10/2015. 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. 15WE0998.CP1.xlsm One low-pressure separator controlled by one enclosed flare.Flare has a minimum control efficiency of 005 95%. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Leed Model L30-0011 48" Serial Number 24673 Gas Heating Value 1898 Btu/scf Throughput 12526.8 MMBtu/yr VRU Information THIS SITE DOES NOT USE VRUs TO COLLECT GAS FROM THIS PROCESS UNIT Equipment Description Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 jib NOX/MMBtu 0.31 IIb CO/MMBtu Caclulated Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 53984 Ib/MMscf 2699.19 lb/MMscf 178.1 tpy 8.91 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.43 tpy 0.43 tpy AP-42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 1.9 tpy 1.94 tpy AP-42 Benzene 212.92 lb/MMscf 10.65 lb/MMscf 1405 lb/yr 70 lb/yr Gas Analysis n-Hexane 1661.30 lb/MMscf 83.0648 lb/MMscf 10965 lb/yr 548 lb/yr Gas Analysis Toluene 272.560 Ib/MMscf 13.6280 lb/MMscf 1799 lb/yr 90 lb/yr Gas Analysis Xylenes 128300 lb/MMscf 6.4150 lb/MMscf 847 lb/yr 42 lb/yr Gas Analysis Ethylbenzene 78.717 Ib/MMscf 3.9359 lb/MMscf 520 lb/yr 26 lb/yr Gas Analysis *Emissions factors used in permit reflect applicant calcualtions.Difference is due to rounding and are insignificant. Emissions Factors for Permit Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 53992 lb/MMscf 2699.59 lb/MMscf 178.2 tpy 8.9 tpy Gas Analysis Nox' 129.064 lb/MMscf 0.4 tpy 0.4 tpy AP-42 CO* 588.38 lb/MMscf 1.9 tpy 0.1 tpy AP-42 Benzene 213.2 lb/MMscf 10.66 lb/MMscf 1407.1 lb/yr 70.4 lb/yr Gas Analysis n-Hexane 1662.80 lb/MMscf 83.1400 lb/MMscf 10974.5 lb/yr 548.7 lb/yr Gas Analysis Toluene 272.800 lb/MMscf 13.6400 lb/MMscf 1800.5 lb/yr 90.0 lb/yr Gas Analysis Xylenes 128.400 lb/MMscf 6.4200 lb/MMscf 847.4 lb/yr 42.4 lb/yr Gas Analysis Ethylbenzene 78.900 lb/MMscf 3.9450 Ib/MMscf 520.7 lb/yr 26.0 lb/yr Gas Analysis *Based on AP-42 emission factors,Gas heating value,and requested gas througput to flare Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 NOTES: *Jerry Dismukes confirmed that this is a single-well facility that does not have a VRT and a meter is installed on the Separator vapor to ECD line that measures the flow of gas from this emissions point.(Other sites have a mass ECD meter that measures the combined inlet streams from other emissions units such as tanks,loadout,pumps,etc.) *ProMax model used to predict volumetric flow from the LP Separator does not match with sampled values.This was communicated with applicant who informed that they would still like to move forward with the requested throughput. This was allowed since the actual volume will be monitored directly as stated above. 15WE0998.CP1.xlsm E0998.CP 1.xlsm • One backup/emergency flare used to control emissions of natural gas at this site.Flare has a minimum 007 control efficiency of 95%. 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 O=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas`MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(Q) 10 MMscf/yr 1141.552511 scf/hr MW 23.35740724 Ib/Ib-mol 0.02739726 MMscf/d mole V. MW Ibx/Ibmol mass fraction lb/hr Ib r tpy PY Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.79 44.01 1.227 0.053 3.69 32361.87 16.18 N2 0.99 28.013 0.279 0.012 0.84 7352.86 3.68 methane 72.16 16.041 11.575 0.496 34.86 305416.83 152.71 ethane 11.14 30.063 3.350 0.143 10.09 88378.87 44.19 propane 7.36 44.092 3.245 0.139 9.77 85625.73 42.81 isobutane 0.81 58.118 0.469 0.020 1.41 12382.66 6.19 n-butane 2.58 58.118 1.501 0.064 4.52 39599.98 19.80 isopentane 0.53 72.114 0.382 0.016 1.15 10078.84 5.04 n-pentane 0.70 72.114 0.503 0.022 1.52 13284.96 6.64 cyclopentane 0.08 70.13 0.058 0.002 0.17 1528.43 0.76 n-Hexane 0.19 86.18 0.163 0.007 0.49 4302.18 2.15 cyclohexane 0.09 84.16 0.077 0.003 0.23 2034.05 1.02 Other hexanes 0.24 86.18 0.210 0.009 0.63 5552.81 2.78 heptanes 0.07 100.21 0.072 0.003 0.22 1887.86 0.94 methylcyclohexane 0.06 98.19 0.063 0.003 0.19 1658.09, 0.83 224-TMP 0.03 114.23 0.031 0.001 0.09 828.85 0.41 Benzene 0.03 78.12 0.022 0.001 0.07 570.96 0.29 Toluene 0.03 92.15 0.031 0.001 0.09 824.24 0.41 Ethylbenzene 0.01 106.17 0.015 0.001 0.04 383.78 0.19 Xylenes 0.02 106.17 0.026 0.001 0.08 689.12 0.34 C8+Heavies 0.05 127.775098 0.059 0.003 0.18 1547.46 0.77 VOC mass frac 0.297 Total VOC(Uncontrolled) 91.39 Notes Mole%,MW,and mass fractions from Crow Valley 7-62-24-2H(Sales Gas)analysis collected 04/10/2015. 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. 15WE0998.CP1.xlsm One backup/emergency flare used to control emissions of natural gas at this site.Flare has a minimum 007 control efficiency of 95%. Flaring Information Equipment Description Flare to combust sales gas from the gas/liquid separator during gathering system downtime. Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1320 Btu/scf Throughput 13200 MMBtu/yr VRU Information THIS SITE DOES NOT USE A VRU Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup 1 'Overall Control 1 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 llb NOX/MMBtu 0.31 rib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions VOC 18278 lb/MMscf 913.90 lb/MMscf 91.4 tpy 4.6 tpy Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.4 tpy 0.4 tpy CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 2.05 tpy 2.0 tpy Benzene 57.10 lb/MMscf 2.85 lb/MMscf 571 lb/yr 29 lb/yr n-Hexane 430.22 lb/MMscf 21.5109 lb/MMscf 4302 lb/yr 215 lb/yr Toluene 82.424 lb/MMscf 4.1212 lb/MMscf 824 lb/yr 41 lb/yr Xylenes 68.912 lb/MMscf 3.4456 lb/MMscf 689 lb/yr 34 lb/yr Ethylbenzene 38.378 lb/MMscf 1.9189 lb/MMscf 384 lb/yr 19 lb/yr 'Emissions factors used in"notes to permit holder"reflect the values below.Difference is due to rounding and is insignificant. Emissions Factors for Permit Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18279 lb/MMscf 913.95 lb/MMscf 91.4 tpy 91.4 tpy Gas Analysis Nox' 89.76 lb/MMscf 0.4 tpy 0.4 tpy AP-42 CO' 409.2 lb/MMscf 2.0 tpy 2.0 tpy AP-42 Benzene 57.0 lb/MMscf 2.85 lb/MMscf 570.0 lb/yr 570.0 lb/yr Gas Analysis n-Hexane 430.60 lb/MMscf 21.53 lb/MMscf 4306.0 lb/yr 4306.0 lb/yr Gas Analysis Toluene 82.500 lb/MMscf 4.13 lb/MMscf 825.0 lb/yr 825.0 lb/yr Gas Analysis Xylenes 69.100 lb/MMscf 3.46 lb/MMscf 691.0 lb/yr 691.0 lb/yr Gas Analysis Ethylbenzene 38.500 lb/MMscf 1.93 lb/MMscf 385.0 lb/yr 385.0 lb/yr Gas Analysis 'Based on AP-42 emission factors,Gas heating value,and requested gas througput to flare Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 NOTES: 'This emissions point is not currently installed at the site.It is a trailer mounted flare that will be brought to the site in the event of upsets/emergency(pipeline shut in,pressure issues,etc.). This flare is being approved for use as an alternative emissions control device per XVII.B.2.e.The flare is approved because it meets the following criteria: -The flare is not the primary destination for emissions(routed to sales during normal operation) -The flare will be able to control 95%of hydrocarbon emissions and have a manufacturers design guarantee of 98%control for hydrocarbons;and -The open flare will operate with no visible emissions,be equipped with an autoigniter,and otherwise be able to comply with the requirements of section XVII.B. 'It was communicated to applicant that in the future facility needs to submit application for alternative emissions control device per Division Memo 15-03.The AECD is being approved at this site since the application was filed prior to the publishing of this information. • 15WE0998.CP1.xlsm AIRS(County/Plant) 123/9D57 Permit No. 15WE0998 Date 10/13/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emisison Factor Emissions Emissions PTE Ctrl. reportable Point# SCC Pollutant or CAS Factor Source (tpy)* (tpy)* (tpy)* Eff% ? 002 40400311 VOC 30.715 lb/1000 ga E&P TANK 1.1 22.6 95% Yes 002 40400311 Benzene 0.167 lb/1000 ga E&P TANK 12.3 245.3 95% No 002 40400311 n-Hexane 1.119 lb/1000 ga E&P TANK 82.3 1646.9 95% Yes 002 40400311 Ethylbenzene 0.024 lb/1000 ga E&P TANK 1.8 35 95% No 002 40400311 Xylenes 0.048 lb/1000 ga E&P TANK 3.5 70.1 95% No 003 40400315 VOC 6.238 lb/1000 ga CDPHE 1 19.5 95% Yes 003 40400315 Benzene 0.167 lb/1000 ga CDPHE 52.1 1042.4 95% Yes 003 40400315 n-Hexane 0.524 lb/1000 ga CDPHE 163.8 3276.2 95% Yes 004 40600132 VOC 3.711 lb/1000 ga AP-42 2.7 2.7 0% Yes 004 40600132 Benzene 0.007 lb/1000 ga AP-42 9.6 9.6 0% No 004 40600132 n-Hexane 0.078 lb/1000 ga AP-42 114.3 114.3 0% No 004 40600132 Toluene 0.005 lb/1000 ga AP-42 7 7 0% No 004 40600132 Xylenes 0.001 lb/1000 ga AP-42 1.7 1.7 0% No 005 31000205 VOC 53983.705 lb/MMscf Gas Analysis 8.9 178.1 95% Yes 005 31000205 NOx 0.068Ib/MMBTUAP-42 0.4 0.4 0% No 005 31000205 CO 0.31 Ib/MMBTU AP-42 1.9 1.9 0% Yes 005 31000205 Benzene 212.923 lb/MMscf Gas Analysis 70.3 1405.3 95% Yes 005 31000205 n-Hexane 1661.296 lb/MMscf Gas Analysis 548.2 10964.6 95% Yes 005 31000205 Toluene 272.56 lb/MMscf Gas Analysis 89.9 1798.9 95% Yes 005 31000205 Ethylbenzene 78.717 lb/MMscf Gas Analysis 26 519.5 95% Yes 005 31000205 Xylenes 128.3 lb/MMscf Gas Analysis 42.3 846.8 95% Yes 007 31000205 VOC 18278 lb/MMscf Gas Analysis 4.6 91.4 95% Yes 007 31000205 NOx 0.068 lb/MMBTU AP-42 0.4 0.4 0% No 007 31000205 CO 0.31 Ib/MMBTU AP-42 2 2 0% Yes 007 31000205 Benzene 57.096 Ib/MMscf Gas Analysis 28.5 571 95% Yes 007 31000205 n-Hexane 430.218 lb/MMscf Gas Analysis 215.1 4302.2 95% Yes 007 31000205 Toluene 82.424 lb/MMscf Gas Analysis 41.2 824.2 95% Yes 007 31000205 Ethylbenzene 38.378 lb/MMscf Gas Analysis 19.2 383.8 95% Yes 007 31000205 Xylenes 68.912 lb/MMscf Gas Analysis 34.5 689.1 95% Yes 3 c ev o 0 0 c o o o c ��. 3 > Z z z w e :: °a ° o 0o n ,a °; o :-.5 o ,. a s v a.) mss, ❑ ®❑ o w a cnmm c 0 ccl d > q vNi v y > z �o d •/`� h rn rn z A o 0 n • W •d W C a, �, i. 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