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Home My WebLink About20142921.tiff ,A CDPHE COLORADO CO Department of Public ..• Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board B 0 St PO RECEIVED PO Box 7 758 Greeley, CO 80632 SEP 1 9 2014 September 17, 2014 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On September 20, 2014, the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company, LLC - Seventy Holes 44.5, in the The Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, • I, if • i a.eL 1:, 2R(L .tij Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure et'.7L W I NL 2014-2921 rRibtki Raute�J )19 �` Q 4300 Cherry Creek Drive S., Denver,CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe 7,/ 751 1>h- 0( 't I John W. Hickenlooper,Governor Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer 1- ,{+ 1e96.�' CDPHE Public Notice Of A Proposed Project Or Activity Warranting Public CO trtComment Website Title: Bonanza Creek Energy Operating Company, LLC - Seventy Holes 44-5 - Weld County Released To: The Greeley Tribune On: September 17, 2014 Published: September 20, 2014 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company, LLC Facility: Seventy Holes 44-5 Oil and gas production facility SESE Sec 5, T4N, R62W Weld County The proposed project or activity is as follows: Applicant proposes to operate a new oil and gas production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 14WE0625 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.cotorado.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 u A® COLORADO wu�.m. 1I STATE OF COLORADO OF�Ol9 LO D T F P = C HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION Fena0 • TELEPHONE: (303)692-3150 �. *1876* CONSTRUCTION PERMIT PERMIT NO: 14W E0625 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 Seventy Holes 44-5 Production Facility, located in the SESE of Section 5, 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 Condensate Six(6)above ground 500 bbl atmospheric condensate 003 storage tanks controlled by four enclosed flares. Each flare Tanks has a minimum combustion efficiency of 95%. One (1)above ground 400 bbl produced water storage tank PW Tanks 004 and two (2)60 bbl produced water vaults. The 400 bbl storage tank is controlled by four enclosed flares. Each flare has a minimum combustion efficiency of 95%. Truck 005 Truck Condensate Loadout Loadout FUG 006 Fugitive VOC equipment leaks Sep-1 and Two(2)low-pressure separators controlled by four enclosed Sep-2 007 flares.r Each flare has a minimum combustion efficiency of 95/0. One (1) pneumatic water transfer pump, rated at 600 scf/hr P-1 008 (Sandpiper, Model G1F, Serial number 2076873). The pneumatic pump is controlled by four enclosed flares. Each flare has a minimum combustion efficiency of 95%. One emergency flare with a minimum combustion efficiency FL-1 009 of 95%.The flare is not enclosed.The emergency flare is used during periods when the pipeline is not available. AIRS ID: 123/9C08 Page 1 of 21 Dci pa e i eaith and Environment 'r Pollution Control Division Point 008: This pu a p in ance 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 tan), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. AIRS Point 009: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdohe.state.co.us/ao/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. AIRS Point 009: The following information shall be provided to the Division within fifteen (15)days after commencement of operation. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 3. AIRS Point 009: Within one hundred and eighty days (180) after commencement of operation, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 4. AIRS Points 003 - 008: 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.cdohe.state.co.us/ao/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 5. AIRS Points 003-008:Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit (Reference: Regulation No. 3, Part B, III.G.2). 6. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either,the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable AIRS ID: 123/9C08 Page 2 of 21 olor epa en P li ealth and Environment it Pollution Control Division time of the c t e. ision grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, IIl.F.4.) 7. AIRS Point 007: 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 each 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. 8. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 9. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 10. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type NO, Equipment ID Point VOC CO Condensate 003 --- 6.5 1.2 Point Tanks PW Tanks 004 --- 0.8 -- Point Truck Loadout 005 --- 19.0 -- Point FUG 006 --- 12.2 -- Fugitive Sep-1 and Sep- 007 1.1 25.3 6.0 Point 2 P-1 008 --- 2.0 1.3 Point FL-1 009 --- 5.3 3.4 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 AIRS ID: 123/9C08 Page 3 of 21 pa e i ealth and Environment r Pollution Control Division twelve-month I t 'on u ' uiring an APEN, at this facility. 11. AIRS Point 006:The operator shall calculate actual emissions from this emissions point ' based on representative component counts for the facility with the most recent extended gas analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 12. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B,Section III.E.) Facility Pollutants Equipment Point Control DeviceP Controlled ID Condensate 003 Enclosed Flare VOC Tanks PW Tanks 004 Enclosed Flare VOC Sep-1 and 007 Enclosed Flare VOC Sep-2 P-1 008 Enclosed Flare VOC FL-1 009 Open Flare VOC PROCESS LIMITATIONS AND RECORDS 13. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility I AIRS Equipment point Process Parameter Annual Limit I ID _ Condensate 003 Condensate Throughput 144,540 BBL Tanks PW Tanks 004 Produced Water Throughput 127,020 BBL Truck 005 Condensate Loaded 144,540 BBL Loadout FUG 006 NA NA Sep-1 and 007 Total Gas Vented from Both Low- 15.0 MMSCF Sep-2 Pressure Separators P-1 008 Natural Gas Consumed _ 5.3 MMSCF FL-1 009 Total Gas Vented from Separator to 13.8 MMSCF Emergency Rare AIRS ID: 123/9O08 Page 4 of 21 epa en P Ii ealth and Environment it Pollution Control Division ComplianceDolor Ii a det ' ed on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility,for Division review. 14. AIRS Point 007: Upon installation of the flow meter required under Condition 7, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from each low pressure separator using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented from each low-pressure separator. The owner or operator shall use the sum of monthly throughput records from both low-pressure separators to demonstrate compliance with the limits specified in Condition 13 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 15. AIRS Points 003, 004, 005, 007, 008, 009: The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 16. Visible emissions shall not exceed twenty percent(20%)opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. &4.) 17. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 18. 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. No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 20. AIRS Point 003: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 21. 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. AIRS ID: 123/9C08 Page 5 of 21 D of pa en i ealh and Environment 'r Pollution Control Division 22. AIRS Point g ver 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. 23. AIRS Points 003 and 004:The flare 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.1.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. . 24. 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.(ixb) 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, visual, olfactory("AVO")and additional visual inspections of the storage tank and any associated equipment (e.g. separator, air pollution control equipment, or other pressure reducing equipment) at the same frequency as liquids are loaded out from the storage tank. These inspections are not required more frequently than every seven (7) days but must be conducted at least every thirty one (31) days. Monitoring is not required for storage tanks or associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i)Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; AIRS ID: 12319C08 Page 6 of 21 olor epa en P li ealth and Environment it Pollution Control Division XVII.CJJ i n ' oring 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 containing only stabilized liquids. The minimum elements of STEM are listed below. XVII.C.2.b.(i) STEM must include selected control technologies, monitoring practices, operational practices, and/or other strategies; procedures for evaluating ongoing storage tank emission capture performance; and monitoring in accordance with approved instrument monitoring methods following the applicable schedule in Section XVII.C.2.b.(ii) and Inspection Frequency in Table 1. XVII.C.2.b.(ii) Owners or operators must achieve the requirements of Sections XVII.C.2.a. and XVII.C.2.b. and begin implementing the required AIRS ID: 123/9C08 Page 7 of 21 1101 pa e i ealth and Environment 'r Pollution Control Division i it od i ance with the following schedule: XVII.C.2.b.(iiXb) 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 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. AIRS ID: 123/9O08 Page 8 of 21 epa en P li ealth and Environment it Pollution Control Division XVII.C.3.c. ThDolor i y re th ollution 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. 25. 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) 26. 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 26 (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. 27. 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. 28. AIRS Point 006: This source is subject to Regulation No. 7, Section XVII.F. leak detection and repair requirements, which include but are not limited to: XVII.F.1. As of the compliance date specified in XVII.F.4, the provisions of Section XVII.F. shall apply in lieu of any directed inspection and maintenance program requirements established pursuant to Regulation Number 3, Part B, Section I I I.D.2. XVII.F.4. Requirements for well production facilities XVII.F.4.b. Owners or operators of well production facilities constructed before October 15, 2014, must identify leaks from components using an approved instrument monitoring method within ninety (90) days of the Phase-In Schedule in Table 4; within thirty (30) days for well production facilities subject to monthly approved instrument monitoring method inspections; or by January 1, 2016, for well production facilities subject to a one time approved instrument monitoring method inspection. Thereafter, approved instrument monitoring method and AVO AIRS ID: 123/9C08 Page 9 of 21 I pas i ealth and Environment it Pollution Control Division ins in Inspection Frequencies in Table 4. XVII.F.4.c. The estimated uncontrolled actual VOC emissions from the highest emitting storage tank at the well production facility determines the frequency at which inspections must be performed. Table 4—Well Production Facility Component Inspections Thresholds(per XVII.F.4.c)—Well Production Facilities Approved Instrument AVO with Storage Tanks Monitoring method Inspection Phase-In (tpy) Inspection Frequency Frequency Schedule >0 and <6 One time Monthly January 1,2016 >6 and< 12 Annually Monthly January 1, 2016 > 12 and <50 Quarterly Monthly January 1, 2015 >50 Monthly January 1, 2015 XVII.F.5. If a component is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor the component until it becomes feasible to do so. XVII.F.6 Leaks requiring repair: Leaks must be identified utilizing the methods listed in Section)0/II.F.6. Only leaks detected pursuant to Section XVII.F.6. require repair under Section XVII.F.7. XVII.F.6.a. For EPA Method 21 monitoring, or other Division approved quantitative instrument based monitoring, at facilities constructed before May 1, 2014, a leak is any concentration of hydrocarbon above 2,000 parts per million (ppm) not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation, except for well production facilities where a leak is defined as any concentration of hydrocarbon above 500 ppm not associated with normal equipment operation,such as pneumatic device actuation and crank case ventilation. XVII.F.6.c. For infra-red camera and AVO monitoring, or other Division approved non- quantitative instrument based monitoring, a leak is any detectable emissions not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation. XVII.F.6.e. For leaks identified using an approved instrument monitoring method or AVO, owners or operators have the option of either repairing the leak in accordance with the repair schedule set forth in Section XVII.F.7. or conducting follow-up monitoring using EPA Method 21 within five (5) working days of the leak detection. If the follow-up EPA Method 21 monitoring shows that the emission is a leak as defined in Section XVII.F.6.,the leak must be repaired and remonitored in accordance with Section XVII.F.7. AIRS ID: 123/9C08 Page 10 of 21 olor Depa en P li ealth and Environment it Pollution Control Division XVII.F.7. Rep ' e XVII.F.7.a. First attempt to repair a leak must be made no later than five (5) working days after discovery, unless parts are unavailable, the equipment requires shutdown to complete repair, or other good cause exists. If parts are unavailable, they must be ordered promptly and the repair must be made within fifteen (15) working days of receipt of the parts. If shutdown is required, the leak must be repaired during the next scheduled shutdown. If delay is attributable to other good cause, repairs must be completed within fifteen (15)working days after the cause of delay ceases to exist. XVII.F.7.b. Within fifteen (15) working days of completion of a repair, the leak must be remonitored to verify the repair was effective. XVII.F.7.c. Leaks discovered pursuant to the leak detection methods of Section XVII.F.6. shall not be subject to enforcement by the Division unless the owner or operator fails to perform the required repairs in accordance with Section XVII.F.7. XVII.F.8. Recordkeeping: The owner or operator of each facility subject to the leak detection and repair requirements in Section XVII.F. must maintain the following records for a period of two (2) years and make them available to the Division upon request. XVII.F.8.a. Documentation of the initial approved instrument monitoring method inspection for new well production facilities; XVII.F.8.b. The date and site information for each inspection; XVII.F.8.c. A list of the leaking components and the monitoring method(s) used to determine the presence of the leak; XVII.F.8.d. The date of first attempt to repair the leak and, if necessary, any additional attempt to repair the leak; XVII.F.8.e. The date the leak was repaired; XVII.F.8.f. The delayed repair list, including the basis for placing leaks on the list; XVII.F.8.g. The date the leak was remonitored to verify the effectiveness of the repair, and the results of the remonitoring; and XVII.F.8.h. A list of components that are designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.F.5., an explanation stating why the component is so designated, and the plan for monitoring such component(s). XVII.F.9. Reporting: The owner or operator of each facility subject to the leak detection and repair requirements in Section XVII.F. must submit reports as specified in Section XVII.F.9. 29. AIRS 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 apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). Upon the compliance dated specified in Regulation No. 7, Section XVII.F.4., the provisions of Section XVII.F. shall apply in lieu of RACT requirements established pursuant to Regulation Number 3, Part B, Section III.D.2. This requirement AIRS ID: 123/9C08 Page 11 of 21 d epa en i earth and Environment 'r Pollution Control Division to apply RA b 's i pie the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. AuditoryMsual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection shall occur within one- hundred and eighty(180)days after permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi)below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable,minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING& MAINTENANCE REQUIREMENTS 30. AIRS Points 003, 004, 007, 008 and.009: 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 Reauirements AIRS ID: 123/9C08 Page 12 of 21 olor Depa en P li ealth and Environment it Pollution Control Division 31. AIRS Point 0 nd s (1 er 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. 32. AIRS Point 009: Within one hundred and eighty (180) days after commencement of operation, the owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare when the flare is receiving gas from the separator. (Reference: Regulation No. 1, Section II.A.1 &4) Periodic Testing Requirements 33. AIRS 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 34. AIRS Point 008: 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. 35. AIRS Point 008: 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. 36. AIRS Point 008: 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 37. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30t° 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 AIRS ID: 123/9C08 Page 13 of 21 ol epa en i ealth and Environment it Pollution Control Division For a 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. 38. Federal regulatory program requirements(i.e. PSD, NANSR)shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 39. 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. 40. 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. 41. 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. 42. 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. 43. 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 AIRS ID: 12319C08 Page 14 of 21 epa en P li ealth and Environment it Pollution Control Division Air PollutionDolor i ' ( on et fo ' 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. 44. 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. 45. 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, I civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122 (civil penalties),-122.1 (criminal penalties), C.R.S. By: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 12319C08 Page 15 of 21 B pa en i eatth and Environment r Pollution Control Division Notes to Permit HolderDI 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: htto://www.colorado.aov/cs/Satellite7c=Document C&childpaaename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&oaoename=CBONWraooer 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Iblyr) Benzene 71432 3,022 Yes 151 • n-Hexane 110543 17,594 Yes 880 • Toluene 108883 2,244 Yes 112 003 Ethylbenzene 100414 156 No 8 Xylenes 1330207 667 Yes 33 2,2'4 540841 914 Yes 46 VimethyI entane Benzene 71432 889 Yes 44 004 n-Hexane 110543 2,794 • Yes 140 Benzene 71432 468 Yes 468 n-Hexane 110543 2,417 Yes 2,417 005 Toluene 108883 1,087 Yes 1,087 Ethylbenzene 100414 207 No 207 Xylenes 1330207 992 Yes 992 2,2,4 540841 289 Yes 289 trimethylpentane 006 Benzene 71432 120 No 120 n-Hexane 110543 599 Yes 599 AIRS ID: 123/9C08 Page 16 of 21 olor epa en P li ealth and Environment it Pollution Control Division TolD 8 237 Ethylbenzene 100414 44 No 44 Xylenes 1330207 208 No 208 Benzene 71432 2,297 Yes 115 n-Hexane 110543 13,718 Yes 686 007 Toluene 108883 1,046 Yes 52 Ethylbenzene 100414 88 No 4 Xylenes 1330207 240 No 12 Benzene 71432 120 No 6 n-Hexane 110543 749 Yes 37 008 Toluene 108883 73 No 4 Ethyl benzene 100414 6 No 0.3 Xylenes 1330207 16 No 1 Benzene 71432 315 Yes 16 n-Hexane 110543 1,961 Yes 98 009 Toluene 108883 191 No 10 Ethylbenzene 100414 15 No 1 Xylenes 1330207 42 No 2 5) The emission levels contained in this permit are based on the following emission factors: Point 003: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42, Table 13.5 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42, Table 13.5 VOC 1.7855 0.0893 E&P TANK n-Hexane 0.1217 0.0061 E&P TANK Benzene 0.0209 0.0010 E&P TANK Toluene 0.0155 0.0008 E&P TANK Ethylbenzene 0.0011 0.00005 E&P TANK Xylenes 0.0046 0.0002 E&P TANK 2,2,4 0.0063 0.0003 E&P TANK trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. A HHV of 2,922 BTU/scf was used for combustion calculations. AIRS ID: 123/9C08 Page 17 of 21 al pa en i eolith and r Pollution ControlEnvironment Division Point 004: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL Produced lb/BBL Produced Source Water Throughput Water Throughput 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: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source V0C 0.2624 AP-42 Benzene 0.0032 AP-42 n-Hexane 0.0167 AP-42 Toluene 0.0075 AP-42 Xylenes 0.0069 AP-42 Ethylbenzene 0.0014 AP-42 2'2'4 0.0020 AP-42 trimethylpentane The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95)using the following values: L= 12.46'S'P'M/T S=0.6(Submerged loading: dedicated normal service) P(true vapor pressure)=6.47 psia M (vapor molecular weight)=67.65 Ib/lb-mol T(temperature of liquid loaded)=524 R The uncontrolled non-criteria reportable air pollutant(NCRP)emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 006: Component Gas Heavy Oil Light Oil Water/Oil Connectors 1384 0 606 467 Flanges 66 0 16 18 Open-ended Lines 42 0 6 1 Pump Seals 4 0 0 1 Valves 199 0 78 ' 50 Other 98 0 10 18 VOC Content(wt 0.2559 1 0.9979 1 fraction) Benzene Content(wt. 0.0004 0 0.0123 0.0012 fraction) Toluene Content(wt. 0.0002 0 0.0287 0.0003 fraction) Ethylbenzene(wt. 0.00002 0 0.0055 0.00001 AIRS ID: 12319C08 Page 18 of 21 olor epa en P li ealth and Environment it Pollution Control Division fraction) Xylenes Content(wt. 0.00005 0 0.0262 0.00004 fraction) n-hexane Content(wt. 0.0024 0 0.0637 0.00001 fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors(kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R-95-017 Table 2-4 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent extended gas analysis. Point 007: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx(Ib/MMBTU) --- 0.068 0.068 AP-42 CO(lb/MMBTU) _-- 0.37 0.37 AP-42 VOC 67.4 67,385 3,369.3 Gas Analysis Benzene 0.15 152.74 7.6368 Gas Analysis Toluene 0.07 69.538 3.4769 Gas Analysis Ethylbenzene 0.006 5.8828 0.2941 Gas Analysis Xylenes 0.02 15.968 0.7984 Gas Analysis n-hexane 0.91 912.28 45.614 Gas Analysis Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 12/12/2013 of the gas vented from the low pressure separators at Seventy Holes 44-41-5HNB and T- P-5HNB to estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow. The controlled VOC and HAP emissions factors for point 007 are based on a flare control efficiency of 95%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 2,171 BTU/scf was used for calculations. AIRS ID: 123/9C08 Page 19 of 21 pa en i ealth and Environment 'r Pollution Control Division Point 008: Emission Emission Factors- Factors- Uncontrolled Controlled Pollutant Ib/MMscf vented IblMMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (lb/MMBTU) VOC 15,331 766.56 Gas Analysis Benzene 22.877 1.1438 Gas Analysis n-Hexane 142.57 7.1286 Gas Analysis Toluene 13.8575 0.6929 Gas Analysis Ethylbenzene 1.1205 0.0560 Gas Analysis Xylenes 3.0815 0.1541 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 1,315 BTU/scf was used for calculations Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled Ib/MMscf IbIMMscf NOx _(lb/MMBTU) 0.068 0.068 AP-42 CO _ 0.37 0.37 AP-42 (lb/MMBTU) VOC 25.6 15,331 766.56 Gas Analysis Benzene 0.04 22.877 1.1438 Gas Analysis Toluene 0.02 13.8575 0.6929 Gas Analysis Ethylbenzene 0.002 1.1205 0.0560 Gas Analysis Xylenes 0.005 3.0815 0.1541 Gas Analysis n-hexane 0.24 142.57 7.1286 Gas Analysis Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,315 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, n-hexane,total HAPs AIRS ID: 123/9O08 Page 20 of 21 olor epa en P Ii and Environment it Pollution ealth ConVol Division NANSR VOC rc MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecf.q poaccess.q ov/ Part 60:Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart 7777—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification. AIRS ID: 123/9C08 Page 21 of 21 Division Information Engineer: Carissa Money Control Engineer: Chris Laplante Review Date: 09/10/2014 Application Date: 01/31/2014 Facility Identifiers Permit No. 14W E0625 AIRS County It 123 Weld Facility it 9C08 Facility Type:exploration and production facility l7 looted in the 8-haur non-allainmeit area? 0 True Minor 0 Synthetic Minor for: R VOC r NOx r co Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Seventy Holes 44-5 Production Facility Source Location: SESE of Section 5,T4N,R62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address Address 2: 410 17th Street,Suite 1500 ty,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pvoung@bonanzacrk.com 'Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Seventy Holes 44-5 Production Facility,located in the SESE of Section 5,T4N,R62W,Weld County.Colorado. Point Name Type Control Action Newly Condensate 003 Condensate Tanks Flare reported Tanks source Newly 004 PW Tanks Water Tanks Flare reported source Truck Newly 005 Loadout None reported Loadout source Newly 006 FUG Fugitives None reported source Newly Sep-1 and 007 Sep-2 Separator Venting Flare reported source Newly 008 P-1 Pump Flare reported source Newly 009 FL-1 Separator Venting Flare reported source 003 Six(6)500 bbl above ground atmospheric condensate storage tanks controlled by four sodas Requsted Throughput 144540 bbl Control Flare Efficiency 95.00%4 Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 1.7855 Ib/bbl 129.0 tpy 6.5 tpy E&P TANK Benzene 0.0209 lb/bbl 3022 lb/yr 151 lb/yr E&P TANK n-Hexane 0.12171b/bbl 17594 lb/yr 880 lb/yr E&P TANK Toluene 0.0155 Ib/bbl 2244 lb/yr 112 lb/yr E&P TANK Ethylbenze 0.0011 lb/bbl 156 lb/yr 8 lb/yr E&P TANK Xylenes 0.0046 Ib/bbl 667 lb/yr 33 lb/yr E&P TANK 2,2,4-TMP 0.0063 Ib/bbl 914 lb/yr 46 lb/yr E&P TANK Nox 0.068 Ib/Mmbtu 0.23 tpy 0.23 tpy AP-42 Table 1 CO 0.37 Ib/Mmbtu 1.23 tpy 1.23 tpy AP-42 Table 1 Regulatory Review Section IIA1-Except as provided in paragraphs 2 through 6 below,no owner or operator of a source shall Now 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, pendix A(July,1992))in all subsections of Section II.A and B of this regulation. Section IIA5-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 °sphere 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. Section LA-No person,wherever located,shall cause or alow 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 K is a violation K odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air. NSPS Kb: for storage vessels greater than 19,800 gallons after 7123184. The 500 bbl tanks are above the minimum capacity threshold of-471 bbl.However,the tanks are located at the Ilhead site,store condensate,and are prior to custody transfer,thus,the tanks are exempt from NSPS Kb (60.110b(d)(4)). NSPS 0000:for storage vessels in the natural gas production,transmission,and processing segments. This source is not subject because each tank emits lass than 6 tpy VOC on a controlled,permitted basis. .VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS PPOcant is subject to the emission control requirement for condensate tanks since It/s located In the nonattalnment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... is currently subject to this since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions an greater than 6 spy. 14WE0625.CP1 123/9008 004 One(1)400 bbl above ground produced water storage tank and two(2)60 bbl concre The 400 bbl storage tank is controlled by four enclosed flares. Emissions Calculations Requsted Throughput 127020 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.262 lb/bbl 16.6 tpy 0.8 tpy CDPHE Benzene 0.007 lb/bbl 889 lb/yr 44 lb/yr CDPHE n-Hexane 0.022 lb/bbl 2794 lb/yr 140 lb/yr CDPHE Pollutant Controlled Emission Factor V0C 0.0131 lb/bbl Benzene 0.00035 lb/bbl n-Hexane 0.0011 lb/bbl 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. Reaulation 7—Volatile Oroanic Compounds XVII.C.1.b Applicant is subject since actual uncontrolled emissions are greater than 6 tpy. 14WE0625.CP1 123/9C08 005 Truck Condensate Loadout Calculations L=12.46*5*P*M/T(AP-42:Chapter 5.2,Equation 1) I.=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units - Source I 5 Saturation Factor 0.6 AP-42 P True Vapor Pressure 6.47 psia Sales Oil Analysis documenting RVP 8.6 and AP- Molecular Weight of Va( 67.65 lb/lb-mole Sales oil analysis for RVP 8.6 and interpolating vs T Uquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver,CO L 6.249 lb/10"3 gal 2.62E-01 lb/bbl Annual requested Throughput 144540 BBL/yr 6070680 gal/yr Annual requested VOC emissions 37933 lb/yr 18.97 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0123 n-hexane 0.0637 Toluene 0.0287 Xylenes 0.0262 Ethylbenzen 0.0055 2,2,4-TMP 0.0076 Source: Pressurized oil analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2624 lb/bbl 19.0 tpy 19.0 tpy AP-42 Benzene 0.0032 lb/bbl 468 lb/yr 468 lb/yr AP-42 n-Hexane 0.0167 lb/bbl 2417 lb/yr 2417 lb/yr AP-42 Toluene 0.0075 lb/bbl 1087 lb/yr 1087 lb/yr AP-42 Xylenes 0.0069 lb/bbl 992 lb/yr 992 lb/yr AP-42 Ethylbenzen 0.0014 lb/bbl 207 lb/yr 207 lb/yr AP-43 2,2,4-TMP 0.0020 lb/bbl 289 lb/yr 289 lb/yr AP-44 Regulatory Review IReordation 7-Volatile Croat*Camoounds This facility is not considered a bulk plant(in Reg.7)because it does not distribute gasoline. 14WE0625.CP1 123/9C08 076 fugitive equipment leaks Regulation 7 Information Operating Hours-. 8780 hourslyear ' Emission Factor Source EPA-4531R-95O17 Table 2-4 Control Efficiency Source. None Calculations Emission Fabr(kcal° Emissions Santa Component Type Count source) Control(%)Pollutant Maas Fraction (try) Table 2-4 Table 28 Re9.3 Connectors 1384 2.00E-04 100E-05 00% VOC 0255995 5.3135373 Flanges 06 3.90E-04 570E-06 0 0% Benzene 0.000382 0.0079289 Open-Ended Lines 42 2.00E-03 150E-05 0 0% Toluene 0000231 0.0047947 Gas Pump Seals 4 2.60E-03 350E-06 00% EMylbenzene 0000019 0.0003944 Valves 199 6.50E-03 250E-05 00% Xylenm 0000051 00010586 Other 98 880E-03 1.20E-06 0.0% MNsane 0002379 00493793 Connectors 0 750E-06 ]50106 0 VOC 1 0 Flanges 0 390E-0] 3.90607 0 Benzene 0 0 Open-Ended Linea 0 1.40E-04 7.20E-0K 0 Toluene 0 0 Heavy Oil Pump Seals 0 000E+0] 0.00E+00 0.0% Ellylbenzene 0 0 Valves 0 8.60E-06 8.40E-06 00% Xylenee 0 0 Other 0 320E-05 3.20E-05 0 0% n-Hesane 0 0 Cannanore 606 2.10E-06 7.50E-06 00% VOC 0.9979 3.9176647Flanged I8 1.10E-06 260E-06 0.0% Benzene 00123 00482888 Open-Ended Lines 6 1.60E-03 1.60E-05 00% Toluene 0.0287 01126733 Lgm 06 Pump Seals 0 1.30E-02 5.10E-06 0.0% Emymnzene 00056 0.0215924 Valves 78 250E-03 1.90E-05 0.0% X)lenee 00262 0.1028586 Other 10 )50E-03 1.10E-0I 00% n-Hesane 00637 0.2500798 Connectors 407 1.10E-06 1.00E-05 00% VOC 1 2973533 Flanges 18 2.50E-06 2.90E-06 00% Benzene 0.0012 00035584 Open-Ended Lines I 250E-04350E-06 0.0% Toluene 00003 00008921 WeuN011 Pump Seals 1 260E-05 340E-05 00% Eliylbencene 0.00009 2976E-05 Vales 50 980E-05 9.70EL6 00% Xylens 000.TM 0IXg1189 Other 18 1.40E-02 590E-05 00% n-Heaene 0.00001 2976E-05 Emlulone Summery Table Pollutant Uncontrolled Emissions controlled Emissions Source I VOC 12.2 iPY _IDY 12.2 Or EPA-463/R-95-017 Table 2-4 __ Benzene 1201o/tt 0.06 120 lb/yr EPA-453/9-95-017 Table 2-4 Toluene 2371CItt 0.12 237 10/yr EPA453IR-95-017 Table 2-4 ENylsnzene 44 lb/yr 002 44 lb/yr EPA-453/R-95017 Tali*2-4 ;Canes 2081s/y- 0.10 208 10/yr EPA-45YA-95017 Table 2-4 mlNaene 594 pow 0.30 5991Nyr EPA45108 017 Table 2-4 Regulatory Applicability The date of imams'or delemeningwhether Me source is new or nodrls4 is therefore November 20,2007 Ole date of the 8-hour ozone NA area designation).Since the ale was built after the date atone(operation Mean 11/4/2013).this Reg.3 source is considered Mew or modified'Opealor has agreed on Me Division's standard conditions. VOC end HAP ooncoanlene for gas senior am based on sales gas sample collected 12/12/2013 from Seventy Holes 7-P-HNB Since sirespecii end warn 1 year of application date,no initial sampling required. 14WE0625 CP1 123/9008 Two bw-pressure separators controlled by tar en dosed Bras.Eadi flare has a minimum combustica efficiency of 007 95%. Equipment Description Tate scums vats natural gas Born: a wet heed separator Emissions Born this slurp are: muted to a Ban 'Natural gas venting from a coal heed separator.Emissions from this source we routed to a flare. Calculations EPA Emission Inventory Improvement Program Publication:Veen II,Chapter 10-Displacement Equation(10.4-3) Erna'MW'Xx IC Ex•emissions or polutanl x 0•Volumetric flow rate/volume of gas processed MW•Molecular weight of gas•SO of gas•MW or air Xx•man fraction of in gas C•male volume of Ideal gas(379 sd/b-mol)at 60F and 1 arm Thaglra(O) 15.037416 MMsdr 1716.8 scOhr MW 37.9 mrl6md 0.0411984 MMed/d mole% MW baffler mess fraction btv Ibex re Helium 0.00 4.0028 0.000 0.000 0.00 000 0.00 CO2 2.07 44.01 0.911 0024 4.13 36145.62 18.07 . 312 0.27 29.013 0.078 0.002 0.34 300094 1.50 methane 22.79 18.041 3.658 0.088 16.59 145051.34 72.53 ethane 25.74 30.063 7.739 0.204 35.05 307058.81 153.53 propane 29.28 44.092 12.905 0.341 58.48 512147.62 258.07 iscOUWe 3.28 58.118 1.904 0.050 8.63 75558.16 37.78 webs 10.39 58118 8.040 0.150 27.36 23884297 119.82 Ieopreene 1.87 72114 1.348 0.038 610 53470.77 2074 Niemen, 2.31 72.114 1.688 0044 7.54 88088.82 33.04 cydoprarr 018 7013 0.125 0.003 057 4964.01 2.48 Mlssene 0.40 8818 0.348 0.00912 1.57 13718.34 6.88 cdohexare 0.10 84.16 0.081 - 0.002 0.37 - 3218.97 1.81 Other butanes 0.72 88.18 0.625 0.016 2.83 24779.85 12.39 hapMrea 024 10021 0.239 0.008 • 1.06 9488.71 4.74 tae 0.06 9810 0.058 0001 0.25 2218.73 1.11 224TMP 000 11423 0000 0.000 000 1613 0.01 Benzene 007 7812 0.058 000153 0.28 229875 1.15 Toluene 003 9215 0.028 000070 0.12 1045.87 _ 0.52 E60Enaene 000 108.17 011)2 0.00008 0.01 8848 0.04 Armes 0.01 104.17 0.000 0.00016 003 240.11 0.12 CB+Heavies 0.09 116 0.109 0.00287 0.49 4321.73 2.16 VOC mass frac 0.674 Total VOC(uncontrolled) 505.65 Mtn MOM%•MW,and mass fractions we based on sila•epecille 19 separator gas analysis colluded 12/12/2013 from Seventy Holes 4441-5HN8 and T-P-5HNI Emissions tea based on 8760 hours of operation per year. SceneTypically I calculate the average MW of C8+based n the average MW n the analysis for the gas.This ea s method mauled In minimal emissions increase Source used MW of 116 for C8+.Since there Is minimal 6Brence In emissions,I used the source's values. • 14W50525.CP1 1231908 Two low-pressure separators controlled by four enclosed flares.Each flare has a minimum combustion efficiency of 007 95%. Flaring Information Equipment Description Fare to combust produced gas until pi reline is available at this wellhead facility. Manufacturer Leed Model L30-0010 Serial Number 21451/21452/21453/21450 Gas Heating Value 21711Btu/sd Throughput 32646.23014 MMBIWyr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress gas to sales line. Make Model Requested Control 100.00% Annual Bypass Tim 0.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 jib NOX/MMBtu 0.37 jlb CO/MM0tu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 67385 Ib/MMsd 3369.27 lb/MMscf 506.7 tpy 25.3 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 1.1 tpy 1.1 tpy AP 42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 6.0 tpy 6.0 tpy AP-42 Benzene 152.736 lb/MMscf 7.6368 lb/MMscf 2297 lb/yr 115 lb/yr Gas Analysis n-Hexane 912.28 lb/MMsd 45.6140 lb/MMscf 13718 lb/yr 686 lb/yr Gas Analysis Toluene 89.538 lb/MMscf 3.4769 lb/MMscf 1046 lb/yr 52 lb/yr Gas Analysis %ylenes 15.968 lb/MMscf 0.7984 lb/MMscf 240 lb/yr 12 lb/yr Gas Analysis Ethylbenzene 5.8828 lb/MMscf 0.2941 lb/MMscf 88 lb/yr 4 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 Reoualion 2 Section LA apples 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.' 14WE0625.CP1 123/9008 One(1)pneumatic water transfer pump,rated at 800 sd/hr(Sandpiper, Model G1F,Serial number 2078873).The pneumatic pump Is controlled by 008 an enclosed flare with a minimum combustion efficiency of 95%. Pump Information Manufactur Sandpiper Model Number.G1F Serial Pump Number.2076873 IMornetIon Pump capacity 9.1 gallons per minute pumped natural gas 600 sd/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=0•MW•Xx/C Ex•emissions of pollutant x ' (lc 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 sof/lb-moll at 60F and 1 atm O eat scf/hr MW 22.7 lb/Ibmol Hound op. 8760 Imuahr Requested Throughput 5.256 MMscf/yr Component mole% MW man fraction Component lb/hr b/yr tpy CO2 2.24 44 0.0434 CO2 1.560 13668.374 6.834 nitrogen 0.58 28 0.0084 nitrogen 0.301 2640.481 1.320 methane 71.05813 16.04 0.5021 methane 18.044 158064.479 79.032 ethane 14.3658 30.07 0.1903 ethane 6.839 59911.421 29.956 propane 8.1104 44.09 0.1575 propane 5.661 49590.504 24.795 isobutane 0.6715 58.12 0.0172 isobutane 0.61$ 5412.374 2.706 n-butane 14020 58.12 0.0487 n-butane 1.751 15336.805 7.668 isopentane 0.2915 72.15 0.0093 isopentane 0.333 2916.695 - 1.458 n-pentane 0.3477 72.15 0.0111 n-pentane 0.397 3479.022 1.740 cyclopentane 0.0247 70.15 0.0008 cydopentane 0.027 240.293 0.120 n-hexane 6.0927 86.18 0.00238 n-hexane 0.086 749.359 0.375 cyclohexane 0.0157 84.18 0.0006 cyclohexane 0.021 183.284 0.092 Other hexanes 0.1113 86.18 0.0042 Other hexane 0.152 1330.203 0.665 heptanes 0.04034 100.21 0.0020 heptanes 0.074 644.830 0.322 methylcyclohexa 0.0111 98.19 0.0005 methylcyclohe 0.017 151.149 0.076 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 . Benzene 0.0111 78.11 0.00038 Benzene 0.014 120.239 0.060 Toluene 0.0067 92.14 0.00023 Toluene 0.008 72.835 0.036 Ethylbenzene 0.0004 106.17 0.00002 Ethylbenzene 0.001 5.889 0.003 Xylenes o.0011 106.17 0.00005 Xylenes 0.002 16.196 0.008 C8+Heavies 0.0205 116 0.0010 C8+Heavies 0.038 329.783 0.165 Mass Fraction VOC: 0.2560 Total VOC 40.291 Heating Value I 1315 BTU/sd I Contusive snanpn fader source: AP-42:Chaplet 13.5 0.07 I e nolrnaew 0.37 1sasses 14WE0625.CP1 123/9C08 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model GIF,Serial number 2076873).The pneumatic pump is controlled by 008 an enclosed flare with a minimum combustion efficiency of 95%. Mole M %,MW,and mass fractions are based on sales gas analysis collected 12/12/2013 ham Seventy Holes T-P-SHNB Emissions Summary Table Pollutant Uncontrolled Emission Fa(Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 15331.25 lb/MMscf 766.56 lb/MMscf 40.3 tpy 2.0 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.3 tpy 1.3 tpy AP-42 Benzene 22.8765 lb/MMscf 1.1438 lb/MMscf 120 lb/yr 6 lb/yr Gas Analysis n-Hexane 142.5722 lb/MMsd 7.1286 lb/MMscf 749 lb/yr 37 lb/yr Gas Analysis Toluene 13.8575 lb/MMscf 0.6929 lb/MMscf 73 lb/yr 4 lb/yr Gas Analysis Xylenes 3.0815 lb/MMscf 0.1541.lb/MMscf 16 lb/yr 1 lb/yr Gas Analysis Ethylbenzene 1.1205 lb/MMscf 0.0560 lb/MMscf 6 lb/yr 0 lb/yr Gas Analysis • 14WE0625.CP1 123/9[08 One emergency flare with a minimum combustion efficiency d 95%. The Sara is not endoead.The misogamy hie is 009 used during periods when the*Pane is not availbl. Equipment Deaadptlun This source vents natural gas Iran: sad heed separator%en the sales gas pipers*is not available or during emergencies Emissive Bon this saliva are: routed Wagon 'Natural gas venting from a sal heed separator elen the sales gas pipeline is not aveggie or dWrng emergendas.Emissions from this source are touted to Calculations ECOIIIIMIrdialillbglitiddIggi EPA Emission Inventory Inprovemeo Program Policed=Volme II,Chapter 10-Displacement Equation(10.4-3) Ex•0'MW•Xx/C Ex•emissions of polutant x 0•Volumetric Bow rate/volume of gas processed MW•Molecular weigM al gas•SG of gas'MW of sit )Cx•mass fraction ofx in gas C•molar volume of idyl gas(379 scfribineg M 80F and 1 man Thmplaq(Q) 13.8 MMairyr 1570.000 wily MW 227 bbmd 0.038 MMed/d mole% MW EMnt mess Br9en bar M/r ON Haman 0.01 4.0028 0.000 0.000 0.00 14.52 0.01 CO2 224 44.01 0.988 0.043 4.08 35773.71 1799 N2 em 28.013 0.190 0.008 0.79 8912.47 3.46 methane 71.06613 16.041 11.388 0.702 4722 413827.84 2)981 etape 14.3666 30.083 4.319 0.190 17.89 156731.72 78.37 propene .1104 44.002 3.578 0.158 14.81 129787.70 84.88 B0bulre 0.6715 56.118 0.380 0.017 1.82 14161.89 7.08 Madam in 58.116 1.106 0.049 4.58 40129.93 20.05 (accent* 02915 72.114 0.210 0.009 0.87 782821 381 NSW. 03477 72.114 0251 0211 1.04 909890 4.55 0100.077105.7 0.0247 70.13 0.017 0901 0.07 ' 82899 0.31 niWWe 03627 86.18 0.054 0.00238 022 198092 0.98 cwiohexae 0.0157 84.16 0.013 0.001 0.08 479.48 0.24 Other hexane 0.1113 86.18 0.096 0.004 0.40 3480.70 1.74 hapins 0.0464 10021 0.048 0.002 0.19 1087.30 0.64 istlryelddeure oam 96.19 0.011 0.000 0.05 395.51 0.20 224-7MP osal 11423 0.000 0.000 0.00 4.15 0.00 Berg sson 1812 0.009 0.00038 0.04 314.6/ 0.18 Toluene 0.4067 92.15 0.005 0.00023 0.02 190.61 0.10 Etlw6rme scoot 106.17 OM 0.00002 0.00 15.41 0.01 want 0.0011 106.17 0.001 0.00005 0.00 42.39 0.02 CB+Heavies 0.0205 118 0.024 0.001 0.10 877.81 0.44 VOC mess rive 0258 Total VOC(Uncontrolled) 105.43 Mat Mole Mole%,MW,and mass fractions are based on sales gas analysis seeded 12/122013 from Seventy Holes T-P-5HNB Emissions we based co 8780 hours of operation par yew. • Typically I calculate the avaegs MW of C8+based On the average MW on the analysis for the gas.This method mauled In mImel 653851003 increase Sours used MW of 115 for CB+.Since there is minimal difference in emissions,I used the source's vales. 14WE0925.CP1 123/9[00 One emergency flare with a minimum combustion efficiency of 95%. The flare is not encbsed.The emergency flare is 009 used during periods when the pipeline is not available. Flaring Information Equipment Description Flare to combust produced qas until pipeline is available at this wellhead facility. Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1315 Btu/scf Throughput 18147 MMBtu/yr VRU Information-NOT APPLICABLE Equipment Description Engine to recompress gas to sales line. Make Model Requested Control 100.00% Annual Bypass Tin- 0.00% Backup Flare Overall Control 95.00% Combustion emission factor source: 42:Chapter 13.5 0.07 Ilb NOX/MMBtu {AP-0.37 lb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 15280.00 lb/MMscf 764.00 ib/MMscf 105.4 tpy 5.3 tpy Gas Analysis Nor 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.6 tpy 0.6 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 3.4 tpy 3.4 tpy AP-42 Benzene 22.80 lb/MMscf 1.14 lb/MMscf 315 lb/yr 16 lb/yr Gas Analysis n-Hexane 142.09 lb/MMscf 7.10 lb/MMscf 1961 lb/yr 98 lb/yr Gas Analysis Toluene 13.81 lb/MMscf 0.69 lb/MMscf 191 lb/yr 10 lb/yr Gas Analysis Xylenes 3.07 lb/MMscf 0.15 lb/MMscf 42 lb/yr 2 lb/yr Gas Analysis Ethylbenzene 1.12 lb/MMscf 0.06 lb/MMscf 15 lb/yr 1 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 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.' 14WE0625.CP1 123/9008 II 2 a re ,,i2Mffi2M- MMIZOOg≥ r2o 002° 2° �LF-M2°z° acooe#eee* * eso0000000 0 0 0 0 0eooe efla tra (ay ygsggsgww msgS ow &Cbc“.4 Ig O1�0 Op CO 3 Om�rhpNp��O N O W I- CO �N�pp in rE(yp 0 W r0�m'Nr(OOO `� m t„, raN�NOIN r r I0 N • 0NO'-OON'OOJH I- y a m 0 b N N G QQ r O p O m P 8 N O N QO1 f` 0 O mO cad-- OOPNONOONr — nN N4.- —(O h�,- iN m— ' Co i.. (BaEg om gma^Pi rmg^N N N N N N N • g 3 3 3 3 3 3 Z IW f IW H H F • a N r n - h N O O ; ; ; ; ; ; .0_ m _muaw ILL33YYYYYY K K & KKKi, V, V V,tn 1, CZZmm2ZZ2ZZ • (8. 88888 m mmm m Q Q Q Q Q Q_ W W W N N LO N I0 1O C ac-I c-pa e0.sapsaasIIIIIIyYyaaaaas 0,a aIa0000O W W Q Q W W W W W L 0 0 0 Q Q Q Q Q Q 6 W W W W W W f7 Q Q(7 0 0 0 5 a . aaaaaaaaaaaaaaaa y(<TJ mBGU s 0' E§B§§§§ § § § §§§§§§§ IR9Ill'l Co amEpIpmamp��pOaOp��aaaaaaaaaaaaa aOpJEag .10dymomo7 N - N NOm^m-0. mo,e4 2 Na0 ON O OOOO (0000000 t75O 14FAilHlg C C 03 DLL 0 0 0 C CO E- 0 m. 7 C 0 0 0 Co m W m ° A =2 " a m g m c A' =.28.A @per c m ` 2 0 B New 300001555,x!0 m = Oa=m55,M00 0 = 055.00020=0£5. rr a >2 U m C I-W X N > m t >m t f W X N 1 m t f W X >z o m �1-W X ^0 0 a 2 W N N O N cm co ex o 0 0 0o 8 8 CO d a d nl M CC 0 6 0 (0 p Op p C O O S 0 O 0 a . 24 o o 2 d N > 2 } 2 )- 2 2 2 > 2 > > > 2 2 2 e e e e e e e e ° e \ \ \ \ 2 O O O 2 N 2 m N _ m o o m m m m m m m m m m U W • w m a '° m 'cr.) a e N N m o m u' O m n m o a - r n `o 'c w r a M m O w oa o r N N O CJ "g "82 NO t` f'J O N 2 [V O r tU M < o r J a'o 0 E a U K W C 9 N m 0 al N N . C o u E n O Q W C 0 V J O N a ✓ y �/f r/Nr/)� yN_ yN(� N N N SSII LL T T T T T T T T ›, T T T o m ccccccN N N N N N N N N N N N < N N Q < < Q < < N N < < < < Q E A d a m Nm Nm m m Nm a a m W m m Nm w O ¢ ¢ O O O O O O ¢ ¢ O O O O O DD > > U r r u U U u u u r r 3 U U U U C 003030000000003030000 9 M M 2 2 2 M 2 2 2 2 2 M M M y 22 M222222222222 2 2 E E E 2 E 2 2 2 2 . 3 3 3 3 3 3 3 3 3 3 a a a a a 2 in m r` r _ r m n n c7) b e� N n N g N n c, n N o O N N m N O p O• N T-- m r O a N woi r ` r M r N p ` m f r0 r r UpC N ,- Du_ C/3 a o 0c m_to it:O N O O 1 N C N N N mw- HE -110 . 2 K '8 , c go .x C d d N a m o00 0 y = o « 5,0 o m ? o t S a > z O O c r W X > Z O 0) o r W X fo �z m a_ E rn o -1 N N O 0 0 o o m m c7) X U Q 0 N it m O C O O O a Air Pollutant Emission Notice(APEN)—and—Application for Construction Permit OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY/.�� N. c, 'tr" Current Status(Check all that apply) Reason for APEN Submittal(Check all that apply) (o��' AIRS ID#r: 123/ q c 0 8 -c'O3 0 APEN update only / ® New or previously unreported battery 0 Modification to existing sources \ -'r~ aozi) ❑ Previously grandfathered battery 0 Registration for coverage under general permit no.GP c,;,-.,r,"'.:: / ' ❑ Synthetic minor facility &cancellation request for individual permits: O Located in the 8-hr Ozone Control Areas ® Application for or Modification of an individual permit ❑ Registered under general permit no.GP01 0 Administrative permit amendments ❑ Permitted under individual permit: 11-1 WE 0615 0 Other: For individual permit applications,check if you wants: 0 A copy of the preliminary analysis conducted by the Division 0 To review a draft of the permit prior to issuance Company Names: Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address1°: 410 17's Street,Suite 1500 City: Denver State: CO Zip: 80202 E-mail: pyomrg@BonanraCrk.com , Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name": Seventy Holes 44-5 Production Facility(COGCC#433304) Number of tankc: 6-500 bbl Location12(QQ Sec.Twp.Range.): SE/SE Sec 5,T4N,R62W County: Weld Total tank capacity[bbl]: 3,000 Calendar year for which"Actual"data applies 3: 2013 Year(s)tank(s)were placed in service1: 6-2013 Control Control Descriptions: Four(4)Leed L30-0010 48"SNs:21451,21452,21453,21450 Efficient 6: 95% Condensate Throughput"[bbl/year] Requested'°: 144,540 Maximum for PTE calculation19: 144,540 Actual3°: 120,450 While Controls Operational" 120,450 Other equipment at facilty22: Heater treaters,produced water tank natural gas-fired engines,pneumatic pump Comments: Estimated emissions at throughputs listed above. Use NM for requested throughput/emission values unless requesting an individual permit ❑Check if the Division is to calculate emissions. 0 Check if site-specific emission factors provided to calculate emissions23. Emission Factor Battery Requested Emissions'° Actual Emissions30 Pollutant" [Ib/bbl] PTE'PTE's Uncontrolled26 Controlled2s Uncontrolled26 Controlled2J VOC[tons/year] 1.79 129.03 129.03 6.45 107.53 5.38 I NOx[tons/year] 0.068 0.23 0.23 0.19 0.19 CO[tons/year] 0.37 1.23 1.23 1.04 1.04 Benzene[lbs/year] 0.021 3,021.6 3,021.6 151.1 2,518.0 / 125.9 n-Hexane[lbs/year] 0.122 17,594.4 17,594.4 879.7 14,662.0 ✓ 733.1 (NCRP Addendum Attached for Toluene) Wells serviced by this tank or tank battery° API#: 05-123-37855 Name: Seventy Holes 44-41-5HNB ®Newly Reported Well API#: 05-123-37579 Name: Seventy Holes T-P-5HNB 0 Newly Reported Well API#: Name: 0 Newly Reported Well API#: Name: 0 Newly Reported Well API#: Name 0 Newly Reported Well The signature below indicates that I have knowledge of the facts herein set forth and that the same are true,accurate,and complete to the best of my knowledge and belief. If this is a registration fo overage under general permit GP0I,I further certify that this source is and will be operated in full compli with ndi['on of gener 01. Signature o Legally Autho ' Person(not a vendor or consultant) Date David I.Lillo Vice President,Rocky Mm.Asset Mgmt. Type or Print Name of Person Signing Above Official Title Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-B1 9 O C5J O t_M (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South J j registration to: Denver,CO 80246-1530 FORM APCD-205 Page 1 oft FormAPCD-205-E&PCondensateTank - a o < O• % . . a O ` _ k 2 f ] k & 2 . , co , @ ; n D Q V �) 2 k \ 0 @ 0 0 § a. ) { i � k -0I k 0. 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