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Home My WebLink About20142835.tiff * coE COLORADO aa CO Department of Public .-• Health b Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150O St PO Box 758 Greeley, CO 80632 RECEIVED September 10, 2014 SEP 15 2014 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On September 13, 2014, the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company, LLC - State Antelope P-32 Production Facility, in the The Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health & Environment APCD-SS-B1 • 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, t. Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 2014-2835 ley. 1,,t . Q CL: el.( ?to, ,HI- /u bLo IFLNLQAAS 9 Its pF Cpl 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe ii.Ef <'* b' 9-22—Di John W. Hickenlooper,Governor I Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer I 1, o. CDPHE Public Notice Of A Proposed Project fln nip Or Activity Warranting Public CO Comment Website Title: Bonanza Creek Energy Operating Company, LLC - State Antelope P-32 Production Facility - Weld County Released To: The Greeley Tribune On: September 10, 2014 Published: September 13, 2014 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company, LLC Facility: State Antelope P-32 Production Facility Oil and gas exploration and production facility NENE Sec 32, T5N, R62W Weld County The proposed project or activity is as follows: The applicant proposes to operate an 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 14WE0195 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us ®N e.rmm O 0 COlORA0 1 I STATE OF COLORADO OF O DR.RAFP C HEALTH AND ENVIRONMENT R"- % AIR POLLUTION CONTROL DIVISION Nom%, TELEPHONE:(303)692-3150 '.�`�'. a1876i CONSTRUCTION PERMIT PERMIT NO: 14W E0195 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State Antelope P-32 Production Facility, located in the NENE Section 32, Township 5N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Six(6)above ground 500 bbl atmospheric condensate storage Condensate tanks. The condensate storage tanks are controlled by four Tanks 004 enclosed flares. Each flare has a minimum combustion efficiency of 95%. Truck 005 Truck Condensate Loadout Loadout FUG 006 Fugitive VOC equipment leaks One (1)pneumatic water transfer pump, rated at 600 scf/hr P-1 007 (Sandpiper, Model G1F, Serial number 2082470). The pneumatic pump is controlled by four enclosed flares. Each flare has a minimum combustion efficiency of 95%. HLP Sep-1, Two low-pressure separators controlled by a VRU and four HLP Sep-2 008 enclosed o flares. Each flare has a minimum combustion efficiency of 95%. Point 007: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario(AOS)in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: AIRS ID: 123/9BE4 Page 1 of 19 epa en ealth and Environment of Rr Pollution Control Division REQUIREMENTS TH T1ON 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to nation. The Notice of Startup form may be downloaded online at www.cdohe.state.co.us/ao/downloadforns.htmj. 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(180)days after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either,the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The DMsion 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. MRS Point 008: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. 5. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 6. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 7. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No.3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO, VOC CO Emission Type Condensate 004 1.9 Point Tanks Truck Loadout 005 22.0 Point FUG 006 13.1 Fugitive AIRS ID: 123/9BE4 Page 2 of 19 olor epa en P li ealth and Environment it Pollution Control Division P-1 07 .3 Point HLP Sep-1, 008 6.0 1.6 Point HLP Sep-2 See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) 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. 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. 9. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Control Device Pollutants Equipment ID Point Controlled Condensate 004 Enclosed Flare VOC Tanks P-1 007 Enclosed Flare VOC HLP Sep-1, 008 VRU and Enclosed Flare VOC HLP Sep-2 PROCESS LIMITATIONS AND RECORDS 10. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Process Parameter Annual Limit Equipment ID Point Condensate 004 Condensate Throughput 183,960 BBL Tanks Truck 005 Condensate Loaded 183,960 BBL Loadout P-1 007 Natural Gas Consumed 5.3 MMSCF HLP Sep-1, 008 Total Gas Vented from Both Low- 8.7 MMSCF AIRS ID: 123/9BE4 Page 3 of 19 pa e i ealth and Environment 'r Pollution Control Division HLP Sep-2 I u rs Compliance with the annual throughput limits shall be determined on a rolling twelve(12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility,for Division review. 11. AIRS Point 008: Upon installation of the flow meter required under Condition 4 the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from each low pressure separator using a flow meter.The flow meter shall continuously measure flowrate and record total volumetric flow vented from each 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 10 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. MRS Points 004, 005, 007 and 008: The permit number and AIRS ID point number (e.g. 123/4567/890)shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.)(State only enforceable) 13. Visible emissions shall not exceed twenty percent(20%)opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1.&4.) 14. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 15. 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.) 16. MRS Point 004: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 17. MRS Point 004: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 18. MRS Point 004: The condensate storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include,but are not limited to: XVII.C.1.a. Beginning May 1, 2008, owners or operators of all atmospheric condensate storage tanks with uncontrolled actual emissions of volatile organic compounds AIRS ID: 123/9BE4 Page 4 of 19 olor Depa en P li ealth and Environment it Pollution Control Division equal at n s ased rolling twelve-month total shall operate air pollution control equipment that has an average control efficiency of at least 95%for VOCs on such tanks. 19. AIRS Point 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. 20. AIRS Point 004: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98%for hydrocarbons. XVII.C.1.b.(i)(b) Control requirements of Section XVII.C.1.b. must be achieved by May 1, 2015. XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section XVII.C.1.b.(i), whichever comes later, owners or operators of storage tanks constructed before May 1, 2014 subject to Section XVII.C.1. must conduct audio, visual, olfactory("AVO") and additional visual inspections of the storage tank and any associated equipment (e.g. separator, air pollution control equipment, or other pressure reducing equipment) at the same frequency as liquids are loaded out from the storage tank. These inspections are not required more frequently than every seven (7) days but must be conducted at least every thirty one (31) days. Monitoring is not required for storage tanks or associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i) Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; XVII.C.1.d.(ii) Visual inspection or monitoring of the air pollution control equipment to ensure that it is operating, including that the pilot light is lit on combustion devices used as air pollution control equipment; AIRS ID: 123/9BE4 Page 5 of 19 olor epa en i eaith and Environment 'r Pollution Control Division XVII.C a , vi 'on 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 approved instrument monitoring method in accordance with the following schedule: XVII.C.2.b.(ii)(b) A storage tank constructed before May 1, 2014, must comply with the requirements of Sections XVII.C.2.a. and XVII.C.2.b. by May 1, AIRS ID: 123/9BE4 Page 6 of 19 epa en P li ealth and Environment it Pollution Control Division Dolor e ng 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. 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). AIRS ID: 123/96E4 Page 7 of 19 of epa en i ealth and Environment it Pollution Control Division XVII.C.3.e. TJJf ad •. ate . g, 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. 21. 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) 22. AIRS Point 005: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere induding, 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 dosed and latched at all times when loading operations are not active, except for periods of maintenance, gauging,or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 22 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 23. AIRS Point 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. 24. 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. 25. 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 II 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: 123193E4 Page 8 of 19 olor p P l it Pollution Control Division inspec stReFiL1eafthandEn*onment inwit 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 XVII.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: 123/9BE4 Page 9 of 19 d a eand Enve 'rI Pdlutionearth n vironmDivisionnt XVII.F.7. Rep p 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)0/II.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.B.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. 26. 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). This requirement to apply RACT shall be satisfied by installingfimplementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. AIRS ID: 123/9BE4 Page 10 of 19 epa en P li ealth and Environment it Pollution Control Division Dolor ow ' n ( will be performed on a semi-annual basis.The first AVO inspection must be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. Hi. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 27. AIRS Points 004, 006, 007 and 008: 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 28. AIRS Point 006: Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the AIRS ID: 123/9BE4 Page 11 of 19 of pa e i ealth and Environment 'r Pollution Control Division Division as ens pliance with emissions limits. 29. AIRS Point 008: The operator shall complete an initial site specific extended gas analysis of the natural gas vented from the low-pressure separator at this site in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4- trimethylpentane content (weight fraction) of this emission stream used in the permit application. Results of testing shall be used to determine site-specific emission factors using Division approved methods. Results of site-specific sampling and analysis shall be submitted to the Division as part of the self-certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. Periodic Testing Reauirementa 30. 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 31. AIRS Point 007: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section IV.A and without applying for a revision to this permit or obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. 32. AIRS Point 007: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer,model number, serial number and capacity of the replacement pump. 33. AIRS Point 007: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 34. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No.3, Part A, ll.C) a. Annually by April 301° 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: 123/9BE4 Page 12 of 19 olor epa en P li ealth and Environment it Pollution Control Division For a it If the.emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 35. Federal regulatory program requirements (i.e. PSD or NANSR) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 36. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 37. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final 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. 38. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 39. Unless specifically stated otherwise, the general and specific conditions contained in this permit have been determined by the APCD to be necessary to assure compliance with the provisions of Section 25-7-114.5(7)(a), C.R.S. 40. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the AIRS ID: 123/98E4 Page 13 of 19 ol pas i ealth and Environment 'r Pollution Control Division Air PollutionDi •' ( n et f the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the.Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 41. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice(APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued;the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 42. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions),-122(civil penalties),-122.1 (criminal penalties), C.R.S. By Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 12319BE4 Page 14 of 19 epa en P li ealth and Environment it Pollution Control Division Notes to Permit HolderDolor o e a . 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued.The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C°/02FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) Benzene 71432 567 Yes 28 n-Hexane 110543 3,869 Yes 193 Toluene 108883 415 Yes 21 004 Ethylbenzene 100414 25 No 1 Xylenes 1330207 93 No 5 2,2,4- 540841 186 No 9 trimethylpentane Benzene 71432 502 Yes 502 n-Hexane 110543 2,602 Yes 2,602 Toluene 108883 1,352 Yes 1,352 005 Ethylbenzene 100414 250 Yes 250 Xylenes 1330207 1,349 Yes 1,349 2,2,4- 540841 381 Yes 381 _ trimethylpentane Benzene 71432 132 No 132 n-Hexane 110543 669 Yes 669 006 Toluene 108883 270 Yes 270 Ethylbenzene 100414 48 No 48 AIRS ID: 123/9BE4 Page 15 of 19 or pa e i eatth and Environment 'r Pollution Control Division Xyl 252 Benzene 71432 274 Yes 14 n-Hexane 110543 1,591 Yes 80 007 Toluene 108883 208 No 10 Ethylbenzene 100414 25 No 1 Xylenes 1330207 78 No 4 Benzene 71432 1,536 Yes 38 n-Hexane 110543 9,624 Yes 241 008 Toluene 108883 1,217 Yes 30 Ethylbenzene 100414 132 No 3 Xylenes 1330207 382 Yes 10 5) The emission levels contained in this permit are based on the following emission factors: Point 004: Emission Factors Emission Factors Uncontrolled Controlled Pollutant Ib/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 0.4063 0.0203 Promax n-Hexane 0.0210 0.0011 Promax Benzene 0.0031 0.0002 Promax Toluene 0.0023 0.0001 Promax Ethylbenzene 0.0001 0.00001 Promax Xylenes 0.0005 0.00003 Promax Note: The controlled emissions for this point are based on the flare control efficiency of 95%.A HHV of 2,165 BTU/scf was used for combustion calculations. Point 005: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.2389 AP-42 Benzene 0.0027 AP-42 n-Hexane 0.0142 AP-42 Toluene 0.0074 AP-42 Ethylbenzene 0.0014 AP-42 Xylenes 0.0073 AP-42 2,2,4- 0.0021 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: AIRS ID: 123/9BE4 Page 16 of 19 R: 4PaFul P li ealth and Environment it Pollution Control Division L= 12. /T S=0.6(Submerged loading: dedicated normal service) P(true vapor pressure)=5.86 psia M (vapor molecular weight)=68 Ib/Ib-mol T(temperature of liquid loaded)=524 R The uncontrolled non-criteria reportable air pollutant(NCRP)emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 006: 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. 0.3 0 0.9973 1 fraction) Benzene Content(wt 0.000845 0 0.011415 0.0012 fraction) Toluene Content(Wt. 0.000643 0 0.030762 0.0003 fraction) Ethylbenzene (wt. 0.000077 0 0.005686 0.0001 fraction) Xylenes Content(wt. 0.00024 0 0.0307 0.0001 fraction) n-hexane Content(wt. 0.004907 0 0.059207 0.0001 fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors(kg/hr-component): Water/Oil Component Gas Service Heavy Oil Light Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R-95-017 Table 2-4 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent extended gas analysis. AIRS ID: 123/9BE4 Page 17 of 19 i - --- - - of pa en i earth and Environment r Pollution Control Division Point 007: Emission Emission Factors- Factors- Uncontrolled Controlled Pollutant Ib/MMscf vented IbiMMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (lb/MMBTU) VOC 18,502 925.11 Gas Analysis Benzene 52.142 2.6071 Gas Analysis n-Hexane 302.65 15.133 Gas Analysis Toluene 39.627 1.9814 Gas Analysis Ethylbenzene 4.7622 0.2381 Xylenes 14.847 0.7424 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 1,351 BTU/scf was used for combustion calculations. Point 008: Weight Emission Pollutant Fraction of Factors Source Gas(%) Uncontrolled Ib/MMscf NOx(lb/MMBTU) 0.068 AP-42 CO 0.37 AP-42 (lb/MMBTU) VOC 60.2 54,756 Gas Analysis Benzene 0.19 175.82 Gas Analysis Toluene 0.15 139.32 Gas Analysis Ethylbenzene 0.02 15.127 Gas Analysis Xylenes 0.05 43.701 Gas Analysis n-hexane 1.21 1,101.9 Gas Analysis Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 5/22/2014 of the gas vented from the low pressure separator at State Antelope P41-T44-30HNB (which is a different site)to estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow. Actual controlled VOC and HAP emissions shall be calculated based on actual VRU operating time, a control efficiency of 100%during VRU uptime,and a flare control efficiency of 95%during VRU downtime. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,956 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 AIRS ID: 123/9BE4 Page 18 of 19 r olor- Depa en . P .li ealth and Environment •it Pollution Control Division associated with thi or *u• .' eg !, •e --.+ecific - ', .tion date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC NANSR Synthetic Minor Source of: VOC MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.q poaccess.oov/ Part 60:Standards of Performance for New Stationary Sources NSPS 60.1-End SubpartA—SubpartKKKK 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 SubpartA—SubpartZ MACT 63.600-63.1199 Subpart M—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QOQ—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.nov/pacific/cdphe/air-permit-self-certification. AIRS ID: 123/9BE4 Page 19 of 19 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 06/05/2014 Application Date: 12/23/2013 Facility Identifiers Permit No. 14W E0195 AIRS County# 123 Weld Facility# 9BE4 Facility Type: exploration and production facility I]Located in the 8-hour non-attainment area? 0 True Minor O Synthetic Minor for: I✓ VOC r NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Antelope P-32 Source Location: NENE Section 32,Township 5N,Range 62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street,Suite 1500 Address :ity,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoune@bonanzacrk.com 'Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Antelope P-32,located in the NENE Section 32, Township 5N,Range 62W,Weld County,Colorado. Point Name Type Control Action Newly Condensate 004 Tanks Condensate Tanks Flare reported source Newly 005 TL Loadout None reported source Newly 006 FUG Fugitives None reported source Newly 007 P-1 Pump Flare reported source HLP Sep-1, Newly Also 008 HLP Sep-2 Separator Venting Flare reported controlled source by VRU 004 Six(6)500 bbl above ground atmospheric condensate storage tanks controlled by four enclos Requsted Throughput 183960 bbl Control Flare Efficiency 95.00%} Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.4063 lb/bbl 37.4 tpy 1.9 tpy Promax Benzene 0.0031 lb/bbl 567 lb/yr 28 lb/yr Promax n-Hexane 0.0210 lb/bbl 3869 lb/yr 193 lb/yr Promax Toluene 0.0023 lb/bbl 415 lb/yr 21 lb/yr Promax Ethylbenze 0.0001 lb/bbi 25 lb/yr 1 lb/yr Promax Xylenes 0.0005 lb/bbl 93 lb/yr 5 lb/yr Promax 2,2,4-TMP 0.0010 Ib/bbl 186 lb/yr 9 lb/yr Promax Nox 0.068 lb/Mmbtu 0.05 tpy 0.05 tpy AP-42 Table 1 CO 0.37 lb/Mmbtu 0.26 tpy 0.26 tpy AP-42 Table 1 Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below,no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20%opacity.This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes.The approved reference test method for visible emissions measurement is EPA Method 9(40 CFR, Part 60, Appendix A(July, 1992))in all subsections of Section II.A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. —'Odor Section IA-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. Standard -.:-. . .. NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. The 500 bbl tanks are above the minimum capacity threshold of—471 bbl.However,the tanks are located at the wellhead site,store condensate,and are prior to custody transfer,thus,the tanks are exempt from NSPS Kb (60.110b(d)(4)). NSPS 0000:for storage vessels in the natural gas production,transmission,and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. uIation7"r . 14WE0195.CP1 123/9BE4 004 Six(6)500 bbl above ground atmospheric condensate storage tanks controlled by four enclos XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS Applicant is subject to the emission control requirements for condensate tanks since it is located in the nonattainment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is currently subject to this since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions are greater than 6 tpy. 14WE0195.CP1 123/99E4 005 Truck Condensate Loadout Calculations L=12.46•S•P•M/T(AP-42:Chapter 5.2,Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 5.86 psia Sales Oil Analysis documenting RVP 8 and AP-42 M Molecular Weight of VaF 68 lb/lb-mole Sales oil analysis for RVP 8 and values from AP-4 T Liquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver,CO L 5.69 lb/10"3 gal 2.39E-01 lb/bbl Annual requested Throughput 183960 BBL/yr 7726320 gal/yr Annual requested VOC emissions 43953 lb/yr 21.98 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0114 n-hexane 0.0592 Toluene 0.0308 Xylenes 0.0307 Ethylbenzeni 0.0057 2,2,4-TMP 0.0087 Source: Pressurized oil analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2389 lb/bbl 21.98 tpy 22.0 tpy AP-42 Benzene 0.0027 lb/bbl 501.73 lb/yr 501.73 lb/yr AP-42 n-Hexane 0.0141 lb/bbl 2602.34 lb/yr 2602.34 lb/yr AP-42 Toluene 0.0073 lb/bbl 1352.09 lb/yr 1352.09 lb/yr AP-42 Xylenes 0.0073 lb/bbl 1349.36 lb/yr 1349.36 lb/yr AP-42 Ethylbenzeni 0.0014 lb/bbl 249.92 lb/yr 249.92 lb/yr AP-43 2,2,4-TMP 0.0021 lb/bbl 381.47 lb/yr 381.47 lb/yr AP-44 Regulatory Review r,i VolatileoritacieCornaouru(s_ This facility is not considered a bulk plant(in Reg.7)because It does not distribute gasoline. 14WE0195.CP1 123/9BE4 006 Fugitive equipment leaks Regulation 7 Information Operating Hours' 8760 nounlyear Emission Factor Source EPA-4531R-95-017 Table 2-4 Control Efficiency Source' None Calculations Emission Factor Ikglnr- Emissions Service Component Type Countsource) Control(%)Pollutant Mass Fraction (tpy) Table 2-4 Table 2-0 Rsg.3 Connectors 1384 2.03E-04 300E-05 00% VOC 03 62268988 Flanges 66 890E-04 906.06 00% Benzene 0.000845 0.0175391 Open-Ended Lines 42 300E-03 1506.05 0.0% Toluene 0.000643 00133463 Gas Pump Seals 4 340E-03 350E-04 00% Elh5benzene 0.000077 0.0015982 Valves 199 159E-03 250E-05 0.0% %ylenes 000024 00049815 other 98 8.80E-03 1.20E-04 00% n-Hesane 0.004907 0.1018513 Connectors 0 J60E-06 7.506.06 0 VOL 0 Flanges 0 3.90E-07 3.90E-07 0.0% Benzene 0 open£nded Lines 0 1.40E-04 7.20E-06 0.0% Toluene 0 Heavy Cl Pump Seals 0 0.005s00 000E+00 0 Elnsbenzene 0 Valves 0 8.40E-06 8.40E-06 0 0% Xylenes 0 Other 0 320E-05 320E-05 0.0% n-Hexane 0 Connectors 606 2.10E-04 750E-06 0 VOC 0.9973 3.9152992 Flanges 16 1.10E-04 240E-06 0 Benzene 0.011415 0.0448141 Open-Ended Linea 6 1.40E-03 140E-05 0 Toluene 0.030762 0.1207685 Light Oil Pump Seals 0 130Em s.10E04 0.0% Emylbenzene 0.005686 00223227 Valves 78 ?50E-03 1.90E-05 0.0% Xylenes 0.0307 0.1205251 Other 10 750E-03 110E-04 0.0% n-Hassan 0059207 0.2324407 Connectors 467 1.10E04 1.00E-05 0.0% VOC 1 2.913633 Flanges 18 2.90E-06 390E-06 0 Benzene 00912 0.0035684 open-Ended Lines 1 2.60E-04 3.60E-06 0.0% Toluene 0.0003 00008921 Water/Oil Pump Seals 1 2.406.05 240E-05 0 Elhybenzene 00001 0.0002974 Valves 50 980E-05 9.70E-06 0 Xylenes 0.0001 0.0002974 Other 18 1.40E-02 5.90E-05 0.0% n-Hexane 0.0001 0.0002974 Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source Ipy VOC 13.12Ipy 13.121py EPA-453/F1-95-017 Table 2-4 Benzene 13184 lb/yr 13104 lb/yr EPA-453/13-95-017 Table 2-4 0.07 Toluene 270.01 lb/yr 270.01 lb/yr EPA-453//14-95-017 Table 2-4 0.14 Elhvlbenzene 49.44lb/yr 48.44 lb/yr EPA-453/R-95-017 Table 2-4 0.02 %Hens 251.61 lb/yr 25161 lb/yr EPA-453/R-65-017 Table 2-4 0.13 n-Hnsane 669.10 lb/yr 689.16 lb/yr EPA-453/R-95017 Table 24 033 Regulatory Applicability The dale of interest for determining whether the source is new or modified is therefore November 20.2007(the dale of the 880ur ozone NA area designation).Since the site was built after the dale above(operation began 9126/20131 Inis Reg.3 source is considered'new or muddied:Operator has agreed on the Divisions standard conditions. VOL and HAP concentrations for gas service are based on sales gas sample collected 1114/2013 from Slate Anlelop U- Y-32HNB.Since site-specific and Within 1 year of application dab.nO initial sampling required. • 14WE0395CP1 123/9604 14WE0195.CP1 123198E4 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model G1F,Serial number 2082470).The pneumatic pump is controlled by 007 an enclosed flare with a minimum combustion efficiency of 95%. Pump Informatlon Manufactur Sandpiper Model Number:G1F Serial Pump Number:2082470 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control Flare 95.00%Efficiency Calculations EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q!MW"Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas"MW of air Xx=mass fraction of x In gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Q 606 scf/hr MW 23.41b/Ib-mcl Hours of Op. 8760 houratr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy CO2 2.15 44 0.0404 CO2 1.498 13119.198 6.560 nitrogen 0.75 28 0.0090 nitrogen 0.332 2912.296 1.456 methane 71.04537 16.04 0.4870 methane 18.041 158036.095 79.018 ethane 12.6491 30.07 0.1625 ethane 6.022 52748.389 26.374 propane 82395 44.09 0.1552 propane 5.751 50379.877 25.190 isobutane 0.8224 58.12 0.0204 isobutane 0.757 6628.646 3.314 n-butane 236 58.12 0.0636 n-butane 2.355 20633.919 10.317 isopentane 0.4861 72.15 0.0144 isopentane 0.532 4663.711 2.332 n-pentane 0.5921 72.15 0.0183 n-pentane 0.676 5924.443 2.962 cyclopentane 0.0489 70.15 0.0015 cyclopentane 0.054 475.721 0.238 n-hexane o.1p31. 86.18 0.0049 n-hexane 0.182 1590.745 0.795 cyclohexane 00366 84.18 0.0013 cyclohexane 0.049 427.274 0.214 Other hexanes 0.268 86.18 0.0083 Other hexane 0.309 2708.211 1.354 heptanes 0.1i73 100.21 0.0050 heptanes 0.186 1630.141 0.815 methylcyclohexa 0.0293 98.19 0.0012 methylcyclohe 0.046 398.980 0.199 ' 224-IMP 0.0001 114.22 0.0000224-1MP 0.000 1.584 0.001 Benzene 0.0253 78.11 0.0008 Benzene 0.031 274.059 0.137 Toluene 0.0163 92.14 0.0006 Toluene 0.024 208.282 0.104 . Ethylbenzene 0.0017 106.17 0.0001 Ethylbenzene 0.003 25.030 0.013 Xylenes 0.0053 106.17 0.0002 Xylenes 0.009 78.036 0.039 C8+Heavies 0.0745 116 0.0037 C8+Heavies 0.137 1198.479 0.599 Mass Fraction VOC: 0.2997 Total VOC 48.624 Heating Value I 1351 BTU/scf Cm4ustbn embsbn facia source: AP-42:Chapter 13.5 14WE0195.CP1 123/96E4 One(1)pneumatic water transfer pump,rated at 600 scf/hr(Sandpiper, Model Cl F,Serial number 2082470).The pneumatic pump is controlled by 007 an enclosed flare with a minimum combustion efficiency of 95%. 0.07 lb NOX4MMBtu 0.37 lb OO/MMBtu Notes Mole%.MW,and mass fractions from: sales gas analysis collected 11)4/2013 at Slate Antelope u-V-32HN8 Typically I would use the calculated MW for C8+which resulted in 0.02 tpy more.Source used 116 for MW for CB+,Since minimal difference in emssions,I used source's values Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18502.12 lb/MMscf 925.11 lb/MMscf 48.62 tpy 2.4 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.24 Spy 0.24 tpy AP-42 CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 1.31 tpy 1.31 tpy AP-42 Benzene 52.142 lb/MMscf 2.6071 Ib/MMscf 274.06 lb/yr 13.70 lb/yr Gas Analysis n-Hexane 302.65 lb/MMscf 15.1327 lb/MMscf 1590.75 lb/yr 79.54 lb/yr Gas Analysis Toluene 39.627 lb/MMscf 1.9814 lb/MMscf 208.28 lb/yr 10.41 lb/yr Gas Analysis Xylenes 14.847 lb/MMscf 0.7423 lb/MMscf 78.04 lb/yr 3.90 lb/yr Gas Analysis Ethylbenzene 4.7622 lb/MMscf 0.2381 lb/MMscf 25.03 lb/yr 1.25 lb/yr Gas Analysis Two low-pressure separators averaged by a VRU and four enclosed flares.Each flare has a minimum 008 combustion efficiency of 95%. Equipment Description This source vents natural gas from: a wel head separator Emissions from this source are: recampressed Natural gas venting from a wel head separator.Emissions from this source am recampressed. Calculations Emsson Celcrlation MBIMd EPA Emission Inventory Improvement Program Pubication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=0•MW•Xx/C Ex=emissions of polutant x Cr=Volumetric flow rate/volme of gas processed MW=Molecular weight of gas=SG of gas BMW of ea Xx=mass fraction of x in gas C=molar voMme of ideal gas(379 scOb-md)at 60F end 1 atm Throughput(0) 8.73372 MMscfryr 997 scftx MW 34.5 IMbmd 0.023928 MM d/d mole% MW twbnnd mass fraction Ilea lbyr ipy Helium 0.0000 4.0028 0.000 0.000 0.00 0.00 0.00 CO2 2.5400 44.01 1.118 0.032 2.94 25759.96 12.88 • N2 0.1300 28.013 0.036 0.001 0.10 839.20 0.42 methane 35.8815 18.041 5.720 - 0.188 15.05 131822.97 65.91 ethane 229547 30.083 6.901 0.200 15.15 159024.48 79.51 propane 21.8688 44.092 9.642 0.279 25.37 222200.38 111.10 eobtae 2.5592 58.118 1.487 0.043 3.91 34274.80 17.14 n4xdne 8.1075 58.118 4.712 0.137 1240 108581.96 54.29 egente a 1.5941 72.114 1.150 0.033 3.02 28490.81 13.25 n-pentane 2.0828 72.114 1.502 0.044 3.95 34808.72 17.30 cydopertlere - 0.1462 70.19 0.103 0.003 027 2362.71 1.18 n-Hexene 0.4846 86.18 0.418 0.0121 1.10 9823.87 4.81 43ddmhere 0.1279 84.16 0.108 0.003 028 2480.48 1.24 Other hexares 0.7998 86.18 0.699 0.020 1.81 15883.58 7.94 hepenes 0.4105 100.21 0.411 0.012 1.08 9479.47 4.74 msdebddexane 0.1035 98.19 0.102 0.003 0.27 2341.90 1.17 224-DAP 0.0002 114.23 0.000 0.0000 0.00 5.26 0.00 Berne 0.0853 78.12 0.087 0.0019 0.18 1535.58 0.77 Toluene 0.0573 92.15 0.053 0.0015 0.14 1216.77 0.61 Eerylbenrene 0.0054 106.17 0.006 0.0002 0.02 132.12 0.07 Xyeies 0.0156 108.17 0.017 0.0005 0.04 381.67 0.19 C8+Heavies 02521 114 0.287 0.0063 0.76 8822.74 3.31 VOC mass Sec 0.602 Total VOC(Uncontrolled) 239.11 34.528 MEt4€ Mole%,MW,and mass fractions are based an LP separator gas analysis collected 5/22/2014 from State Antelope P41-74430HN8(rot cite-spedBc so will Emissions are based on 8760 hours of operation per year. Typicay I calculate the average MW of Cif+based on the average MW on the analysis for the gas.This method resulted In minimal emissions increase Source used MW of 114 for CB+.Since them is minimal difference In emissions,I used the source's values. • 14WE0195.CP1 123/98(4 Two low-pressure separators controlled by a VRU and four enclosed flares.Each flare has a minimum 008 combustion efficiency of 95%. Flaring Information Equipment Description Flare to combust LP separator gas during VRU downtime. Manufacturer Leed Model L30-0010 48" Serial Number 21432.21425.21424,21431 Gas Heating Value 1956 Btu/scf Throughput 8541.57816 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ230 Requested Control 100.00% Annual Bypass Tim 50.00% Backup Flare [Overall Control I 97.50%l Combustion emission factor source: AP-42:Chapter 13.5 0.07 jib NOX/MMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 54755.91 lb/MMscf 1368.90 lb/MMscf 239.11 tpy 5.98 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 0.29 tiN 0.29 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.58 WY 1.58 tpy AP-42 Benzene 175.82 lb/MMscf 4.401b/MMscf 1535.58 lb/Yr 38.39 lb/yr Gas Analysis n-Hexane 1101.92 lb/MMscf 27.5516/MMscf 9623.87 lb/Yr 240.60 lb/yr Gas Analysis Toluene 139.32 lb/MMscf 3.48 lb/MMscf 1216.77 lb/yr 30.42 lb/yr Gas Analysis Xylenes 43.70 lb/MMscf 1.09 lb/MMscf 381.67 lb/yr 9.54 lb/yr Gas Analysis EthVlbenzene 15.13 lb/MMscf 0.38 lb/MMscf 132.12 lb/yr 3.30 lb/yr Gas Analysis Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section 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" 14WE0195.CP1 123/96E4 m ii mre zmo yg000 rggloo0ggliYgEEggggoggolgg0000 ru 0 8 0 0 8 8 m m 8 8 0 0 0 0 0 0 0 0 0 0 0 0 0 8 0 0 8 8 m m m o W �p m �p p �m Iom pp cgs y m a tm+l O O N A V N W m N Sj N Cf N O ^ ,- (O N a N V O,-N Iwo N N r W r p a p p pp p m 1• m a o N' N O! N N c4 - 8N _ - -- I cn wo N Y 0, c40- 0. 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Air Pollutant Emission Notice (APEN)—and—Application for Construction Permit OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY Current Status(Check all that apply) Reason for APEN Submittal(Check all that apply) AIRS ID#1: 123/9BE4/ Dog ❑ APEN update only' ® New or previously unreported battery 0 Modification to existing sources ❑ Previously grandfathered battery 0 Registration for coverage under general permit no.GPO] ❑ Synthetic minor facility &cancellation request for individual permits: ® Located in the 8-hr Ozone Control Areas 0 Application for or Modification of an individual permit O Registered under general permit no.GP01 iu WED[qc ❑ Administrative permit amendment' O Permitted under individual permit: I 1 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 Name9: Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address": 41017`"Street,Suite 1500 City: Denver State: CO Zip: 80202 E-mail: pyoung@BonmzaCrk.com Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name'1: State Antelope P-32 Production Facility(COGCC#432677) Number of tanks: 6-500 bbl Location'2(QQ Sec.Twp.Range.): NE/NE Sec 32,T5N,R62W County: Weld Total tank capacity[bbl]: 3000 Calendar year for which"Actual"data applies": 2013 Year(s)tank(s)were placed in service": 2013 Control Description's: Four(4)Leed L30-0010 48"SNs:21432,21425,21424,21431 Control Efficiency": 95% Condensate Throughput"[bbl/year] Requested": N/A Maximum for PTE calculation": 183,960 Actual20: 153,300 While Controls Operational' 153,300 Other equipment at facihty23: Heater treaters,produced water tanks, pneumatic pump,engines,flare,high/low pressure separators. Comments: 2 year update to SSEF not required. Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit ❑Check if the Division is to calculate emissions. 0 Check if site-specific emission factors provided to calculate emissions". Emission Factor Battery Requested Emissions" Actual Emissions20 Pollutant" [lb/bbl] PTE" Uncontrolled26 Controlled" Uncontrolled�6 Controlled" VOC[tons/year] 0.41 37.37 37.37 1.87 31.14 1.56 NOx[tons/year] 0.05 0.04 CO[tons/year] 0.25 0.22 Benzene[lbs/year] 0.003 567.1 567.1 28.4 472.6 23.6 n-Hexane[lbs/year] 0.021 3,868.5 3,868.5 193.4 3,223.8 161.2 Wells serviced by this tank or tank battery's API#: 05-123-37267 Name: State Antelope P-T-32HNB _ ®Newly Reported Well API#: 05-123-37227 Name: State Antelope U-Y-321-INB 0 Newly Reported Well API#: Name: - - 0 Newly Reported Well API#: Name: - 0 Newly Reported Well API#: Name - ❑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 f verage under general permit GP0I,I further certify that this source is and will be operated in full com i ce with each conditi n of gen P01. / 2-1 a- /3 ' Si re of Legally Autho ' Person(not a vendor or consultant) Date David J.Lillo Vice President,Rocky Mt.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 filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-B 1 303211 (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South registration to: Denver,CO 80246-1530 FORM APCD-205 Page 1 of 2 FormAPCD-205-E&PCondensateTankAPEN.docx i g u` 0 0 0 0 0 `o E •-��\o E O �2 3r .� .� a aC er 0. O I w T G "G O "c "C a {�I] CO y _ M NCI ... 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