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Home My WebLink About20152159.tiff A CDPHE COLORADO CO1O Department of Public Y Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado RECEIVED Weld County - Clerk to the Board 1150 O St JUL ra PO Box 758 l v�J Greeley, CO 80632 WELD COUNTY C0MMISSI0' NERS July 15, 2015 Dear Sir or Madam: On July 22, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company LLC - North Platte A-33 Production Facility. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, 1 Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure �1 7 2015-2159 -2e2- aO( CC =P�->�W; fit. �20 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickenlooper, Governor Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer ,;. ,, C©PHE Air Pollution Control Division co Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company LLC - North Platte A-33 Production Facility - Weld County Notice Period Begins: July 22, 2015 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company LLC Facility: North Platte A-33 Production Facility Oil and Gas Exploration and Production Facility NWNW SEC 33 R5N R63W Weld County The proposed project or activity is as follows: Applicant proposes the construction of an exploration and production facility with all associated equipment The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 15WE0418 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: Christopher Kester Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us s0�tn COIC%R ACsO 1 I .... .. STATE OF COLORADO of co LORAD D P T F P BLit HEALTH AND ENVIRONMENT to� AIR POLLUTION CONTROL DIVISION it-7 0 TELEPHONE: (303) 692-3150 #' *1876* CONSTRUCTION PERMIT PERMIT NO: 15WE0418 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the North Platte A-33 Production Facility, located in the NWNW SEC 33 T5N R63W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID One vapor recovery tower (VRT) controlled by six (6) enclosed VRT-1 006 flares during gas compressor downtime. The enclosed flares have a minimum destruction efficiency of 95%. Six (6) low-pressure separators controlled by six (6) enclosed SEP-1 007 flares during gas compressor downtime. The enclosed flares have a minimum destruction efficiency of 95%. One open flare to control sales gas in case of an emergency. The OFL 2 008 open flare has a minimum destruction efficiency of 95%. Two (2) 750 bbl produced water tanks. Emissions from the water PW 010 tanks are routed to six (6) enclosed combustors that achieve a minimum VOC destruction efficiency of 95% Eight (8) 750 bbl atmospheric condensate storage tank. Emissions CNDTK-1 011 from the water tanks are routed to six (6) enclosed combustors that achieve a minimum VOC destruction efficiency of 95% TLO 012 Hydrocarbon Loadout to Tanker Trucks 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: 12319D43 Page 1 of 14 olor Depa en f P •li Health and Environment Ak A it Pollution Control Division REQUIREMENTS - • I 7.. ' TH.�``' `TION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation or issuance of this permit, whichever comes later, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) after commencement of operation or issuance of this permit, whichever comes later, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 4. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 5. Points 006, 007, 009, 010, 011, and 012: Within one hundred and eighty days (180) after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flow rate of natural gas flared from all high and low pressure separators, the VRT, tanks, and loadout activity. 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. 6. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 7. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) AIRS ID: 12319D43 Page 2 of 14 rri , , ,,,,,,,,:„ molora 3 DeparnenJf P Iic4Health and Environment ki A it Pollution Control Division ` Annual Limits11,4 Facility AIRS Tons per Year Emission Type X Equipment ID Point NO VOC CO VRT-1 006 0.3 7.2 1.4 Point SEP-1 007 0.8 17.9 4.2 Point FL-2 008 0.5 3.7 2.5 Point PW 010 --- 2.7 --- Point CNDTK-1 011 0.2 4.3 0.9 Point TLO 012 0.1 10.0 0.3 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 8. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit (Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID VRT-1 006 Six(6) Enclosed Flares VOC SEP-1 007 Six (6) Enclosed Flares VOC FL-2 008 Emergency Open Flare VOC PW 010 Six(6) Enclosed Flares VOC CNDTK-1 011 Six(6) Enclosed Flares VOC TLO 012 Six (6) Enclosed Flares VOC AIRS ID: 123/9D43 Page 3 of 14 il • olor- Depa en . •Ii Health" and Environment 0 •it Pollution Control Division A PROCESS LIMITA a, § A N• •a✓ 9. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Equipment Point Process Parameter Annual Limit ID VRT-1 006 Gas Flared from Separator 2.6 MMSCF SEP-1 007 Gas Flared from Separator 10.5 MMSCF FL-2 008 Gas Flared from Separator 10.0 MMSCF PW 010 Produced Water Throughput 411,720 BBL CNDTK-1 011 Condensate Throughput 398,580 BBL TLO 012 Condensate Loaded 398,580 BBL Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 10. Points 006 and 007: The owner or operator shall continuously monitor and record the volumetric flow rate of natural gas flared from the separator(s) using a flow meter. The flow meter shall continuously measure flow rate and record total volumetric flow flared from each separator. The owner or operator shall use monthly throughput records along with the methodology in the Operating and Maintenance Plan for these points to demonstrate compliance with the process limits specified above and to calculate emissions as described in this permit. 11. Point 008: The owner or operator shall continuously monitor and record the volumetric flow rate of natural gas flared from the separator(s) using a flow meter. The flow meter shall continuously measure flow rate and record total volumetric flow flared from each separator. The owner or operator shall use monthly throughput records to demonstrate compliance with the process limits specified above and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. The permit number and AIRS ID number shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 13. These sources are subject to the odor requirements of Regulation No. 2. (State only enforceable) 14. Point 011: 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 AIRS ID: 123/9D43 Page 4 of 14 I olorDepa en P li Health and Environment it Pollution Control Division • operator shallJ;- wi • vz ile nts Lion XII including but not limited to the monitoring, reporting and emission control requirements of Regulation 7, Section XII. 15. Point 006, 007, 010, 011, and 012: The flares covered by this permit are subject to Regulation No. 7, Section XVII.B.2. General Provisions (State only enforceable). 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. This flare must be equipped with an operational auto-igniter according to the following schedule: o If the combustion device was installed on/after May 1, 2014, upon installation of the combustion device; 16. Points 010 and 011: The storage tanks covered by this permit are subject to the emission control requirements in Regulation No. 7, Section XVII.C.1.a. The owner/operator must install and operate air pollution control equipment that achieves an average control efficiency of 95% for VOC's. The source shall follow the inspection requirements of Regulation No. 7, Section XVII.C.1.d. and maintain records of the inspections for a period of two years, made available to the Division upon request. 17. Points 010 and 011: The storage tanks covered by this permit are subject to the emission control requirements in Regulation No. 7, Section XVII.C.1.b. The owner/operator must install and 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. The source shall follow the inspection requirements of Regulation No. 7, Section XVII.C.1.d. and maintain records of the inspections for a period of two years, made available to the Division upon request. This control must be achieved according to the following schedule: o If storage tank was constructed on/after May 1, 2014, within 90 days of the date that the storage tank commences operation; 18. Points 010 and 011: The storage tanks covered by this permit are subject to the venting and Storage Tank Emission Management System ("STEM") requirements of Regulation No. 7, Section XVII.C.2. This storage tank shall be operated 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. The owner/operator must develop, certify, and implement a documented STEM plan to identify, evaluate, and employ appropriate control technologies, monitoring practices, operational practices, and/or other strategies designed to meet these requirements. Compliance is required on the following schedule: o A storage tank constructed on/after May 1, 2014 must comply and implement a STEM Plan within 90 days of the storage tank commencing operation; o A storage tank constructed before May 1, 2014, must comply and implement a STEM Plan 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 AIRS ID: 123/9D43 Page 5 of 14 olor. .Depa en . P ell Health and Environment 1 A it Pollution Control Division thirty ( for . -. " , ,. r - '--trolle• al VOC emissions greater than 50 tons per year. 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 ("AIMM") Schedule Emissions (tpy) Inspection Frequency >6 and < 12 Annually January 1, 2016 > 12 and < 50 Quarterly July 1, 2015 > 50 Monthly January 1, 2015 The owner/operator shall maintain records in accordance with Regulation No. 7, Section XVII.C.3. and make them available to the Division upon request. The owner or operator shall maintain records of STEM, including the plan, any updates, and the certification, for the life of the storage tank. The owner/operator will maintain records of all required inspections and monitoring for a period of two years. 19. Points 006, 007, and 008: The separator covered by this permit is subject to Regulation 7, Section XVII.G. (State Only). On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. 20. Point 008: The open flare covered by this permit has been approved as an alternative emissions control device under Regulation No. 7, Section XVII.B.2.e. The open flare shall have no visible emissions during normal operations and be designed so that an observer can, by means of visual observation from the outside of the open flare, or by other convenient means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XVII. This flare must be equipped with an operational auto-igniter according to the following schedule: o If the combustion device was installed on/after May 1, 2014, upon installation of the combustion device; 21. Point 012: 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) AIRS ID: 123/9D43 Page 6 of 14 I (iIoloriDepLerrs f P li Health and Environment it Pollution Control Division 22. Point 012: Tilt wr • X e all ading edures 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 onsite at the time of inspections to monitor compliance with above conditions. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 23. Point 012: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. OPERATING & MAINTENANCE REQUIREMENTS 24. Points 006, 007, 008, 010, 011, and 012: 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 25. Points 006, 007, 010, 011, and 012: The owner or operator shall demonstrate compliance with opacity standards, using EPA Method 22 to determine the presence or absence of visible emissions. "Visible Emissions" means observations of smoke for any period or periods of duration greater than or equal to one (1) minute in any fifteen (15) minute period during normal operation. (Reference: Regulation No. 7 Section XVII.All) 26. Point 008: The owner or operator shall demonstrate compliance with opacity standards using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.5). Periodic Testing Requirements 27. Points 007 and 008: On an annual basis, the operator shall complete a site specific extended gas analysis of the high and low pressure natural gas produced at this site that is routed to the flare in order to verify the VOC 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. ADDITIONAL REQUIREMENTS 28. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, I I.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: AIRS ID: 123/9D43 Page 7 of 14 olor.a Depa en : P •li Health and Environment • it Pollution Control Division Fora .. a • -.d ... a ,.. For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOr) in ozone nonattainment areas emitting less than 100 tons of VOC or NO. per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 29. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 30. 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. 31. 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. AIRS ID: 123/9D43 Page 8 of 14 1 ' oIora Depa en 61 P" li Health and Environment it Pollution Control Division 32. This permit i p in ncet,- t y an pleteness 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. 33. 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. 34. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 35. 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. 36. 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: Christopher Kester Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company AIRS ID: 12319D43 Page 9 of 14 olor Depa en . '•li Health and Environment x � A it Pollution Control Division Notes to Permit Holder - °me o ' z•e "` an -. 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°/02FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) Benzene 71432 1,483 Yes 75 n-Hexane 110543 12,218 Yes 611 Toluene 108883 1,788 Yes 90 006 Ethylbenzene 100414 104 No 6 Xylenes 1330207 680 Yes 34 224 TMP 540841 798 Yes 40 Benzene 71432 962 Yes 49 n-Hexane 110543 7,023 Yes 352 007 Toluene 108883 383 Yes 20 Ethylbenzene 100414 17 No 1 Xylenes 1330207 41 No 3 Benzene 71432 256 Yes 13 n-Hexane 110543 2,092 Yes 105 008 Toluene 108883 344 Yes 18 Ethylbenzene 100414 44 No 3 Xylenes 1330207 122 No 7 AIRS ID: 123/9D43 Page 10 of 14 of.., :4 trawl;, „:' 3 olor. Depa enz f P .li Health and Environment ?' it Pollution Control Division Berms 437z--.--.23a38z 145 010 n-Hexane 110543 9,058 Yes 453 Benzene 71432 524 Yes 27 n-Hexane 110543 4,345 Yes 218 Toluene 108883 649 Yes 33 011 Ethylbenzene 100414 40 No 2 Xylenes 1330207 262 Yes 14 224 IMP 540841 395 Yes 20 Benzene 71432 221 No 74 n-Hexane 110543 2,717 Yes 910 012 Toluene 108883 216 No 73 Xylenes 1330207 63 No 21 5) The emission levels contained in this permit are based on the following emission factors: Point 006: Weight Emission Pollutant Fraction of Factors Source Gas (%) Uncontrolled Ib/MMscf NOx 0.068 AP-42 (lb/MMBTU) CO 0.37 AP-42 (lb/MMBTU) VOC 84.95 110,643 Promax Benzene 0.4441 578.5 Promax Toluene 0.5355 697.5 Promax Ethylbenzene 0.0310 40.4 Promax Xylenes 0.2035 265.0 Promax n-Hexane 3.6595 4766.3 Promax 224 TMP 0.2389 311.1 Promax Point 007: Weight Emission Pollutant Fraction of Factors Source Gas(%) Uncontrolled lb/MMscf NOx ___ 0.068 AP-42 (lb/MMBTU) CO(lb/MMBTU) ___ 0.37 AP 42 VOC 67.95 67,787 Gas Analysis Benzene 0.0915 91.3 Gas Analysis Toluene 0.0364 36.3 Gas Analysis Ethylbenzene 0.0015 1.5 Gas Analysis AIRS ID: 123/9D43 Page 11 of 14 ' � olor. Depa en ' P •li Health and Environment �' it Pollution Control Division Pollutant Fraction of Factors Source Gas (%) Uncontrolled lb/MMscf Xylenes 0.0039 3.9 Gas Analysis n-hexane 0.6694 667.8 Gas Analysis Point 008: Weight Emission Pollutant Fraction of Factors Source Gas (%) Uncontrolled lb/MMscf NOx(lb/MMBTU) --- 0.068 AP-42 CO(Ib/MMBTU) --- 0.37 AP-42 VOC 24.36 14,488 Gas Analysis Benzene 0.043 25.6 Gas Analysis Toluene 0.058 34.3 Gas Analysis Ethylbenzene 0.007 4.4 Gas Analysis Xylenes 0.020 12.1 Gas Analysis n-hexane 0.352 209.1 Gas Analysis Point 010: Emission Factors Pollutant Uncontrolled Source lb/BBL Produced Water Throughput VOC 0.262 CDPHE n-Hexane 0.022 CDPHE Benzene 0.007 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 011: Emission Factors Uncontrolled Pollutant lb/BBL Source Condensate Throughput VOC 0.422 Promax n-Hexane 0.0109 Promax Benzene 0.0013 Promax Toluene 0.0016 Promax Ethylbenzene 0.0001 Promax Xylenes 0.0007 Promax Note: The controlled emissions for this point are based on the flare control efficiency of 95%. • AIRS ID: 123/9D43 Page 12 of 14 olor Depa enngf P li Health and Environment it Pollution Control Division Point 012: Emission Factors - Uncontrolled Pollutant lb/BBL loaded Source VOC 0.1495 AP-42 Benzene 0.0006 AP-42 n-Hexane 0.0068 AP-42 Toluene 0.0006 AP-42 Xylenes 0.0002 AP-42 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values multiplied by the VOC weight fraction: L = 12.46*S*P*M/T* [VOC wt fraction] S = 1.0 (Submerged loading: dedicated vapor balance service) P (true vapor pressure) =2.92 psia M (vapor molecular weight) = 55.04 Ib/Ib-mol T(temperature of liquid loaded) = 523.67 °R [VOC wt fraction] = 0.9302 The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors by the VOC emission factor. 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 and HAP NANSR Synthetic Minor Source of: VOC 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK AIRS ID: 123/9D43 Page 13 of 14 • .;t II olor. Depa en . - •li ''Health and Environment k, •it Pollution Control Division NSPS Part 6k,- _- dix-.:. • A _ ° A -, - I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/9D43 Page 14 of 14 Division Information Engineer: Christopher Kester Control Engineer: Stefanie Rucker Review Date: 06/09/2015 Application Date: 02/18/2015 Facility Identifiers Permit No. 15WE0418 Potentially located in ozone nonattainment area AIRS County# 123 Weld Facility# 9D43 Facility Type: exploration and production facility O Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: VOC l✓ NOx P CO Administrative Information Company Name: Bonanza Creek Energy Operating Company Source Name: North Platte A-33 Production Facility Source Location: NWNW SEC 33 T5N R63W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company Mailing Address 2: 410 17th Street,Suite 1400 Address ity,State Zip: Denver,CO 80202 Name: Jerry Dismukes Person To Phone: 303-803-1724 Contact Fax: Email: Jdismukes@bonanzacrk.com 'Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the North Platte A-33 Production Facility, located in the NWNW SEC 33 T5N R63W,Weld County,Colorado. Point Name Type Control Action Newly 006 VRT-1 Separator Venting Flare reported source Newly 007 SEP-1 Separator Venting Flare reported source Newly 008 OFL-2 Separator Venting Flare reported source Newly 010 PW Water Tanks Flare reported source Newly 011 CNDTK-1 Condensate Tanks Flare reported source Newly 012 TLO Loadout Flare reported source One vapor recovery tower(VRT)controlled by six(6)enclosed flares during gas compressor downtime.The 006 enclosed flares have a minimum destruction efficiency of 95%. Equipment Description This source vents natural gas from: Vapor Recovery Tower Emissions from this source are: routed to a flare Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 2.563614 MMscf/yr 292.65 scf/hr MW 49.4 lb/lb-mol 0.0070236 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.0000 4.0026 0.000 0 0.00 0.00 0.00 CO2 0.8548 44.01 0.376 0.007625 0.29 2547.89 1.27 N2 0.1516 28.013 0.042 0.000861 0.03 287.70 0.14 methane 5.5942 16.041 0.897 0.018187 0.69 6077.17 3.04 ethane 20.3226 30.063 6.110 0.123826 4.72 41376.35 20.69 propane 33.8185 44.092 14.911 0.302213 11.53 100984.22 50.49 isobutane 5.1131 58.118 2.972 0.060227 2.30 20124.80 10.06 n-butane 16.4858 58.118 9.581 0.194187 7.41 64887.42 32.44 isopentane 3.3667 72.114 2.428 0.0492 1.88 16440.14 8.22 n-pentane 4.4224 72.114 3.189 0.06174, 2.36 20630.37 10.32 cyclopentane 0.8811 70.13 0.618 0.012524 0.48 4184.88 2.09 n-Hexane 2.0954 86.18 1.806 0.036595 1.40 12228.19 6.11 cyclohexane 0.6604 84.16 0.556 0.011265 0.43 3764.19 1.88 Other hexanes 3.3200 86.18 2.861 0.057988 2.21 19376.64 9.69 heptanes 1.1755 100.21 1.178 0.023875 0.91 7977.81 3.99 methylcyclohexane 0.5009 98.19 0.492 0.009969 0.38 3331.13 1.67 224-TMP 0.1032 114.23 0.118 0.002389 0.09 798.28 0.40 Benzene 0.2805 78.12 0.219 0.004441 0.17 1483.96 0.74 Toluene 0.2867 92.15 0.264 0.005355 0.20 1789.37 0.89 Ethylbenzene 0.0144 106.17 0.015 0.00031 0.01 103.59 0.05 Xylenes 0.0946 106.17 0.100 0.002035 0.08 679.99 0.34 C8+Heavies 0.6558 114.23 0.749 0.015184 0.58 5073.72 2.54 VOC mass tact 0.8495 Total VOC(Uncontrolled) 141.93 Notes Mole%,MW,and mass fractions from Promax Analysis modeling VRT emissions based on 3 site specific pressurized condensate samples Emissions are based 1,314 hr/yr where VRTs Vent to Flare 15WE0418.CP1.xlsm One vapor recovery tower(VRT)controlled by six(6)enclosed flares during gas compressor downtime.The 006 enclosed flares have a minimum destruction efficiency of 95%. Flaring Information Equipment Description Flare to combust VRT gas during VRU downtime. Gas Heating Value 2763 Btu/scf Throughput 7083.265482 MMBtu/yr Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.068 jib NOX/MMBtu 0.37 alb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 110726 lb/MMscf 5536.30 lb/MMscf 141.93 tpy 7.10 tpy Promax Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.24 tpy 0.24 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.31 tpy 1.31 tpy AP-42 Benzene 578.85 lb/MMscf 28.94 lb/MMscf 1484 lb/yr 74 lb/yr Promax n-Hexane 4769.90 lb/MMscf 238.4951 lb/MMscf 12228 lb/yr 611 lb/yr Promax Toluene 697.987 lb/MMscf 34.8993 lb/MMscf 1789 lb/yr 89 lb/yr Promax Xylenes 265.248 lb/MMscf 13.2624 lb/MMscf 680 lb/yr 34 lb/yr Promax Ethylbenzene 40.406 lb/MMscf 2.0203 lb/MMscf 104 lb/yr 5 lb/yr Promax 224 TMP 311.389 lb/MMscf 15.5695 lb/MMscf 798 lb/yr 40 lb/yr Promax Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 15WE0418.CP1.xlsm Six(6)low-pressure separators controlled by six(6)enclosed flares during gas compressor downtime.The 007 enclosed flares have a minimum destruction efficiency of 95%. Equipment Description This source vents natural gas from: Six(6)low pressure separator Emissions from this source are: routed to a flare Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(O) 10.53 MMscf/yr 1202.511416 scf/hr MW 37.7885 Ib/Ib-mol 0.028860274 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.0000 4.0026 0.000 0.000000 0.0000 0.0 0.00 CO2 1.6244 44.01 0.715 0.018918 2.2683 19870.0 9.94 N2 0.5037 28.013 0.141 0.003734 0.4477 3921.8 1.96 methane 23.6272 16.041 3.790 0.100296 12.0252 105341.1 52.67 ethane 24.7757 30.063 7.448 0.197105 23.6324 207020.0 103.51 propane 28.1625 44.092 12.417 0.328603 39.3986 345131.9 172.57 isobutane 4.1753 58.118 2.427 0.064215 7.6992 67445.4 33.72 n-butane 11.4626 58.118 6.662 0.176293 21.1370 185160.3 92.58 isopentane 2.0275 72.114 1.462 0.038692 4.6391 40638.2 20.32 n-pentane 2.3426 72.114 1.689 0.044705 5.3600 46953.9 23.48 cyclopentane 0.1480 70.13 0.104 0.002747 0.3293 2884.8 1.44 n-Hexane 0.2932 86.18 0.253 0.006687 0.8017 7023.0 3.51 cyclohexane 0.0871 84.16 0.073 0.001940 0.2326 2037.4 1.02 Otherhexanes 0.5153 86.18 0.444 0.011752 1.4090 12343.0 6.17 heptanes 0.0273 100.21 0.027 0.000724 0.0868 760.4, 0.38 methylcyclohexane 0.0263 98.19 0.026 0.000683 0.0819 717.8 0.36 224-TMP 0.0093 114.23 0.011 0.000281 0.0337 295.3 0.15 Benzene 0.0442 78.12 0.035 0.000914 0.1096 959.7 0.48 Toluene 0.0149 92.15 0.014 0.000363 0.0436 381.6 0.19 Ethylbenzene 0.0005 106.17 0.001 0.000014 0.0017 14.8 0.01 Xylenes 0.0014 106.17 0.001 0.000039 0.0047 41.3 0.02 C8+Heavies 0.0022 114.06 0.003 0.000066 0.0080 69.7 0.03 VOC mass fracl 0.679 Total VOC(Uncontrolled) 356.43 Notes , Mole%,MW,and mass fractions from LP gas analysis directly off of LP Separator Emissions are based 1,314 hr/yr where Separators Vent to Flare 15WE0418.CP1.xlsm Six(6)low-pressure separators controlled by six(6)enclosed flares during gas compressor downtime.The 007 enclosed flares have a minimum destruction efficiency of 95%. Flaring Information Equipment Description Gas Heating Value 2152 Bty/scf Throughput 22669.168 MMBtu/yr Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.068 Ilb NOX/MMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 67672 lb/MMscf 3383.61 Ib/MMscf 356.4 tpy 17.8 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 lb/MMBTU 0.77 tpy 0.77 tpy AP-42 CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 4.19 tpy 4.19 tpy AP-42 Benzene 91.11 lb/MMscf 4.56 Ib/MMscf 960 lb/yr 48 lb/yr Gas Analysis n-Hexane 666.70 lb/MMscf 33.3351 lb/MMscf 7023 lb/yr 351 lb/yr Gas Analysis Toluene 36.228 lb/MMscf 1.8114 lb/MMscf 382 lb/yr 19 lb/yr Gas Analysis Xylenes 3.922 lb/MMscf 0.1961 lb/MMscf 41 lb/yr 2 lb/yr Gas Analysis Ethylbenzene 1.401 lb/MMscf 0.0700 lb/MMscf 15 lb/yr 1 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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 15WE0418.CP1.xlsm One open flare to control sales gas in case of an emergency.The open flare has a minimum destruction 008 efficiency of 95%. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 10 MMscf/yr 1141.552511 scf/hr MW 22.54 Ib/Ib-mol 0.02739726 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.0000 4.0026 0.000 0.00000 0.00 0.00 0.00 CO2 2.0249 44.01 0.891 0.03954 2.68 23513.42 11.76 N2 0.4619 28.013 0.129 0.00574 0.39 3414.04 1.71 methane 71.7852 16.041 11.515 0.51087 34.68 303827.54 151.91 ethane 14.9631 30.063 4.498 0.19957 13.55 118690.15 59.35 propane 7.0363 44.092 3.102 0.13764 9.34 81858.72 40.93 isobutane 0.7287 58.118 0.424 0.01879 1.28 11174.30 5.59 n-butane 1.8624 58.118 1.082 0.04802 3.26 28559.09 14.28 isopentane 0.3364 72.114 0.243 0.01076 0.73 6400.83 3.20 n-pentane 0.4149 72.114 0.299 0.01327 0.90 7894.49 3.95 cyclopentane 0.0396 70.13 0.028 0.00123 0.08 732.76 0.37 n-Hexane 0.0919 86.18 0.079 0.00351 0.24 2089.69 1.04 cyclohexane 0.0390 84.16 0.033 0.00146 0.10 866.03 0.43 Otherhexanes 0.1245 86.18 0.107 0.00476 0.32 2830.98 1.42 heptanes 0.0248 100.21 0.025 0.00110 0.07 655.73 0.33 methylcycohexane 0.0216 98.19 0.021 0.00094 0.06 559.61 0.28 224-TMP 0.0057 114.23 0.007 0.00029 0.02 171.80 0.09 Benzene 0.0124 78.12 0.010, 0.00043 0.03 255.59 0.13 Toluene 0.0141 92.15 0.013 0.00058 0.04 342.83 0.17 Ethylbenzene 0.0016 106.17 0.002 0.00008 0.01 44.82 0.02 Xylenes 0.0043 106.17 0.005 0.00020 0.01 120.46 0.06 C8+Heavies 0.0067 114.23 0.008 0.00034 0.02 201.94 0.10 VOC mass fracl 0.243 Total VOC(Uncontrolled) 72.38 Notes Mole%,MW,and mass fractions fromaverage of 3 site specific sales gas samples 15WE0418.CP1.xlsm One open flare to control sales gas in case of an emergency.The open flare has a minimum destruction 008 efficiency of 95%. Flaring Information Equipment Description Gas Heating Value 1305 Btu/scf Throughput 13050 MMBtu/yr Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.068 jib NOX/MMBtu 0.37 Ilb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 14476 lb/MMscf 723.80 lb/MMscf 72.4 tpy 3.62 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 lb/MMBTU 0.44 tpy 0.44 tpy AP-42 CO 0.37 lb/MMBTU 0.37 lb/MMBTU 2.41 tpy 2.41 tpy AP-42 Benzene 25.56 lb/MMscf 1.28 lb/MMscf 256 lb/yr 13 lb/yr Gas Analysis n-Hexane 208.97 lb/MMscf 10.4485 lb/MMscf 2090 lb/yr 104 lb/yr Gas Analysis Toluene 34.283 lb/MMscf 1.7141 lb/MMscf 343 lb/yr 17 lb/yr Gas Analysis Xylenes 12.046 lb/MMscf 0.6023 lb/MMscf 120 lb/yr 6 lb/yr Gas Analysis Ethylbenzene 4.482 lb/MMscf 0.2241 lb/MMscf 45 lb/yr 2 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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 15WE0418.CP1.xlsm 1010 Two(2)750 bbl produced water tanks. Emissions from the water tanks are routed to six(6)enclosed combustors that achieve a minimum VOC destruction efficiency of 95% Emissions Calculations Requsted Throughput 411720'bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 53.93532 tpy 2.696766 tpy CDPHE Benzene 0.007 lb/bbl 2882.04 lb/yr 144.102 lb/yr CDPHE n-Hexane 0.022 lb/bbl 9057.84 lb/yr 452.892 lb/yr CDPHE Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II.A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2—Odor Section I.A-No person,wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. 011 Eight(8)750 bbl atmospheric condensate storage tank. Emissions from the water tanks are routed to six(6)enclosed combustors that achieve a minimum VOC destruction efficiency of 95% Requsted Throughput 398580 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.422 lb/bbl 84.1 tpy 4.2 tpy Promax Benzene 0.001313 lb/bbl 523 lb/yr 26 lb/yr Promax Toluene 0.001626 lb/bbl 648 lb/yr 32 lb/yr Promax Ethylbenzene 0.000098 lb/bbl 39 lb/yr 2 lb/yr Promax Xylenes 0.000656 lb/bbl 261 lb/yr 13 lb/yr Promax n-Hexane 0.0109 lb/bbl 4345 lb/yr 217 lb/yr Promax 224 TMP 0.000992 lb/bbl 395 lb/yr 20 lb/yr Promax 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 LA-No person,wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. Regulation 6- New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons(471 bbl) NSPS OOOO: for storage vessels in the natural gas production,transmission, and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. Regulation 7—Volatile Organic Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is subject to the emission control requirements for condensate tanks since it is located in a non- attainment area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is currently subject) 012 Hydrocarbon Loadout to Tanker Trucks Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2, Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 1 AP-42 P True Vapor Pressure 2.92 psia Sales Oil Analysis M Molecular Weight of Vap 55.07 lb/lb-mole Sales Oil Analysis T Liquid Temperature 523.67 deg. R Field Data VOC weight fraction 0.9302 L 3.56 lb/10^3 gal 1.49E-01 lb/bbl Annual requested Throughput 398580 BBL/yr 16740360 gal/yr Annual requested VOC emissions 59580 lb/yr 29.79 tpy Control: Flare Vapor balance collection system has collection efficiency of 70%and the Efficiency: 66.50% flare has a destruction efficiency of 95%-overall control efficiency of 66.5% NCRPs Component Mass Fraction Benzene 0.0037 n-hexane 0.0457 Toluene 0.0036 Xylenes 0.0011 Source: Stable Sales Oil Analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.1495 lb/bbl 29.8 tpy 10.0 tpy AP-42 Benzene 0.0006 lb/bbl 220.9 lb/yr 74.0 lb/yr AP-42 n-Hexane 0.0068 lb/bbl 2720 lb/yr 911 lb/yr AP-42 Toluene 0.0005 lb/bbl 216 lb/yr 72 lb/yr AP-42 Xylenes 0.0002 lb/bbl 63 lb/yr 21 lb/yr AP-42 Regulatory Review 'Regulation 3-APEN and Permitting'.Requirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day of crude oil on an annual average basis? NA If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 AIRS(County/Plant) 123/9D43 Permit No, 15WE0418 Date 6/9/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emissions Emissions Ctrl. reportable Point# SCC Pollutant or CAS Factor Emisison Factor Source (tpy)' (tpy)` PTE(tpy)*Eff% ? 006 31000205 VOC 110725.994 lb/MMscf Promax 7.1 141.9 95% Yes 006 31000205 NOx 0.068 lb/MMBTU AP-42 0.2 0.2 0% No 006 31000205 CO 0.37Ib/MMBTUAP42 1.3 1.3 0% Yes 006 31000205 Benzene 578.853 lb/MMscf Promax 74.2 1484 95% Yes 006 31000205 n-Hexane 4769.902 lb/MMscf Promax 611.4 12228.2 95% Yes 006 31000205 Toluene 697.987 lb/MMscf Promax 89.5 1789.4 95% Yes 006 31000205 Ethylbenzene 40.406 lb/MMscf Promax 5.2 103.6 95% No 006 31000205 Xylenes 265.248 lb/MMscf Promax 34 680 95% Yes 007 31000205 VOC 67672.163 lb/MMscf Gas Analysis 17.8 356.4 95% Yes 007 31000205 • NOx 0.068 lb/MMBTUAP42 0.8 0.8 0% No 007 31000205 CO 0.37Ib/MMBTLAP42 4.2 4.2 0% Yes 007 31000205 Benzene 91.106 lb/MMscf Gas Analysis 48 959.7 95% Yes 007 31000205 n-Hexane 666.701 lb/MMscf Gas Analysis 351.2 7023 95% Yes 007 31000205 Toluene 36.228 lb/MMscf Gas Analysis 19.1 381.6 95% Yes 007 31000205 Ethylbenzene 1.401 lb/MMscf Gas Analysis 0.7 14.8 95% No 007 31000205 Xylenes 3.922 lb/MMscf Gas Analysis 2.1 41.3 95% No 008 31000205 VOC 14475.964 lb/MMscf Gas Analysis 3.6 72.4 95% Yes 008 31000205 NOx 0.068 lb/MMBTU AP-42 0.4 0.4 0% No 008 31000205 CO 0.37 lb/MMBTLAP42 2.4 2.4 0% Yes 008 31000205 Benzene 25.559 lb/MMscf Gas Analysis 12.8 255.6 95% Yes 008 31000205 n-Hexane 208.969 lb/MMscf Gas Analysis 104.5 2089.7 95% Yes 008 31000205 Toluene 34.283 lb/MMscf Gas Analysis 17.1 342.8 95% Yes 008 31000205 Ethylbenzene 4.482 lb/MMscf Gas Analysis 2.2 44.8 95% No 008 31000205 Xylenes 12.046 lb/MMscf Gas Analysis 6 120.5 95% No 010 40400315 VOC 6.238 lb/1000 ga CDPHE 2.7 53.9 95% Yes 010 40400315 Benzene 0.167 lb/1000 ga CDPHE 144.1 2882 95% Yes 010 40400315 n-Hexane 0.524 lb/1000 ga CDPHE 452.9 9057.8 95% Yes 011 40400311 VOC 10.048 lb/1000 ga Promax 4.2 84.1 95% Yes 011 40400311 Benzene 0.031 lb/1000 ga Promax 26.2 523.3 95% Yes 011 40400311 n-Hexane 0.26 lb/1000 qa Promax 217.2 4344.5 95% Yes 011 40400311 Toluene 0.039 lb/1000 ga Promax 32.4 648.1 95% Yes 011 40400311 Ethylbenzene 0.003 lb/1000 ga Promax 2 39.1 95% No 011 40400311 Xylenes 0.016 lb/1000 ga Promax 13.1 261.5 95% Yes 012 40600132 VOC 3.559lb/1000gaAP42 10 29.8 66% Yes 012 40600132 Benzene 0.013 lb/1000 ga AP-42 74 220.9 67% No 12 40600132 n-Hexane 0.163 lb/1000 ga AP-42 911.3 2720.3 67% Yes 12 40600132 Toluene 0.013 lb/1000 ga AP-42 72.5 216.3 66% No 12 40600132 Xylenes 0.004 lb/1000 ga AP-42 21 62.8 67% No y o a) a5 R� b ,Ur 00 0 co •o o f O. ++ C otrp 0o v, ai p ElN E Z O • —, —, —, -.... , as -aU M M M P CA o 1:41 menM s. e. 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C CC a E a) a) a) En O a a"" OO v, a Q W z G U g 7:i0 - , a, w g 5 O O OU N N o 49 5, 1 a a E ``ca' c c O c a ai a. o c . c 5 . c a z a l H .y c •c ,-o a) c a, a 03 N "O 4R,C Z u ai C a4 U Q C y C W W H. a ›. a C C O 0 Q W ❑ IDa) a. a.) ❑ N y '' -,t CC w) cn Cn Cn z up r E&P Storage Tank Air Pollutant Emissions Notice (APEN)Addendum Form' Company Name: Bonanza Creek Energy Operating Company LLC Source Name: North Platte A-33 Production Facility(COGCC#438202) Emissions Source AIRS ID2: 123/9D43/ Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well 05-123-399007 North Platte B11-V41-33HNC - - ❑ - - ❑ - - ❑ - - ❑ _ _ ❑ ❑ - - ❑ - - ❑ - - ❑ - - ❑ Footnotes: 1 Attach this addendum to associated APEN form when needed to report additional wells. 2 If this is a newly report source that has not been assigned an AIRS ID by the APCD, enter N/A fa LForm APCD-212 Form APCD-212-EP-StorageTank-APEN-Addendum.docx Z W G-' O O O O 3 o °3 ov a) aa) Z ZZ w ,.. 0 cam° E o000 0 To 0 c 3 > a°i c L a c ' 1 y al d N C b U L y N N N 0 O C ❑ cu N> .O i!7 Cn aJ 4. ^O W w Zo C O O\ O\ O, Z c .O y c > w O p. o � � � W 'p �d Y oz 0 N y O ° >.. to 70ent-nt C I a) ,d Q+ C •`� ›" �" >" L a) o p) y "v CO -,; O O O U O 01 CI ^ .O a. 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