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Home My WebLink About20150571.tiff A COPHE COLORADO iA CO . Department of Public .. Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150 O PO Box 758 RECEIVED Greeley, CO 80632 FEB 2 6 2015 February 23, 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On February 25, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company, LLC - State Antelope D-13 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, .f.. ta,,. t Ca..c,2,; .. Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 7U-bat). U-bl�v l oil) �t L i�LI 414..- aia to 5 si 7 3-a-aol5 CG' c 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe I raz+v r y o`.I . . John W. Hickenlooper, Governor I Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer t, (: , \ ..{ CDPHE Air Pollution Control Division CO Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC - State Antelope D-13 Production Facility - Weld County Notice Period Begins: February 25, 2015 Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company, LLC Facility: State Antelope D-13 Production Facility Oil and Gas Exploration and Production Facility NWSW, Section 13, T5N, R62W Weld County The proposed project or activity is as follows: The applicant proposes to permit equipment associated with an oil and gas exploration and production facility. This permit covers condensate storage tanks, produced water storage tanks, emergency flare, separators, vapor recovery tower, and hydrocarbon loadout. 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 14WE1687 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: David V Thompson Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1 I Amy COLORADO . "77.= STATE OF COLORADO OF COzo •LO- • ■• D - • -Tv •F P C HEALTH AND ENVIRONMENT 4 AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692-3150 *4 ikk *Ian. CONSTRUCTION PERMIT PERMIT NO: 14WE1687 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 D-13 Production Facility, located in the NWSW, Section 13, T5N, R62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID CNDTK-1 007 Eight (8) 500 bbl tanks used for condensate storage. PW 008 Two (2) 500 bbl tanks and two (2) 60 bbl vaults are used for the storage of produced water associated with oil and gas production FL-2 010 One (1) Candlestick flare to be used in case of emergency. Flare has not yet been installed SEI l Four (4) low pressure gas/oil separators controlled by four (4) through 011 enclosed flares while compressors are down SEP-4 VRT-1 012 One (1) VRT controlled by four(4) enclosed flares when gas compressors are down TL 013 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: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit or commencement of operation, l 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 AIRS ID: 123/9CE4 Page 1 of 13 olor Depa en li ealth and Environment it Pollution Control Division Commission io 3, ectio .1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) after issuance of this permit or commencement of operations, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self- certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 4. Point 011: Within one hundred and eighty days (180) 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. Point 010: The following information shall be provided to the Division within fifteen (15) days after commencement of operations. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 7. 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 8. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type Equipment ID Point NO, VOC CO AIRS ID: 123/9CE4 Page 2 of 13 olormi Depa en . .li Health and Environment it Pollution Control Division CNDTK-1 007 - Point PW 008 2.2 Point FL-2 010 0.4 3.9 2.4 Point SEP-1 through 011 0.3 9.2 1.4 Point SEP-4 VRT-1 012 0.1 3.2 0.6 Point TL 013 4.4 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) 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. 9. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit (Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID CNDTK-1 007 Enclosed Flare VOC PW 008 Enclosed Flare VOC FL-2 010 Open Flare (Emergency) VOC SEP-1 through 011 Enclosed Flare VOC SEP-4 VRT-1 012 Enclosed Flare VOC TL 013 Vapor Balance and Enclosed Flare VOC PROCESS LIMITATIONS AND RECORDS 10. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Lim its Facility AIRS f Process Parameter Annual Limit AIRS ID: 123/9CE4 Page 3 of 13 olor Depa en li ealth and Environment it Pollution Control Division Equipment ID CNDTK-1 007 Condensate Throughput 267,180 BBL PW 008 Produced Water Throughput 339,450 BBL FL-2 010 Gas Vented to Emergency Flare 10 MMSCF SEP-1 Gas Vented from Separators while gas through 011 compressors are down 4.8 MMSCF SEP-4 VRT-1 012 Gas Vented from VRT while gas 1 MMSCF compressors are down TL 013 Oil Loaded 267,180 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. 11. Point 011: 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 monthly throughput records to demonstrate compliance with the limits specified in Condition 11 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 13. Visible emissions shall not exceed twenty percent(20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVI1.B.2.b 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. Point 007: 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 AIRS ID: 123/9CE4 Page 4 of 13 ll olor Depa en . P •Ii Health and Environment Air Pollution Control Division other means -- _ . b - I , d- heth- is operating properly. The operator shall comply with all applicable requirements of Section XII. 17. Point 007: 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. Point 007: The flare covered by this permit is subject to Regulation No. 7, Section XVII.B 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. 19. Point 007: The condensate storage tanks covered by this permit are subject to Regulation 7, Section XVII emission control requirements. These requirements include, but are not limited to: Section XVII.C. - Emission reduction from condensate storage tanks at oil and gas exploration and production operations, natural gas compressor stations, natural gas drip stations and natural gas processing plants. XVII.C.1. Beginning May 1, 2008, owners or operators of all atmospheric condensate storage tanks with uncontrolled actual emissions of volatile organic compounds equal to or greater than 20 tons per year based on a rolling twelve-month total shall operate air pollution control equipment that has an average control efficiency of at least 95%for VOCs on such tanks. XVII.C.3. Monitoring: The owner or operator of any condensate storage tank that is required to control volatile organic compound emissions pursuant to this section XVII.C. shall visually inspect or monitor the Air Pollution Control Equipment to ensure that it is operating at least as often as condensate is loaded out from the tank, unless a more frequent inspection or monitoring schedule is followed. In addition, if a flare or other combustion device is used, the owner or operator shall visually inspect the device for visible emissions at least as often as condensate is loaded out from the tank. XVII.C.4. Recordkeeping: The owner or operator of each condensate storage tank shall maintain the following records for a period of five years: XVII.C.4.a. Monthly condensate production from the tank. XVII.C.4.b For any condensate storage tank required to be controlled pursuant to this section XVII.C., the date, time and duration of any period where the air pollution control equipment is not operating. The duration of a period of non-operation shall be from the time that the air pollution control equipment was last observed to be operating until the time the equipment recommences operation. XVII.C.4.c. For tanks where a flare or other combustion device is being used, the date and time of any instances where visible emissions are observed from the device. AIRS ID: 123/9CE4 Page 5 of 13 Depa en li ealth and Environment Ii Pollution Control Division 20. Point 013: Dolor i ne ttainment 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) 21. Point 013: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 21 (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. 22. Point 013: 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 23. Points 007, 008, 010, 011, 012, and 013: 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 24. Point 010 : 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.1 & 4). This measurement shall consist of a minimum observation period of sixty consecutive minutes with opacity not to exceed 30% for more than 6 minutes during the observation period. Periodic Testing Requirements 25. There are no periodic testing requirements associated with this permit. AIRS ID: 123/9CE4 Page 6 of 13 olor Depa en P .'Ii ''Health and Environment II it Pollution Control Division ADDITIONAL REQ= N 26. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 301h 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 (NOx) in ozone nonattainment areas emitting less than 100 tons of V0C or N0x 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. 27. 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 0). GENERAL TERMS AND CONDITIONS 28. 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. 29. 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 AIRS ID: 123/9CE4 Page 7 of 13 olor Depa en li ealth and Environment it Pollution Control Division and has been y c in all cts 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. 30. 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. 31. 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. 32. 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. 33. 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. 34. 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: David Thompson Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC AIRS ID: 123/9CE4 Page 8 of 13 II olor Depa en P .li Health and Environment it Pollution Control Division Notes to Permit Holder - "'- me o •e a '`=. 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C%2FCBONAddlinkView&cid=1251599389641&pagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (lb/yr) reportable? (Ib/yr) Benzene 71432 801.5 Yes 40.1 n-Hexane 110543 4274.9 Yes 213.7 007 Toluene 108883 534.4 Yes 26.7 Ethylbenzene 100414 80.2 No 4 Xylenes 1330207 267.2 Yes 13.4 Benzene 71432 2376.2 Yes 118.8 008 n-Hexane 110543 7467.9 Yes 373.4 Benzene 71432 280.3 Yes 14 n-Hexane 110543 2098.8 Yes 104.9 010 Toluene 108883 223.7 No 11.2 Ethylbenzene 100414 61.6 No 3.1 Xylenes 1330207 103.6 No 5.2 Benzene 71432 739.1 Yes 37 n-Hexane 110543 5372.2 Yes 268.6 011 Toluene 108883 273.1 Yes 13.7 Ethylbenzene 100414 22.9 No 1.1 AIRS ID: 123/9CE4 Page 9 of 13 olor Depa en li ealth and Environment it Pollution Control Division Xyl 0 • 1.7 Benzene 71432 1065.6 Yes 53.3 n-Hexane 110543 6585.7 Yes 329.3 012 Toluene 108883 844.9 Yes 42.2 Ethylbenzene 100414 108.5 No 5.4 Xylenes 1330207 232.6 No 11.6 Benzene 71432 165.6 No 55.5 n-Hexane 110543 1749.4 Yes 586.1 013 Toluene 108883 104.5 No 35 Xylenes 1330207 24.5 No 8.2 5) The emission levels contained in this permit are based on the following emission factors: Point 007: Emission Factors Uncontrolled Pollutant lb/BBL Source Condensate Throughput VOC 0.42 E&P TANK n-Hexane 0.016 E&P TANK Benzene 0.003 E&P TANK Toluene 0.002 E&P TANK Ethylbenzene 0.0003 E&P TANK Xylenes 0.001 E&P TANK Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 008: 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 010: Weight Emission Emission Pollutant Fraction of Factors Factors Gas(%) Uncontrolled Controlled Source lb/MMscf lb/MMsd AIRS ID: 123/9CE4 Page 10 of 13 ` olor Depa en P di Health' and Environment it Pollution Control Division t ;on Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled Ib/MMscf lb/MMscf NOx 0.068 0.068 AP-42 (Ib/MMBTU) CO(Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 26.300 15720.55 786.0275 Gas Analysis Benzene 0.047 28.0325 1.4016 Gas Analysis Toluene 0.037 22.3689 1.1185 Gas Analysis Ethylbenzene 0.010 6.1629 0.3082 Gas Analysis Xylenes 0.018 10.3649 0.5183 Gas Analysis n-hexane 0.350 209.879 10.494 Gas Analysis Point 011: Weight Emission Emission Fraction of Factors Factors Source Pollutant Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx ObIMMBTU) --- 0.068 0.068 AP-42 (Ib/ CO(Ib/MMBTU) --- 0.37 0.37 AP-42 VOC 72.920 76585.9374 3829.2969 Gas Analysis Benzene 0.147 153.9727 7.6986 Gas Analysis Toluene 0.054 56.8947 2.8447 Gas Analysis Ethylbenzene 0.005 4.7623 0.2381 Gas Analysis Xylenes 0.007 7.2834 0.3642 Gas Analysis n-hexane 1.065 1119.2031 55.9602 Gas Analysis Point 012: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled lb/MMscf Ib/MMscf NOx ObIMMBTU) --- 0.068 0.068 AP-42 (Ib/ CO 0.37 0.37 AP-42 (Ib/MMBTU) VOC 90.328 129954.1 6497.705 Gas Analysis Benzene 0.741 1065.6 53.28 Gas Analysis Toluene 0.587 844.9 42.245 Gas Analysis Ethylbenzene 0.075 108.5 5.425 Gas Analysis Xylenes 0.162 232.6 11.63 Gas Analysis n-hexane 4.578 6585.7 329.285 Gas Analysis Point 013: Emission Factors - Uncontrol led AIRS ID: 123/9CE4 Page 11 of 13 olor Depa en li m it Pollutionealthand ControlEnviron Divisionent Pollutant VOC 0.0991 AP-42 Benzene 0.0006 AP-42 n-Hexane 0.0066 AP-42 Toluene 0.0004 AP-42 Xylenes 0.0001 AP-42 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46'S'P'M/T S= 1.0 (Submerged loading: VRU) P(true vapor pressure) = 1.69 psia M (vapor molecular weight) =61.17 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 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, 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://ecfrsi poaccess.c ov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD AIRS ID: 123/0CE4 Page 12 of 13 olorl Depa en P .Ii Health and Environment ' A it Pollution Control Division MACT 63.121 9 S4- E . . „ 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: 123/9CE4 Page 13 of 13 Division Information Engineer: David Thompson Control Engineer: Chris Laplante Review Date: 02/09/2015 Application Date: 10/15/2014 Facility Identifiers Permit No. 14WE1687 Potentially located in ozone nonattainment area AIRS County# 123 Weld Facility# 9CE4 Facility Type: exploration and production facility ❑Located in the 8-hour non-attainment area? O True Minor 0 Synthetic Minor for: i✓ VOC r NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company, LLC Source Name: State Antelope D-13 Production Facility Source Location: NWSW, Section 13, T5N, R62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company, LLC Mailing Address 2: 410 17th Stree,Suite 1500 Address State Zip: Denver, CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 000-000-0000 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 D-13 Production Facility, located in the NWSW,Section 13,T5N, R62W,Weld County,Colorado. Point Name Type Control Action Newly 007 CNDTK-1 Condensate Tanks Flare reported source Newly 008 PW Water Tanks Flare reported source Newly 010 FL-2 Separator Venting Flare reported source SEP-1 Newly 011 through Separator Venting Flare reported SEP-4 source Newly 012 VRT-1 Separator Venting Flare reported source Newly 013 TL Loadout Flare reported source 007 Eight(8)500 bbl tanks used for condensate storage. Requsted Throughput 267180 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled VOC 0.42 lb/bbl 56.1 tpy 2.8 Benzene 0.003 lb/bbl 801.54 lb/yr 40.077 Toluene 0.002 lb/bbl 534.36 lb/yr 26.718 Ethylbenzene 0.0003 Ib/bbl 80.154 lb/yr 4.0077 xylenes 0.001 lb/bbl 267.18 lb/yr 13.359 n-Hexane 0.016 lb/bbl 4274.88 lb/yr 213.744 Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a source s emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is bas readings taken at 15-second intervals for six minutes. The approved reference test method for visible en Method 9(40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II.A and B of this regi. Section II.A.5 -Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air po 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 contaminant such as to result in detectable odors which are measured in excess of the following limits: For areas us( residential or commercial purposes it is a violation if odors are detected after the odorous air has been d 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 se 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 not subject to the emission control requirements for condensate tanks since it is lc area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is not currently subject to this since actual uncontrolled emissions are less than 20 tp Emissions Source tpy E&P TANK lb/yr E&P TANK lb/yr E&P TANK lb/yr E&P TANK lb/yr E&P TANK lb/yr E&P TANK ;hall allow or cause the ;ed on 24 consecutive opacity fissions measurement is EPA elation. a smokeless flare or other illutant which is in excess of Is from any single source :d predominantly for iluted with seven (7) or more figments. mated in an attainment 008 Two (2)500 bbl tanks and two (2)60 bbl vaults are used for the storage of produced v Emissions Calculations Requsted Throughput 339450 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.262 lb/bbl 44.46795 tpy 2.223398 tpy CDPHE Benzene 0.007 lb/bbl 2376.15 lb/yr 118.8075 lb/yr CDPHE n-Hexane 0.022 lb/bbl 7467.9 lb/yr 373.395 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. (only needed if using flare) 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. 010 One(1)Candlestick flare to be used in case of emergency.Flare has not yet been installed Equipment Description This source vents natural gas from: Flare Emissions from this source are: routed to a flare Natural gas venting from Flare.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=D'MW'Xx/C Ex=emissions of pollutant x 0=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-nap at 60F and 1 atm Throughput(Q) 10 MMscf/yr 1141.552511 sc81r MW 22.7 Ibdb-mol 0.02739726 MMscf/d mole% MW Ibwlbmol mass fraction Ib/hr lb/yr tPy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.41 44.01 1.062 0.047 3.20 28027.05 14.01 N2 0.86 28.013 0.241 0.011 0.73 6355.03 3.18 methane 72.61 16.041 11.647 0.513 35.08 307302.39 153.65 ethane 12.46 30.063 3.746 0.165 11.28 98843.81 49.42 propane 7.49 44.092 3.302 0.145 9.95 87119.51 43.56 isobutane 0.72 58.118 0.418 0.018 1.26 11025.55 5.51 n-butane 2.21 58.118 1.283 0.057 3.86, 33854.12 16.93 isopentane 0.38 72.114 0.273 0.012 0.82 7211.40 3.61 n-pentane 0.47 72.114 0.342 0.015 1.03 9011.40 4.51 cycloperdane 0.04 70.13 0.030 0.001 0.09 793.82 0.40 n-Hexane 0.09 88.18 0.080 0.004 0.24 2098.79 1.05 cydohexane 0.04 84.16 0.030 0.001 0.09 783.88 0.39 Other hexanes 0.14 86.18 0.116 0.005 0.35 3072.01 1.54 heptanes 0.02 100.21 0.022 0.001 0.06 588.47 0.28 methylcydohexane 0.02 98.19 0.018 0.001 0.06 481.88 0.24 224-TMP 0.01 114.23 0.010 0.000 0.03 256.19 0.13 Benzene 0.01 78.12 0.011 0.000 0.03 280.33 0.14 Toluene 0.01 92.15 0.008 0.000 0.03 223.69 0.11 Ethylbenzene 0.00 106.17 0.002_ 0.000 0.01 61.63 0.03 Xylenes 0.00 106.17 0.004 0.000 0.01 103.65 0.05 08+Heavies 0.01 114.23 0.010 0.000 0.03 259.20 0.13 VOC mass frad 0.262 Total VOC(Uncontrolled) 78.60 Notes Mole%,MW,and mass fractions are comprised of weighted average of two gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. 14WE1687.CP1.xlsm 010 One(1)Candlestick flare to be used in case of emergency.Flare has not yet been installed Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Candlestick Flare Model TBD Serial Number TBD Gas Heating Value 1295 Btulscf Throughput 12950 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make TBD Model TBD Requested Control 100.00% Annual Bypass Tim 50.00% Backup Flare LOverall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBtu 0.37 CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 15721 lb/MMscf 786.03 lb/MMscf 78.6 tpy 3.9 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.4 tpy 0.4 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 2.4 tpy 2.4 tpy AP-42 Benzene 28.03 lb/MMscf 1.40 lb/MMscf 280 lb/yr 14 lb/yr Gas Analysis n-Hexane 209.88 lb/MMscf 10.4939 lb/MMsd 2099 lb/yr 105 lb/yr Gas Analysis Toluene 22.369 lb/MMscf 1.1184 lb/MMscf 224 lb/yr 11 lb/yr Gas Analysis Xylenes 10.365 lb/MMsd 0.5182 lb/MMscf 104 lb/yr S lb/yr Gas Analysis Ethylbenzene 6.163 lb/MMsd 0.3081 lb/MMscf 62 lb/yr 3 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 14WE1687.CP1.xlsm 011 Four (4)low pressure gas/oil separators controlled by four(4)enclosed flares while compressors are down Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Cr MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at B0F and 1 atm Throughput(O) 4.8 MMscf/yr 547.9452055 scf/nr MW 39.8 lb/lb-mol 0.013150685 MMscf/d mole% MW Ibx/Ibmd mass fraction Ib/hr Ib/yr WY Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.04 44.01 0.899 0.023 1.30 11379.52 5.69 N2 0.18 28.013 0.049 0.001 0.07 624.06 0.31 methane 22.08 16.041 3.542 0.089 5.12 44859.68 22.43 ethane 20.92 30.063 6.289 0.158 9.09 79654.92 39.83 propane 29.42 44.092 12.971 0.326 18.75 164278.56 82.14 isobutane 3.95 58.118 2.298 0.058 3.32 29104.51 14.55 n-butane 13.61 58.118 7.910 0.199 11.44 100175.44 50.09 Isopentane 2.57 72.114 1.851 0.047 2.88 23439.37 11.72 n-pentane 3.24 72.114 2.335 0.059 3.38 29586.82 14.78 cyclopentane 0.25 70.13 0.172 0.004 0.25 2177.84 1.09 n-Hexane 0.49 86.18 0.424 0.011 0.81 5372.17 2.69 C/dohexane 0.15 84.16 0.124 0.003 0.18 1572.17 0.79 Otherhexanes 0.82 86.18 0.710 0.018 1.03 8987.10 4.49 heptanes 0.06 100.21 0.057 0.001 0.08 725.95 0.36 methylbyclohexane 0.05 98.19 0.049 0.001 0.07 820.54 0.31 224TMP 0.03 114.23 0.033 0.001 0.05 415.21 0.21 Benzene 0.07 78.12 0.058 0.001 0.08 739.07 0.37 Toluene 0.02 92.15 0.022 0.001 0.03 273.09 0.14 Ethylbenzene 0.00 106.17 0.002 0.000 0.00 22.86 0.01 Xylenes 0.00 106.17 0.003 0.000 0.00 34.96 0.02 C8+Heavies 0.01 114 0.008 0.000 0.01 106.84 0.05 VOC mass frau 0.729 Total VOC(Uncontrolled) 183.81 Notes Mole%,MW,and mass fractions from Critter Creek 2-03H gas analysis collected XX/XX/XX. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. 14WE1687.CP1.xlsm . 011 Four (4)low pressure gas/oil separators controlled by four(4)enclosed flares while compressors are down Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Tornado Model 40'Flare Stack Serial Number 12345678 Gas Heating Value 1549 Btu/scf Throughput 7435.2 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make TBD Model TBD Requested Control 100.00% Annual Bypass Tim 50.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 Ilb NOX/MMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 76586 Ib/MMsd 3829.30 lb/MMscf 183.8 tpy 9.2 tpy Gas Analysis Noy 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.3 tpy 0.3 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 1.4 tpy 1.4 tpy AP-42 Benzene 153.97 lb/MMscf 7.70 Ib/MMsd 739 lb/yr 37 lb/yr Gas Analysis n-Hexane 1119.20 Ib/MMsd 55.9602 lb/MMscf 5372 lb/yr 269 lb/yr Gas Analysis Toluene 56.895 lb/MMscf 2.8447 lb/MMscf 273 lb/yr 14 lb/yr Gas Analysis Xylenes 7.283 lb/MMscf 0.3642 lb/MMscf 35 lb/yr 2 lb/yr Gas Analysis Ethylbenzene 4.762 lb/MMscf 0.2381 lb/MMscf 23 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 14WE1687.CP1.xlsm 012 Four(4)enclosed flares are used to control gas from a single VRT when gas compressors are down Equipment Description This source vents natural gas from: a single VRT Emissions from this source are: routed to a flare Natural gas venting from a single VRT.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 0=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/Ibmol)at 60F and 1 atm Throughput(O) 1 MMscf/yr 114.1552511 sd/hr MW 54.5 Ib/Ib-mil 0.002739726 MMscf/d mole% MW Ibxllbmol mass fraction lb/hr Ib/yr WY Helium 4.0026 0.000 0.000 0.00 0.00 0.00 ' CO2 44.01 0.000 0.000 0.00 0.00 0.00 N2 28.013 0.000 0.000 0.00 0.00 0.00 methane 16.041 0.000 0.000 0.00 0.00 0.00 ethane 30.063 0.000 0.000 0.00 0.00 0.00 propane 44.092 0.000 0.000 0.00 0.00 0.00 isobutane 58.118 0.000 0.000 0.00 0.00 0.00 n-butane 58.118 0.000 0.000 0.00 0.00 0.00 isopentane 72.114 0.000 0.000 0.00 0.00 0.00 n-pentane 72.114 0.000 0.000 0.00 0.00 0.00 cydoPentane 70.13 0.000 0.000 0.00 0.00 0.00 n-Hexane 86.18 0.000 0.000 0.00 0.00 0.00 cydohexane 84.16 0.000 0.000 0.00 0.00 0.00 Other hexanes 86.18 0.000 0.000 0.00 0.00 0.00 heptanes 100.21 0.000 0.000 0.00 0.00 0.00 methylcyclohexane 98.19 0.000 0.000 0.00 0.00 0.00 224-TMP 114.23 0.000 0.000 0.00 0.00 0.00 Benzene 78.12 0.000 0.000 0.00 0.00 0.00 Toluene 92.15 0.000 0.000 0.00 0.00 0.00 Ethylbenzene 106.17 0.000 0.000 0.00 0.00 0.00 Xylenes 108.17 0.000 0.000 0.00 0.00 0.00 C8+Heavies 137.4837288 0.000 0.000 0.00 0.00 0.00 VOC mass trail 0.000 Total VOC(Uncontrolled) 0.00 Notes 14 WE1687.CP1.xlsm 012 Four(4)enclosed flares are used to control gas from a single VRT when gas compressors are down Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Abutec 200 Model 200 ECD Serial Number 90020-010,90025-001,90020-007,90020-031 Gas Heating Value 3040 Btu/scf Throughput 3040 MMBtu/yr _ VRU Information Equipment Description Engine to recompress gas to sales line. Make TBD Model TBD Requested Control 100.00% Annual Bypass Ti 50.00% Backup Flare Overall Control 95.00°/j 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 129954 Ib/MMsd 6497.71 lb/MMscf 65.0 tpy 3.2 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.1 tpy 0.1 tpy AP-42 CO 037 lb/MMBTU 0.37 Ib/MMBTU 0.6 tpy 0.6 tpy AP-42 Benzene 1065.60 lb/MMscf 53.28 lb/MMscf 1066 lb/yr 53 lb/yr Gas Analysis n-Hexane 6585.70 lb/MMscf 329.2850 lb/MMscf 6586 lb/yr 329 lb/yr Gas Analysis Toluene 844.900 lb/MMscf 42.2450 lb/MMsd 845 lb/yr 42 lb/yr Gas Analysis Xylenes 232.600 lb/MMscf 11.6300 lb/MMscf 233 lb/yr 12 lb/yr Gas Analysis Ethylbenzene 108.500 lb/MMsd 5.4250 lb/MMscf 109 lb/yr 5 lb/yr Gas Analysis Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section ll.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 4' 14WE1687.CP1.xlsm 013 Hydrocarbon Loadout to Tanker Trucks The table of inputs below enables you to calculate the loading loss emissions factor"L". Calculations If you choose to use a state default emissions factor,you may enter is directly into cell B14 L= 12.46*S*P*M/T(AP-42: Chapter 5.2, Equation 1) in units lb/1,000 gallons which will overwrite L= loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 1 AP-42 P True Vapor Pressure 1.69 psia Sales Oil Analysis M Molecular Weight of Var 61.17 lb/lb-mole AP-42 T Liquid Temperature 524 deg. R Field Data C Vapor VOC Content 0.96 L 2.36 lb/10^3 gal 9.91E-02 lb/bbl Annual requested Throughput 267180 BBL/yr 11221560 gal/yr Annual requested VOC emissions 26481 lb/yr 13.24 tpy Control: Flare Efficiency: 95.00% Collection Efi 0.7 NCRPs Component Mass Fraction If the operator provides HAP speciation from a stable"sales oil" Benzene 0.0063 analysis,enter the mass fraction from this data. Alternatively,if n-hexane 0.0661 the operator modeled a pressurized oil to develop a site specific Toluene 0.0039 emissions factor,enter the modeled mass fraction for the Xylenes 0.0009 Source: Stable Sales Oil Analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.0991 lb/bbl 13.2 tpy 4.4 tpy AP-42 Benzene 0.0006 lb/bbl 165.6 lb/yr 55.5 lb/yr AP-42 n-Hexane 0.0065 lb/bbl 1749 lb/yr 586.1 lb/yr AP-42 Toluene 0.0004 lb/bbl 105 lb/yr 35.0 lb/yr AP-42 Xylenes 0.0001 lb/bbl 24 lb/yr 8.2 lb/yr AP-42 Regulatory Review (Reoulafon 3-APEN and Permittina Requirements Is this site considered an exploration and production location (e.g.well pad)? Yes/No If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day on an annual average basis? Yes/No • If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? Yes/No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION FACILITY EMISSION SUMMARY Ronan Creek Enrgy Opening Company,LLC Stole Antelope 0-13 Production Facility 123/9064 NWSW,Section 13.TaN,R82W Weld County PTE-WITH ENFORCEABLE CONTROLS PTE-UNCONTROLLED POINT Penn Description NO4 VOC Fug CO Ryon Total NOs VOC Fug CO Report Total REMARKS VOC We HAP, VOC able HAPs HAP, HAPs 007 14WE1687 Condensate Tanks 2.8 58.1 008 14WE1687 Water Tanks 2.2 44.5 010 14WE1687 Separator Venting 0.4 3.0 2.4 0.4 78.8 2.4 011 I4WE1687 Separator Venting 0.3 02 16, 0.3 183.8 1.4 012 14WE1887 Separator Venting 0.1 3.2 0.6 0.1 85.0 0.6 013 14WE1687 Loadoul 4.4 13.2 014 14WE1687 FoollNee 17.3 173 Total 0.8 25.7 17.3 4.4 0.0 0.0 0A 441.2 17.3 4.4 0.0 0.0 Total PBTIAIes 01 26.7 17.3 4.4 0.0 0.0 • • Page 15 of 21 Printed 2/18/2015 Bonanza Creek Energy Operating Company,LLC Slate Antelope D-13 Production Facility 123/9CE4 NWSW.Section 13,1514,R62W Weld County HAPs IbM Controlled Formaldehyde Aeemeehpee Benzene Acrolein Toluene Swann.Xylenes n-Hexane 224 IMP McOH DEA Total lib/yr)Total lTPYI. au1w 007 14WE1687 Condensale Taos 40 26 3 7 4 14 214 29]9 0.1 ow 0.1 008 14WE1687 Water inks 119 3734 492.2 0.2 02 010 14WE1687 Separator Venino 14 112 31 52 104.9 1304 0.1 0.1 011 14W61687 Separator Vntna 37 13.7 1.1 17 268.6 322.1 02 02 012 14WE1687 Separator Vntna 53 4?2 54 116 329.3 441.8 0.2 0.2 013 14W61687 LoadeN 555 35 8.2 586.1 684.8 03 0.3 014 14WElW7 FUOVues 80. 130.1 399 920 5372 880.6 04 6.3 0.0 0.0 00 • 0.0 0.0 0.0 0.0 0.0 00 TOTAL 00 0.0 0.2 0.0 0.1 00 01 12 0.0 0.0 0.0 32578 1.6 1.4 'Red text indicates emissions below de minimus levels , HAPs lb* Uncontrolled Formaldehyde 4 etaeebvde Benzene Acrolein Toluene e uolhaeaane Xylenes n-Hexane 224 IMP McOH DEA Total llb/wl Total(TAY)"'^^^se 007 14W61687 Condense'',Tanks 4 rts 802 534 80.2 267.2 42749 5958.2 3.0 2.9 008 14W61687 Water Tanks 2376 74679 9844.1 4.9 49 010 14W51687 Scattier Pontine 280 2237 616 103.6 2098.8 2768.0 1.4 1.2 011 14W51687 SmaaboVmdna 739 273.1 22.9 35 53722 64423 3.2 3.2 012 14W51687 Swards,Ventre 1068 844.9 108.5 232.65 6 6587 8837.3 44 42 013 14WE1687 Loalom 165.6 1045 24.5 1749.4 2044.0 1.0 09 014 14WE1687 Fualives 805 ,130.1 399 929 53T2 8806 0.4 0.3 0.0 00 00 00 0.0 0.0 0.0 0.0 00 TOTAL 00 0.0 2.8 00 1.1 02 04 14.0 0.0 0.0 00 36T745 18.4 176 'Red text Indicates emissions below de minimus levels AIRS(County/Plant) 123/9CE4 Permit No. 14WE1687 Date 2/9/2015 Uncontrolled Emission Point# SCC Pollutant or CAS Factor 007 40400311 VOC 10 lb/1000 ga 007 40400311 Benzene 0.072 lb/1000 ga 007 40400311 n-Hexane 0.381 lb/1000 ga 007 40400311 Toluene 0.048 lb/1000 ga 007 40400311 Ethylbenzene 0.007 lb/1000 qa 007 40400311 Xylenes 0.024 lb/1000 ga 008 40400315 VOC 6.238 lb/1000 ga 008 40400315 Benzene 0.167 lb/1000 ga 008 40400315 n-Hexane 0.524 lb/1000 ga 010 31000205 VOC 15720.55 Ib/MMscf 010 31000205 NOx 0.068 Ib/MMBTU 010 31000205 CO 0.37 Ib/MMBTU 010 31000205 Benzene 28.033 lb/MMscf 010 31000205 n-Hexane 209.879 lb/MMscf 010 31000205 Toluene 22.369 Ib/MMscf 010 31000205 Ethylbenzene 6.163 lb/MMscf 010 31000205 Xylenes 10.365 lb/MMscf 011 31000205 VOC 76585.937 lb/MMscf 011 31000205 NOx 0.068Ib/MMBTU 011 31000205 CO 0.37 Ib/MMBTU 011 31000205 Benzene 153.973 lb/MMscf 011 31000205 n-Hexane 1119.203 lb/MMscf 011 31000205 Toluene 56.895 lb/MMscf 011 31000205 Ethylbenzene 4.762 lb/MMscf 011 31000205 Xylenes 7.283 lb/MMscf 012 31000205 VOC 129954.1 Ib/MMscf 012 31000205 NOx 0.068 Ib/MMBTU 012 31000205 CO 0.37 Ib/MMBTU 012 31000205 Benzene 1065.6 lb/MMscf 012 31000205 n-Hexane 6585.7 Ib/MMscf 012 31000205 Toluene 844.9 Ib/MMscf 012 31000205 Ethylbenzene 108.5 lb/MMscf 012 31000205 Xylenes 232.6 lb/MMscf 013 40600132 VOC 2.36 lb/1000 ga 013 40600132 Benzene 0.015 lb/1000 ga 13 40600132 n-Hexane 0.156 lb/1000 ga 13 40600132 Toluene 0.01 lb/1000 ga 13 40600132 Xylenes 0.002 lb/1000 ga 14 31000220 VOC 14 31000220 Benzene 14 31000220 n-Hexane 14 31000220 Toluene 14 31000220 Ethylbenzene 14 31000220 Xylenes Controlled Controlled Actual Requested NCRP= Emissions Emissions Ctrl. reportable Emisison Factor Source (tpyp (tpy)* PTE(tpy)' Eff% ? E&P TANK 2.8 56.1 95% Yes E&P TANK 40.1 801.5 95% Yes E&P TANK 213.7 4274.9 95% Yes E&P TANK 26.7 534.4 95% Yes E&P TANK 4 80.2 95% No E&P TANK 13.4 267.2 95% Yes CDPHE 2.2 44.5 95% Yes CDPHE 118.8 2376.2 95% Yes CDPHE 373.4 7467.9 95% Yes Gas Analysis 3.9 78.6 95% Yes AP-42 0.4 0.4 0% No AP-42 2.4 2.4 0% Yes Gas Analysis 14 280.3 95% Yes Gas Analysis 104.9 2098.8 95% Yes Gas Analysis 11.2 223.7 95% No Gas Analysis 3.1 61.6 95% No Gas Analysis 5.2 103.6 95% No Gas Analysis 9.2 183.8 95% Yes AP-42 0.3 0.3 0% No AP-42 1.4 1.4 0% Yes Gas Analysis 37 739.1 95% Yes Gas Analysis 268.6 5372.2 95% Yes Gas Analysis 13.7 273.1 95% Yes Gas Analysis 1.1 22.9 95% No Gas Analysis 1.7 35 95% No Gas Analysis 3.2 65 95% Yes AP-42 0.1 0.1 0% No AP-42 0.6 0.6 0% No Gas Analysis 53.3 1065.6 95% Yes Gas Analysis 329.3 6585.7 95% Yes Gas Analysis 42.2 844.9 95% Yes Gas Analysis 5.4 108.5 95% No Gas Analysis 11.6 232.6 95% No AP-42 4.4 13.2 67% Yes AP-42 55.5 165.6 66% No AP-42 586.1 1749.4 0.665 Yes AP-42 35 104.5 0.665 No AP-42 8.2 24.5 0.665 No Standard EFs-EPA-453/R-95-017 Table 2-4 17.3 17.3 0 Yes Standard EFs-EPA-453/R-95-017 Table 2-4 80.5 80.5 0 No Standard EFs-EPA-453/R-95-017 Table 2-4 537.2 537.2 0 Yes Standard EFs- EPA-453/R-95-017 Table 2-4 130.1 130.1 0 No Standard EFs- EPA-453/R-95-017 Table 2-4 39.9 39.9 0 No Standard EFs-EPA-453/R-95-017 Table 2-4 92.9 92.9 0 No 0 \ v '° °' v m o 0 0 '' v 3 c 'E `o 'Z ° O 5.. 3 aZ Z Z' Ce w I c 0 0 P d o00vn C. 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