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Home My WebLink About20160829.tiff ,A CAE COLORADO COto 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 1150OSt POBox758 RECEIVED Greeley,CO 80632 MAR 0 3 2016 February 26, 2016 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On March 2. 2016,the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company,LLC—Pronghorn F-22 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&Environment APCD-SS-B 1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, .4. ., t„..741.-0„,1* Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control.Division Enclosure 2016-0829 ��1-ZzA; 6,6: `313 -c°�a 3 4i0DCherry Creek Drive S., Denver,CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe fig '` o`i. John W. Hickenlooper,Governor 1" Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer * v *, tic\i,,.0>/"*r CDPHE Air Pollution Control Division CO ' Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Bonanza Creek Energy Operating Company, LLC—Pronghorn F-22 Production Facility—Weld County Notice Period Begins: March 2, 2016 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: Pronghorn F-22 Production Facility Exploration and Production NW/NW, Section 22,T5N,R61W Weld County The proposed project or activity is as follows: oil and gas production facility The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3.Part B, Section III.C.1.a(25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application,the Division's analysis, and a draft of Construction Permit 15WE1108 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-perm it-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: Kirk Bear Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B 1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1 I AYCOLORADO °�. , , STATE OF COLORADO COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT cod ye AIR POLLUTION CONTROL DIVISION TELEPHONE: 303 692 3150 A 41876* CONSTRUCTION PERMIT PERMIT NO: 15WE1108 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 Pronghorn F-22 Production Facility, located in the NWNW, Section 22, T5N, R61W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Twelve (12) 1100 barrel above ground atmospheric condensate CNDTK-1 005 storage tanks controlled by six enclosed flares. The flares have a minimum control efficiency of 95%. Two (2) 1100 barrel above ground atmospheric produced water PW 006 storage tanks controlled by six enclosed flares. The flares have a minimum control efficiency of 95%. Hydrocarbon loadout to tanker trucks. Loadout is controlled by using dedicated vapor balance service and six enclosed flares. TLO 007 The flares have a minimum control efficiency of 95%. Collection system is 70% efficient. Overall control efficiency is 66.5%. One (1) open flare used to control sales gas in case of emergency. FL-2 009 Flare has a minimum control efficiency of 95%. SEP-1 to Four(4) low pressure separators controlled by six enclosed flares 010 when the gas compressors are down. The flares have a minimum SEP-4 control efficiency of 95%. Two (2) VRT's controlled by six enclosed flares when the gas VRT 011 compressors are down. The flares have a minimum control efficiency of 95%. MNTK-1 015 One (1) above ground 500 barrel maintenance tank. No control. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: AIRS ID: 123-9DA3 Page 1 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation or issuance of this permit, whichever comes later, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdghe.state.co.us/aD/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. 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 6. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO VOC CO Emission Type X CNDTK-1 005 0.2 3.7 0.7 Point PW 006 — 2.1 — Point TLO 007 0.1 15.9 0.4 Point FL-2 009 0.7 6.3 3.6 Point SEP-1 to SEP-4 010 0.6 15.4 2.5 Point AIRS ID: 123-9DA3 Page 2 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division VRT 011 0.1 3.5 0.6 Point MNTK-1 015 -- 1.9 -- 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. 7. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit (Reference: Regulation No.3, Part B, Section III.E.) Facility Pollutants AIRS Point Control Device Equipment ID Controlled Six(6) Leeds 30-0011 enclosed flares. CNDTK-1 005 The flares have a minimum control VOC, HAPs efficiency of 95%. Six(6) Leeds 30-0011 enclosed flares. PW 006 The flares have a minimum control VOC, HAPs efficiency of 95%. Vapor balancing and six(6) Leeds 30- TLO 007 0011 enclosed flares. The flares have VOC, HAPs a minimum control efficiency of 95%. Open Flare for emergency only. 95% FL-2 009 minimum control efficiency. VOC, HAPs SEP-1 to SEP- Six(6) Leeds 30-0011 enclosed flares. 010 The flares have a minimum control VOC, HAPs 4 efficiency of 95%. Six(6) Leeds 30-0011 enclosed flares. VRT 011 The flares have a minimum control VOC, HAPs efficiency of 95%. PROCESS LIMITATIONS AND RECORDS 8. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Process Parameter Annual Limit AIRS ID: 123-9DA3 Page 3 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division Equipment Point ID CNDTK-1 005 Condensate Throughput 424,860 barrels PW 006 Produced Water Throughput 306,600 barrels TLO 007 Oil Loaded 424,860 barrels FL-2 009 Gas Vented from Sales Gas Line in case of 15.0 MMscf Emergency SEP-1 to 010 Gas Vented from Separators when Gas 5.0 MMscf SEP-4 Compressors are down VRT 011 Total Gas Vented from VRT when Gas 1.3 MMscf Compressors are down MNTK-1 015 Condensate Throughput 1000 barrels Compliance with the annual throughput Jimits 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. 9. Point 009, 010, and 011: The owner or operator shall continuously monitor and record the volumetric flow rate of natural gas vented from the separators and the vapor recovery towers and the sales gas line using a flow meter. The flow meter shall continuously measure flow rate and record total volumetric flow vented from each separator and vapor recovery tower and sales gas line. The owner or operator shall use monthly throughput records to demonstrate compliance with.the process and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 10. Point 005, 006, 009, 010, 011, and 015: The permit number and ten digit AIRS ID number assigned by the Division (e.g. 123/4567/001) shall be marked on the subject equipment for ease of identification. (Regulation Number 3, Part B, Section Ilhf.) (State only enforceable) 11. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 12. Point 005: This source is subject to Regulation Number 7, Section XII. The operator shall comply with all applicable requirements of Section XII and, specifically, shall: • Comply with the recordkeeping, monitoring, reporting and emission control requirements for condensate storage tanks; and • Ensure that the combustion device controlling emissions from this storage tank 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. (Regulation Number 7, Section XII.C.) (State only enforceable) 13. Point 009: The emergency open flare covered by this permit has been approved as an alternative emissions control device under Regulation Number 7, Section XVII.B.2.e. The open flare must have no visible emissions during normal operations and be designed so that an observer can, by means of visual observation from the outside of the open flare, or by other convenient means approved by the Division, determine AIRS ID: 123-9DA3 Page 4 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division whether it is operating properly. This open flare must be equipped with an operational auto-igniter according to the following schedule: • All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device; • All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 14. Point 005, 006, 007, 010, and 011: The combustion device covered by this permit is subject to Regulation Number 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. This flare must be equipped with an operational auto-igniter according to the following schedule: • All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device; • All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 15. Point 005, 006: The storage tank covered by this permit is subject to the emission control requirements in Regulation Number 7, Section XVII.C.1. The owner or operator shall 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 except where the combustion device has been authorized by permit prior to May 1, 2014. The source shall follow the inspection requirements of Regulation Number 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 requirement must be met within 90 days of the date that the storage tank commences operation. 16. Point 005, 006, and 015: The storage tanks covered by this permit are subject to the venting and Storage Tank Emission Management System ("STEM") requirements of Regulation Number 7, Section XVII.C.2. 17. Point 010: 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. 18. Point 005, 006, 007, 010, and 011: The flare(s) covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: AIRS ID: 123-9DA3 Page 5 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division XVII.B.2.b If a combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. XVII.B.2.d Auto-igniters: All combustion devices used to control emissions of hydrocarbons must be equipped with and operate an auto-igniter as follows: XVII.B.2.d.(i)All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device. XVII.B.2.d.(ii) All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 19. Point 007: 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) 20. Point 007: 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, I I I.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 the conditions (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. Point 007: 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 22. Point 005, 006, 007, 010, and 011: 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 AIRS ID: 123-9DA3 Page 6 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division 23. Point 005, 006, 007, 009, 010, and 011: The owner or operator shall demonstrate compliance with opacity standards, using EPA Reference Method 22, 40 C.F.R. Part 60, Appendix A, 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 minute in any fifteen minute period during normal operation. (Regulation Number 7, Sections XII.C, XVII.B.2. and XVII.A.16) ADDITIONAL REQUIREMENTS 24. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOX) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 25. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 26. This permit and any attachments must be retained and made available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. AIRS ID: 123-9DA3 Page 7 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division • 27. 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. 28. 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. 29. 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. 30. 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. 31. 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. 32. 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: Kirk Bear Permit Engineer AIRS ID: 123-9DA3 Page 8 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company, LLC AIRS ID: 123-9DA3 Page 9 of 14 • Colorado Department of Public Health and Environment Air Pollution Control Division Notes to Permit Holder at the time of this permit issuance: 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 tothe invoice will result in revocation of this permit (Reference: P pay 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.aov/cs/SStellite?c=Document C&childpaaename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=12515993896418magename=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 Are the Controlled AIRS Emissions emissions Emissions Point Pollutant CAS# (lb/yr) reportable? (Ib/yr) 005 Benzene 71432 850 Yes 43 005 Xylenes 1330207 425 Yes 22 005 n-Hexane 110543 3824 Yes 192 005 224 TMP 540841 850 Yes 43 006 Benzene 71432 2147 Yes 108 006 n-Hexane 110543 6746 Yes 338 007 n-Hexane 110543 3035 Yes 1014 007 Benzene 71432 261 Yes 87 009 Benzene 71432 504 Yes 26 009 Toluene 108883 460 Yes 23 . 009 Xylenes 1330207 269 Yes 14 009 n-Hexane 110543 3530 Yes 177 009 224 TMP 540841 503 Yes 26 010 Benzene 71432 1703 Yes 86 010 Toluene 18883 1119 Yes 56 010 Xylenes 1330207 303 Yes 16 010 n-Hexane 110543 12792 Yes 640 AIRS ID: 123-9DA3 Page 10 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division 010 224 TMP 540841 1578 Yes 79 011 Benzene 71432 896 Yes 45 011 n-Hexane 110543 4779 Yes 239 011 Toluene 108883 630 Yes 31 011 224 TMP 540841 397 Yes 20 5) The emission levels contained in this permit are based on the following emission factors: Point 005: Emission Factors Pollutant Uncontrolled Source lb/bbl Condensate Throughput VOC 0.34 sample/Promax NOx 0.068 lb/MMBtu AP-42 CO 0.310 lb/MMBtu AP-42 n-Hexane 0.009 sample/Promax Benzene 0.002 sample/Promax 224 TMP 0.002 sample/Promax Xylenes 0.001 sample/Promax Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 006: 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 007: Emission Factors-Uncontrolled Pollutant lb/bbl loaded Source VOC 0.2246 AP-42/Promax NOx 0.0068 lb/MMBtu AP-42/Promax CO 0.310 lb/MMBtu AP-42/Promax Benzene 0.0006 AP-42/Promax n-Hexane 0.0072 AP-42/Promax 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: dedicated vapor balance service) P (true vapor pressure) =4.22 psia AIRS ID: 123-9DA3 Page 11 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division M (vapor molecular weight)=55.3 Ib/Ib-mol T(temperature of liquid loaded)= 524°R The uncontrolled non-criteria reportable air pollutant(NCRP)emission factors were calculated by a site specific sample ran through Promax. Point 009: Weight Emission Emission Factors Factors Pollutant Fraction of Source Gas(%) Uncontrolled Controlled Ib/MMscf Ib/MMscf NOx — 0.068 lb/MMBtu NA AP-42 CO — 0.31 lb/MMBtu NA AP-42 VOC 27.78 16767.6 838.4 Promax Benzene 0.056 33.6 1.68 Promax Toluene 0.051 30.6 1.53 Promax Ethylbenzene 0.018 10.7 0.54 Promax Xylenes 0.030 17.9 0.90 Promax n-hexane 0.390 235.6 11.78 Promax 224 TMP 0.055 33.5 1.68 Promax Point 010: Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas Uncontrolled Controlled (%) Ib/MMscf Ib/MMscf NOx(lb/MMBTU) -- 0.068 NA AP-42 CO(lb/MMBTU) -- 0.310 NA AP-42 VOC 83.5939 122854.4 6142.7 Promax Benzene 0.2317 340.6 17.1 Promax Toluene 0.1522 223.7 11.2 Promax Ethylbenzene 0.0294 43.2 2.2 Promax Xylenes 0.0411 60.5 3.0 Promax n-hexane 1.7408 . 2558.4 127.9 Promax 224 TMP 0.118 315.2 15.8 Promax Point 011: Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas Uncontrolled Controlled (%) Ib/MMscf . Ib/MMscf NOx(Ib/MMBTU) — 0.068 0.068 AP-42 CO(lb/MMBTU) — 0.31 0.31 AP-42 VOC 77.06 106345.7 5317.3 Promax Benzene 0.499 689.0 34.5 Promax Toluene 0.351 484.5 24.2 Promax Ethylbenzene 0.051 70.2 3.5 Promax Xylenes 0.139 191.9 9.6 Promax n-hexane 2.664 3676.5 183.8 Promax 224 TMP 0.222 305.4 15.3 Promax AIRS ID: 123-9DA3 Page 12 of 14 Colorado Department of Public Health and Environment Air Pollution Control Division Point 015' Emission Factors Pollutant Uncontrolled Source lb/bbl Condensate Throughput VOC 3.74 Promax n-Hexane 0.18 Promax Benzene 0.03 Promax Toluene 0.03 Promax Ethylbenzene 0.004 Promax Xylenes 0.01 Promax 224 TMP 0.02 Promax Note: The controlled emissions for this point are based on the flare control efficiency of 95%. 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 HAPs NANSR Synthetic Minor Source of: VOC and HAPs MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM AIRS ID: 123-9DA3 Page 13 of 14 '"VNNI • Colorado Department of Public Health and Environment Air Pollution Control Division 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: 123-9DA3 Page 14 of 14 Division Information Engineer: Kirk Bear Control Engineer: Christopher Laplante Review Date: 12/16/2015 Application Date: 06/10/2015 • Facility Identifiers Permit No. 15WE1108 Potentially located in ozone nonattainment area AIRS County# 123 (Weld Facility# 9DA3 Facility Type:exploration and production facility ❑� Located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: r..;•-VOC r NOx r co Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Pronghom F-22 Production Facility Source Location: NWNW,Section 22,T5N,R61W SIC: 1311 Mailing Address 1: Bonanza Creek Energy Operating Company LLC Address Address 2: 410 17th Street,Suite 1500 ity,State Zip: Denver,Colorado 80202 Name: Jerry Dismukes Person To Phone: 303 803 1724 Contact Fax: 720 305 0804 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 Pronghom F-22 Production Facility,located in the NWNW,Section 22,T5N,R61W,Weld County,Colorado. Point Name Type Control Action Newly 005 CNDTK-1 Condensate Tanks Flare reported source Newly 006 PW Water Tanks Flare reported source Newly 007 TLO Loadout Flare reported source Newly 009 FL-2 Separator Venting Flare reported source SEP-1 to Newly 010 SEP-4 Separator Venting Flare reported source Newly 011 VRT Separator Venting Flare reported source Newly 012 Sand Sep-1 Separator Venting None reported source Newly 013 P-1 Separator Venting Flare reported source Newly 014 P-2 Separator Venting Flare reported source Newly 015 MNTK-1 Condensate Tanks None reported source 015 One(1)above ground 500 barrel maintenance tank Requsted Throughput 1000 bbl Control No Control I Efficiency 0.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 3.74 lb/bbl 1.9 tpy 1.9 tpy promax Benzene 0.03 lb/bbl 30 lb/yr 30 lb/yr promax n-Hexane 0.18 Ib/bbl - 180 lb/yr 180 lb/yr promax toulene 0.03,lb/bbl 30 lb/yr 30 lb/yr promax xylene 0.01 lb/bbl 10 lb/yr 10 lb/yr promax e-benzene 0.004 lb/bbl 4 lb/yr 4 lb/yr promax 224 0.02 lb/bbl 20 lb/yr 20 lb/yr promax Regulatory Review Section II.A1 -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 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. NSPS Kb: for storage vessels greater than 19,800-gallons after 7/23/84. This source is not subject because each tank is before custody transfer NSPS 0000:for storage vessels in the natural gas production,transmission,and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. 7 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 not currently subject to this since actual uncontrolled emissions are less than 20 tpy of VOC.) 014 One Sandpiper G1 F natural gas driven pneumatic pump used for water transfer Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(Q) 5.3 MMscf/yr 605.0228311 scf/hr MW 22.91 Ib/Ib-mol 0.014520548 MMscf/d mole% MW Ib dlbmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.37 44.01 1.044 0.046 1.67 14605.70 7.30 N2 0.88 28.013 0.246 0.011 0.39 3439.07 1.72 methane 72.32 16.041 11.602 0.506 18.52 162237.46 81.12 ethane 12.03 30.063 3.618 0.158 5.78 50592.93 25.30 propane 7.93 44.092 3.495 0.153 5.58 48877.70 24.44 isobutane 0.76 58.118 0.441 0.019 0.70 6165.38 3.08 n-butane 2.34 58.118 1.362 0.059 2.17 19042.31 9.52 isopentane 0.40 72.114 0.292 0.013 0.47 4078.19 2.04 n-pentane 0.50 72.114 0.363 0.016 0.58 5082.61 2.54 cyclopentane 0.05 70.13 0.034 0.001 0.05 471.72 0.24 n-Hexane 0.10 86.18 0.089 0.004 0.14 1247.34 0.62 cyclohexane 0.04 84.16 0.031 0.001 0.05 428.39 0.21 Other hexanes 0.15 86.18 0.129 0.006 0.21 1800.50 0.90 heptanes 0.03 100.21 0.028 0.001 0.04 389.58 0.19 methylcyclohexane 0.02 98.19 0.024 0.001 0.04 330.92 0.17 224-TMP 0.01 114.23 0.013 0.001 0.02 177.31 0.09 Benzene 0.02 78.12 0.013 0.001 0.02 178.07 0.09 Toluene 0.01 92.15 0.012 0.001 0.02 162.37 0.08 Ethylbenzene 0.00 106.17 0.004 0.000 0.01 56.42 0.03 Xylenes 0.01 106.17 0.007 0.000 0.01 95.02 0.05 C8+Heavies 0.01 469.0584071 0.066 0.003 0.10 918.31 0.46 VOC mass fract 0.279 Total VOC(Uncontrolled) 44.75 Notes Mole°/0,MW,and mass fractions for the gas are from Sales Gas analysis Pronghorn K21-024-22HNC&Pronghorn K-O-22HNB collected 4/10/2015. Emissions are based on 8760 hours of operation per year. 15WE1108.CP1.xlsm 014 One Sandpiper G1 F natural gas driven pneumatic pump used for water transfer Flaring Information Equipment Description Flare Manufacturer Leed Model 30-0011 Serial Number TBD Gas Heating Value 1307 Btu/scf Throughput 6927.1 MMBtu/yr VRU Information Equipment Description Not Applicable Make NA Model NA Requested Control NA Annual Bypass Ti NA Backup NA Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 jlb NOX/MMBtu 0.37 alb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18788 lb/MMscf 838.38 Ib/MMsd 44.4 tpy 2.2 tpy Gas Analysis Nox 0.07 lb/MMBTU 0.07 Ib/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 1.3 tpy 1.3 tpy AP-42 Benzene 33.8 lb/MMscf 1.68 Ib/MMsd 178 lb/yr 9 lb/yr Gas Analysis n-Hexane 235.8 lb/MMsd 11.7800 lb/MMscf 1249 lb/yr 62 lb/yr Gas Analysis Toluene 30.8 Ib/MMsd 1.5300 Ib/MMsd 162 lb/yr 8 lb/yr Gas Analysis Xylenes 17.9 Ib/MMsd 0.8950 lb/MMscf 95 lb/yr 5 lb/yr Gas Analysis Ethylbenzene 10.7 lb/MMscf 0.5350 Ib/MMsd 57 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 Reaulation Z Section IA 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 Reaulation 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 XVlI.B.2 15WE1108.CP1.xism 013 One Sandpiper G1F natural gas driven pneumatic pump used for water transfer Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x O=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 5.3 MMscf/yr 605.0228311 scf/hr MW 22.91 Ib/Ib-mol 0.014520548 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.37 44.01 1.044 0.046 1.67 14605.70 7.30 N2 0.88 28.013 0.246 0.011 0.39 3439.07 1.72 methane 72.32 16.041 11.602 0.506 18.52 162237.46 81.12 ethane 12.03 30.063 3.618 0.158 5.78 50592.93 25.30 propane 7.93 44.092 3.495 0.153 5.58 48877.70 24.44 isobutane 0.76 58.118 0.441 0.019 0.70 6165.38, 3.08 n-butane 2.34 58.118 1.362 0.059 2.17 19042.31 9.52 isopentane 0.40 72.114 0.292 0.013 0.47 4078.19 2.04 n-pentane 0.50 72.114 0.363 0.016 0.58 5082.61 2.54 cyclopentane 0.05 70.13 0.034 0.001 0.05 471.72 0.24 n-Hexane 0.10 86.18 0.089 0.004 0.14 1247.34 0.62 cyclohexane 0.04 84.16 0.031 0.001 0.05 428.39 0.21 Otherhexanes 0.15 86.18 0.129 0.006 0.21 1800.50 0.90 heptanes 0.03 100.21 0.028 0.001 0.04 389.58 0.19 methylcyclohexane 0.02 . 98.19 0.024 0.001 0.04 330.92 0.17 224-TMP 0.01 114.23 0.013 0.001 0.02 177.31 0.09 Benzene 0.02 78.12 0.013 0.001 0.02 178.07 0.09 Toluene 0.01 92.15 0.012 0.001 0.02 162.37 0.08 Ethylbenzene 0.00 106.17 0.004 0.000 0.01 56.42 0.03 • Xylenes 0.01 106.17 0.007 0.000 0.01 95.02 0.05 C8+Heavies 0.01 469.0584071 0.066 0.003 0.10 918.31 0.46 VOC mass frac 0.279 Total VOC(Uncontrolled) 44.75 Notes Mole%,MW,and mass fractions for the gas are from Sales Gas analysis Pronghorn K21-024-22HNC&Pronghorn K-O-22HNB collected 4/10/2015. Emissions are based on 8760 hours of operation per year. • 15WE1108.CP1.xlsm 013 One Sandpiper G1F natural gas driven pneumatic pump used for water transfer Flaring Information Equipment Description Flare Manufacturer Leed Model 30-0011 Serial Number TBD Gas Heating Value 1307 Btu/sd Throughput 6927.1 MMBtu/yr VRU Information Equipment Description Not Applicable Make NA Model NA Requested Control NA Annual Bypass Ti NA 1 Backup NA Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 lib NOX/MMBtu 0.37 lIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 16768 lb/MMscf 838.38 lb/MMscf 44.4 tpy 2.2 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.2 tpy 0.2 tpy AP-42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 1.3 tpy 1.3 tpy AP-42 Benzene 33.6 lb/MMscf 1.68 Ib/MMsd 178 lb/yr 9 lb/yr Gas Analysis n-Hexane 235.6 Ib/MMsd 11.7800 Ib/MMsd 1249 lb/yr 62 lb/yr Gas Analysis Toluene 30.6 lb/MMscf 1.5300 Ib/MMsd 162 lb/yr 8 lb/yr Gas Analysis Xylenes 17.9Ib/MMsd 0.8950,Ib/MMsd 95 lb/yr 5 lb/yr Gas Analysis Ethylbenzene 10.7 lb/MMscf 0.5350 lb/MMscf _ 57 lb/yr 3 lb/yr Gas Analysis Regulatory Applicability AQCC Reaulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AOCC Reaulation Z Section LA 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." AOCC Reaulation 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 15WE1108.CP1xlsm - r 012 Four blowdown sand separators Equipment Description This source vents natural gas from: Fuel/Sales gas lines Emissions from this source are: vented to the atmosphere Natural gas venting from Fuel/Sales qas lines.Emissions from this source are vented to the atmosphere. 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 rateNolume 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) 0.1 MMscf/yr 11.41552511 scf/hr MW 22.9 Ib/Ib-mol 0.000273973 MMscf/d mole% MW lbx/lbmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.37 44.01 1.044 0.046 0.03 275.58 0.14 N2 0.88 28.013 0.246 0.011 0.01 64.89 0.03 methane 72.32 16.041 11.602 0.507 0.35 3061.08 1.53 ethane 12.03 30.063 3.618 0.158 0.11 954.58 0.48 propane 7.93 44.092 3.495 0.153 0.11 922.22 0.46 isobutane 0.76 58.118 0.441 0.019 0.01 116.33 0.06 n-butane 2.34 58.118 1.362 0.059 0.04 359.29 0.18 isopentane .0.40 72.114 0.292 0.013 0.01 76.95 0.04 n-pentane 0.50 72.114 0.363 0.016 0.01 95.90 0.05 cyclopentane 0.05 70.13 0.034 0.001 0.00 8.90 0.00 n-Hexane 0.10 86.18 0.089 0.004 0.00 23.53 0.01 cyclohexane 0.04 84.16 0.031 0.001 0.00 8.08 0.00 Other hexanes 0.15 86.18 0.129 0.006 0.00 33.97 0.02 heptanes 0.03 100.21 0.028 0.001 0.00 7.35 0.00 methylcyclohexane 0.02 98.19 0.024 0.001 0.00 6.24 0.00 224-TMP 0.01 114.23 0.013 0.001 0.00 3.35 0.00 Benzene 0.02 78.12 0.013 0.001 0.00 3.36 0.00 Toluene 0.01 92.15 0.012 0.001 0.00 3.06 0.00 Ethylbenzene 0.00 106.17 0.004 0.000 0.00 1.06 0.00 Xylenes 0.01 106.17 0.007 0.000 0.00 1.79 0.00 C8+Heavies 0.01 397.6298357 0.056 0.002 0.00 14.69 0.01 100.00 VOC mass tract 0.279 Total VOC(Uncontrolled) • 0.84 Notes Mole%,MW,and mass fractions for the gas are from Sales Gas analysis Pronghom K21-024-22HNC&Pronghorn K-O-22HNB collected 4/10/2015. Emissions are based on 720 blowdowns events per year in total.3 seconds/gas blowdown&15 seconds/liquid blowdown event. Mole%,MW,and mass fractions for the oil/water(flashing)are from Promax using an average condensate analysis 15WE1108.CP1.xlsm 012 Four blowdown sand separators Flaring Information Equipment Description Manufacturer Model Serial Number Gas Heating Value 1307 Btu/scf Throughput 130.7 MMBtu/yr VRU Information Equipment Description Not Applicable Make NA Model NA number of blowdowns Requested Control NA 720 Annual Bypass Ti NA Backup NA Overall Control 0.00% Combustion emission factor source: AP-42:Chapter 13.5 0.00 (lb NOX/MMBtu 0.00 (lb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 5.34 lb/blowdown lb/MMscf 19 tpy tpy Gas Analysis/Promax Nox 0.00 lb/blowdown Ib/MMBTU 0.0 tpy tpy CO 0.00 lb/blowdown Ib/MMBTU 0.0 tpy tpy Benzene 0.05 lb/blowdown lb/MMscf ,' 36 lb/yr lb/yr Gas Analysis/Promax n-Hexane 0.29 lb/blowdown lb/MMscf 209 lb/yr lb/yr Gas Analysis/Promax Toluene 0.050 lb/blowdown lb/MMscf 36 lb/yr lb/yr Gas Analysis/Promax Xylenes 0.020 lb/blowdown Ib/MMscf 14 lb/yr lb/yr Gas Analysis/Promax Ethylbenzene 0.010 lb/blowdown Ib/MMscf 7 lb/yr lb/yr Gas Analysis/Promax Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section IIA5:'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 ReOuladon_2 Section l.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 m 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 Reaulalion 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 15WE110B.CPlxlsm Two VRT's controlled by six enclosed flares when the gas compressors are down. The flares have a 95% 011 control efficiency. Equipment Description This source vents natural gas from: Two VRT's when the compressors are down. Emissions from this source are: routed to a flare Natural gas venting from Two VRT's when the compressors are down..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) 1.3 MMscf/yr 148.4018265 scf/hr MW 52.3 Ib/Ib-mol 0.003561644 MMscf/d mole% MW lbx/lbmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 0.90 44.01 0.395 0.008 0.15 1356.20 0.68 N2 0.27 28.013 0.076 0.001 0.03 261.45 0.13 methane 16.25 16.041 2.607 0.050 1.02 8942.10 4.47 ethane 22.65 30.063 6.809 0.130 2.67 23355.61 11.68 propane 31.62 44.092 13.942 0.267 5.46 47820.58 23.91 isobutane 3.35 58.118 1.949 0.037 0.76 6685.98 3.34 n-butane 12.85 58.118 7.468 0.143 2.92 25616.59 12.81 • isopentane 2.30 72.114 1.660 0.032 0.65 5692.42 2.85 n-pentane 2.78 72.114 2.002 0.038 0.78 6867.12 3.43 cyclopentane 0.85 70.13 0.595 0.011 0.23 2040.12 1.02 n-Hexane 1.33 86.18 1.148 0.022 0.45 3938.63 1.97 cyclohexane 0.43 84.16 0.360 0.007 0.14 1235.82 0.62 Otherhexanes 2.39 86.18 2.062 0.039 0.81 7073.51 3.54 heptanes 0.73 100.21 0.736 0.014 0.29 2524.00 1.26 methylcyclohexane 0.29 98.19 0.282 0.005 0.11 968.64 0.48 224-TMP 0.08 114.23 0.095 0.002 0.04 327.17 0.16 Benzene 0.28 78.12 0.215 0.004 0.08 737.96 0.37 Toluene 0.16 92.15 0.151 0.003 0.06 519.01 0.26 Ethylbenzene 0.02 106.17 0.022 0.000 0.01 75.02 0.04 Xylenes 0.06 106.17 0.060 0.001 0.02 205.39 0.10 C8+Heavies 0.40 2392.190714 9.664 0.185 3.78 33149.83 16.57 VOC mass frail 0.811 Total VOC(Uncontrolled) 7274 Notes based on a site specific analysis run through promax Emissions are based on 8760 hours of operation per year. molecular weight based on a sample ran through promax 15WE1108.CP1.xlsm Two VRT's controlled by six enclosed flares when the gas compressors are down. The flares have a 95% 011 control efficiency. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Leed Model 30-0011 Serial Number Gas Heating Value 2908 Btu/scf Throughput 3780.4 MMBtu/yr VRU Information NA Equipment Description Engine to recompress gas to sales line. Make Model Requested Control Efficiency Annual Bypass Time Backup I Flare • Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 j lb NOX/MMBtu 0.31 llb CO/MMBtu Emissions Summary Table . Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 106346 Ib/MMscf 5317.29 Ib/MMscf 69.1 tpy 3.5 tpy promax Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.1 tpy 0.1 tpy AP-42 CO 0.31 Ib/MMBTU 0.31 Ib/MMBTU 0.6 tpy 0.6 tpy AP-42 Benzene 689.00 Ib/MMscf 34.45 lb/MMscf` 896 lb/yr 45 lb/yr promax n-Hexane 3676.50 lb/MMscf 183.8250lb/MMscf 4779 lb/yr 239 lb/yr promax Toluene 484.500 lb/MMscf 24.2250 lb/MMscf 630 lb/yr 31 lb/yr promax Xylenes 191.900 lb/MMscf 9.5950Ib/MMscf 249 lb/yr 1.2 lb/yr promax Ethylbenzene 70.200Ib/MMscf 3.5100 Ib/MMscf 91 lb/yr 5 lb/yr promax • 224 305.4Ib/MMscf 15.2700Ib/MMscf ( 397 lb/yr 20 lb/yr promax Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A5:'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 XVI1.B.2 15WE1108.CP1.xlsm 010 Four low pressure separators controlled by six enclosed flares when the gas compressors are down. Equipment Description This source vents natural gas from: four well head separator Emissions from this source are: routed to a flare Natural gas venting from four well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW`Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 5 MMscf/yr 570.7762557 scf/hr MW 46.4 Ib/Ib-mol 0.01369863 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.0000 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.9294 44.01 1.289 0.028 1.94 17008.30 8.50 N2 0.2249 28.013 0.063 0.001 0.09 831.15 0.42 methane 43.3001 16.041 6.946 0.150 10.46 91632.84 45.82 ethane 21.0968 30.063 6.342 0.137 9.55 83671.91 41.84 propane 19.6924 44.092 8.683 0.187 13.08 114548.46 57.27 isobutane 2.1044 58.118 1.223 0.026 1.84 16135.03 8.07 n-butane 6.6615 58.118 3.872 0.083 5.83 51075.60 25.54 isopentane 1.1869 72.114 0.856 0.018 1.29 11291.83 5.65 n-pentane 1.4937 72.114 1.077 0.023 1.62 14210.64 7.11 cyclopentane 0.1447 70.13 0.101 0.002 0.15 1338.76 0.67 n-Hexane 0.3123 86.18 0.269 0.006 0.41 3551 1.78 cyclohexane 0.0997 84.16 0.084 0.002 0.13 1107 0.55 Other hexanes 0.4450 86.18 0.384 0.008 0.58 5059 2.53 heptanes 0.0791 100.21 0.079 0.002 0.12 1046 0.52 methylcyclohexane 0.0679 98.19 0.067 0.001 0.10 880 0.44 224-TMP 0.0323 114.23 0.037 0.001 0.06 487 0.24 Benzene 0.0497 78.12 0.039 0.001 0.06 512 0.26 Toluene 0.0348 92.15, 0.032 0.001 0.05 423 0.21 Ethylbenzene 0.0070 106.17 0.007 0.000 0.01 98 0.05 Xylenes 0.0112 106.17 0.012 0.000 0.02 157 0.08 C8+Heavies 0.0261 57234.3532 14.938 0.322 22.50 197073 98.54 99.9999 VOC mass fracl 0.684 Total VOC(Uncontrolled) 209.50 Notes 15WE1108.CP1.xlsm 010 Four low pressure separators controlled by six enclosed flares when the gas compressors are down. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Leed Model Serial Number Gas Heating Value 2636 Btu/scf Throughput 13180 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make TBD Model TBD Requested Control 0.00% Annual Bypass Ti 100.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 llb NOX/MMBtu 0.37 lib CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 122854.4 lb/MMscf 6142.72 lb/MMscf 307.1 tpy 15.4 tpy Gas Analysis Nox 0.1 Ib/MMBTU 0.15 Ib/MMBTU 0.4 tpy 0.4 tpy AP-42 CO 0.4 Ib/MMBTU 0.37 Ib/MMBTU 2.4 tpy 2.4 tpy AP-42 Benzene 340.8 lb/MMscf 17.03 lb/MMscf 1703 lb/yr 85 lb/yr Gas Analysis n-Hexane 2558.4 lb/MMscf 127.9200 lb/MMscf 12792 lb/yr 640 lb/yr Gas Analysis Toluene 223.7 lb/MMfcf 11.1840 lb/MMscf 1118 lb/yr 56 lb/yr Gas Analysis Xylenes 80.5 lb/MMscf 3.0240 lb/MMscf 302 lb/yr 15 lb/yr Gas Analysis Ethylbenzene 43.2 lb/MMscf 2.1600 lb/MMscf 216 lb/yr 11 lb/yr Gas Analysis 224 315.2 lb/MMscf 15.7620 lb/MMscf 1576 lb/yr 79 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$ 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 15WE1108.CP1.xlsm One open flare used to control sales gas in case of emergency. Flare has a minimum control efficiency of 009 95%. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 15 MMscf/yr 1712.328767 scf/hr MW 22.9 Ib/Ib-mol 0.04109589 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lbyr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0 0.00 CO2 2.37 44.01 1.044 0.046 4.72 41337 20.67 N2 0.88 28.013 0.246 0.011 1.11 9733 4.87 methane 72.32 16.041 11.602 0.507 52.42 459163 229.58 ethane 12.03 30.063 3.618 0.158 16.35 143188 71.59 propane 7.93 44.092 3.495 0.153 15.79 138333 69.17 isobutane 0.76 58.118 0.441 0.019 1.99 17449 8.72 n-butane 2.34 58.118 1.362 0.059 6.15 53893 26.95 isopentane 0.40 72.114 0.292 0.013 1.32 11542 5.77 n-pentane 0.50 72.114 0.363 0.016 1.64 14385 7.19 cyclopentane 0.05 70.13 0.034 0.001 0.15 1335 0.67 n-Hexane 0.10 86.18 0.089 0.004 0.40 3530 1.77 cyclohexane 0.04 84.16 0.031 0.001 0.14 1212 0.61 Other hexanes 0.15 86.18 0.129 0.006 0.58 5096 2.55 heptanes 0.03 100.21 0.028 0.001 0.13 1103 0.55 methylcyclohexane 0.02 98.19 0.024 0.001 0.11 937 0.47 224-TMP 0.01 114.23 0.013 0.001 0.06 502 0.25 Benzene 0.02 78.12 0.013 0.001 0.06 504 0.25 Toluene 0.01 92.15 0.012 0.001 0.05 460 0.23 Ethylbenzene 0.00 106.17 0.004 0.000 0.02 160 0.08 Xylenes 0.01 106.17 0.007 0.000 0.03 269 0.13 C8+Heavies 0.01 397.6298357 0.056 0.002 0.25 2203 1.10 100.00 VOC mass frad 0.279 Total VOC(Uncontrolled) 126.46 Notes 15WE1108.CP1.xlsm One open flare used to control sales gas in case of emergency. Flare has a minimum control efficiency of 009 95%. Flaring Information Equipment Description Manufacturer Model • Serial Number Gas Heating Value 1307 Btu/scf Throughput 19605 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make - Model Requested Control 0.00% Annual Bypass Ti 100.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMBtu 0.37 l lb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 18861 lb/MMscf 843.04 Ib/MMscf 126.5 tpy 6.3 tpy promax Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.7 tpy 0.7 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 3.6 tpy 3.6 tpy AP-42 Benzene 33.60 lb/MMscf 1.68lb/MMscf 504 lb/yr 25 lb/yr promax n-Hexane 235.35lb/MMscf 11.7673 lb/MMscf 3530 lb/yr 177 lb/yr promax Toluene 30.836lb/MMscf 1.5318 lb/MMscf 460 lb/yr 23 lb/yr promax Xylenes 17.928lb/MMscf 0.8964lb/MMscf 269 lb/yr 13 lb/yr promax Ethylbenzene 10.645lb/MMscf 0.5323lb/MMscf 160 lb/yr 8 lb/yr promax Regulatory Applicability AQCC Reaulation 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 Reaulation Z Section IA 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 Reaulation 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 15WE1108.CPLxism Hydrocarbon Loadout to Tanker Trucks. Loadout is controlled by using dedicatied vapor balance 007 service and an enclosed flare. Collection system is 70%efficient and the flare has a minimum control efficiency of 95%. Overall control efficiency is 66.5%. 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 4.22 psia promax M Molecular Weight of Var 53.3 lb/lb-mole promax T Liquid Temperature 524 deg.R Field Data L 5.35 lb/1000 gal 0.22 lb/bbl Annual requested Throughput 424860 bbl/yr 17844120 gal/yr Annual requested VOC emissions 95438 lb/yr 47.7 tpy Control: Flare Efficiency: 66.60% NCRPs Component Mass Fraction of VOC If the operator provides HAP speciation from a stable"sales oil" Benzene 0.2730 analysis,enter the mass fraction from this data. Alternatively,if n-hexane 3.1803 the operator modeled a pressurized oil to develop a site specific emissions factor,enter the modeled mass fraction for the Toluene Xylenes Source: Pressurized oil or Stable Sales Oil Analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2246 lb/bbl 47.7 tpy 15.9 tpy AP-42 Benzene 0.0006 lb/bbl 261 lb/yr 87 lb/yr AP-42 n-Hexane 0.0071 lb/bbl 3035 lb/yr 1014 lb/yr AP-42 Toluene 0.0000 lb/bbl 0 lb/yr 0 lb/yr AP-42 Xylenes 0.0000 lb/bbl 0 lb/yr 0 lb/yr AP-42 Regulatory Review 'Regulation 3 APEN and Permitting Requirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day of crude oil on an annual average basis? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 006 Two(2) 1100 barrel above ground atmospheric produced water storage tanks controlled by an enclosed flare. The flare has a minimum control efficiency of 95%. Emissions Calculations Requsted Throughput 306600 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.262 lb/bbl 40.1646 tpy 2.00823 tpy CDPHE Benzene 0.007 lb/bbl 2146.2 lb/yr '107.31 lb/yr CDPHE n-Hexane 0.022 lb/bbl 6745.2 lb/yr 337.26 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) Raoul 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. 005 Twelve(12) 1100 barrel above ground atmospheric condensate storage tanks controlled by an enclosed flare. The flare has a minimum control efficiency of 95%. Requsted Throughput 424860 bbl Control Flare Efficiency _ 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.34 lb/bbl 72.2 tpy 3.6 tpy promax Benzene 0.002 lb/bbl 849.72 lb/yr 42.486 lb/yr promax n-Hexane 0.009 lb/bbl 3823.74 lb/yr 191.187 lb/yr promax toulene 0.0005 lb/bbl 212.43 lb/yr 10.6215 lb/yr promax ethyl benz 0.0005 lb/bbl 212.43 lb/yr 10.6215 lb/yr promax xylene 0.001 lb/bbl 424.86 lb/yr 21.243 lb/yr promax 224 0.002 lb/bbl 849.72 lb/yr 42.486 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. (only needed if using flare) Re ulation 2-Odor Section I.A- No person,wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is before custody transfer 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. 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U ;8 G7 a: ¢ U A N W W N � t_ a ''� C �j I C/)_ __ - V] C/] 4 -- -- --' V] V] E&P Storage Tank Air Pollutant Emissions Notice(APEN) Addendum Forml Company Name: Bonanza Creek Energy Operating Company,LLC Source Name: Pronghorn F-22 Production Facility(COGCC#437437) Emissions Source AIRS ID2: 123/9DA3/005 Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well 05-123-41162 Pronghorn O24-15-10XRLNB LEI 05-123-41161 Pronghorn J24-15-10XRLNC - - ❑ - ❑ 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 Form APCD-212 Form APCD-212-EP-StorageTank-APEN-Addendum_Condensate.docx \ W .•. 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