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Home My WebLink About20142204.tiff STATE OF COLORADO John W.Hickenlooper,Governor by•Co� Larry Wolk, MD,MSPH p _o,- Executive Director and Chief Medical Officer yt, rQ o, Dedicated to protecting and improving the health and environment of the people of Colorado .}- * 4300 Cherry Creek Dr.S. Laboratory Services Division ia7s Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Weld County- Clerk to the Board 1150 O St PO Box 758 • Greeley, CO 80632 July 9, 2014 Dear Sir or Madam: On July 15, 2014, the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—Pronghorn P-8, in the The Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty(30) days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health &Environment APCD-SS-B I 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, , / t RECEIVED Clara Gonzales JUL $ 2��§ Public Notice Coordinator Stationary Sources Program Air Pollution Control Division WELD COUNTY COMMISSIONERS Enclosure ��blXv p\QUinl.) et: ( t /mMrr)&L o) 23 PIA) (ci, Cb,i-m) -7 - l8-j9 2014-2204 • • STATE OF COLORADO John W.Hickenlooper,Governor pe cod Larry Wolk,MD,MSPH 0 0,� Executive Director and Chief Medical Officer �'� '� Dedicated to protecting and improving the health and environment of the people of Colorado P 9 P P <:(7,* ,71, �o . 4300 Cherry Creek Dr.S. Laboratory Services DivisionNt ir> Denver,Colorado 80246-1530 8100 Lowry Blvd. fan Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy Operating Company LLC—Pronghorn P-8— Weld County Released To: The Greeley Tribune On: July 9, 2014 Published: July 15, 2014 PUBLIC NOTICE OF A PROPOSED PROJECT OR ACTIVITY WARRANTING PUBLIC COMMENT 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 P-8 Wellpad NWNE Section 8 T5N R61 W Weld County The proposed project or activity is as follows: Bonanza Creek is operating a wellhead facility in Weld County. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B,Section IILC due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.I.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 14WE0160 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 www.colorado.gov/cdphe/AirPublicNotices 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: • Peter Armington Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South,APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us ILT STATE OF COLORADO �6F �A COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692-3150 .et 8]6 CONSTRUCTION PERMIT PERMIT NO: 14WE0160 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 P-8 Production Facility, located in the NWNE Section 8 T5N R61W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Point Description Equipment ID PW Tanks 002 One (1) above ground 400 bbl and one (1) 60 bbl vault for produced water storage. TL 003 Truck Condensate Loadout FUG 004 Fugitive VOC leak emissions HLP Sep-1 005 Separator controlled by an enclosed flare. Flare has a minimum combustion efficiency of 95%. P-1 006 One(1)water transfer pump, rated at 600 scf/hr. Emergency gas emissions controlled by a candlestick flare. FL-1 007 Flare has a minimum combustion efficiency of 95%. The flare is not enclosed. Point 006: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: 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, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup AIRS ID: 123/9BC6 Page 1 of 14 Depa en li ealth and Environment it Pollution Control Division of the permiDolor en ality rol 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 issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The 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. Point 005: Within one-hundred and eighty (180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from the 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. 6. Point 007: The following information shall be provided to the Division within fifteen (15) days after issuance of permit. • 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 Equipment ID Point NOx VOC CO Type PW Tanks 002 - 0.4 — Point AIRS ID: 123/9BC6 Page 2 of 14 olor Depa I en v .Ii Health and Environment * it Pollution Control Division e TL w' x* ,: ` , s. ,,= s. --- Point FUG 004 --- 9.2 --- Fugitive HLP Sep-1 005 --- 10.8 2.9 Point P-1 006 --- 2.9 1.4 Point FL-1 007 --- 9.3 4.4 Point See "Notes to Permit Holder" for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 9. Point 004: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas analysis, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 10. 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 Point , Control Device Pollutants Equipment ID Controlled PW Tanks 002 Enclosedflare VOC HLP Sep-1 005 Enclosed Flare VOC P-1 006 Enclosed Flare VOC FL-1 007 Open Flare VOC PROCESS LIMITATIONS AND RECORDS 11. 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 AIRS ID: 12319BC6 Page 3 of 14 Dolor Depa en li ealth and Environment it Pollution Control Division Facility Equi ro mete Annual Limit PW Tanks 002 Produced Water Throughput 65,700 BBL TL 003 Oil Loaded 83,220 BBL HLP Sep-1 005 Gas Vented from Separator 8.0 MMSCF P-1 006 Natural Gas 5.3 MMSCF FL-1 007 Gas Vented from Separator 16.8 MMSCF 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. 12. Upon installation of the flow meter required under Condition 5, 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 13. 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) 14. 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.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. &4.) 15. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 16. Point 003: 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) 17. Point 003: 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): AIRS ID: 123/9BC6 Page 4 of 14 olor. A Depa en li Health and Environment it Pollution Control Division tit a. Hoses 'gs, v.', - = al ' fined event 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 17 (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. 18. Point 003: 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. 19. Point 004: This source is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. The operator shall comply with all applicable requirements of Section XII. 20. Point 004: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a quarterly basis. The first AVO inspection must occur within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: AIRS ID: 123/96C6 Page 5 of 14 Depa en li ealth and Environment it Pollution Control Division Dolor n t eene AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 21. 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 22. Point 004: Within one hundred and eighty days (180) after issuance of this permit, the owner or operator shall complete the initial extended gas analysis of gas samples that are representative of volatile organic compound (VOC) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 23. Point 004: Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 24. Point 005: The operator shall complete an initial site specific extended gas analysis of the natural gas vented from the low pressure separator in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4-trimethylpentane content (weight fraction) of this emission stream used in the permit application. Results of testing shall be used to determine site-specific emission factors using Division approved methods. Results of site-specific sampling and analysis shall be submitted to the Division as part of the self-certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. 25. Point 006: The owner or operator shall complete an initial extended wet gas analysis and submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. (Reference: Regulation No. 3, Part B, Section III.E.) AIRS ID: 123/9BC6 Page 6 of 14 olor f Dep a,Y en' . P .li Health and Environment Iiia ?it Pollution Control Division ... Periodic Tes :' , uir 26. Point 004: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples liquids that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 27. Point 006: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section IV.A and without applying for a revision to this permit or obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. 28. Point 006: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 29. Point 006: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 30. 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 ponattainment 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 AIRS ID: 123/9BC6 Page 7 of 14 olor Depa en li ealth and Environment it Pollution Control Division e. No lot d e e ' N e 31. 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). 32. MACT Subpart HH - National Emission Standards for Hazardous Air Pollutants From Oil and Natural Gas Production Facilities major stationary source requirements shall apply to this stationary source at any such time that this stationary source becomes major solely by virtue of a relaxation in any permit limitation and shall be subject to all appropriate applicable requirements of Subpart HH. (Reference: Regulation No. 8, Part E) GENERAL TERMS AND CONDITIONS 33. 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. 34. 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. 35. 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. 36. 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. 37. 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 AIRS ID: 123/9BC6 Page 8 of 14 olor Depa en • P .li rHealth and Environment s it Pollution Control Division permit, condit it ted . =9- 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. 38. 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. 39. 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: Peter Armington Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BC6 Page 9 of 14 De.pa en li ealth and Environment it Pollution Control Division Notes to Permit HolderDolor o e a 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.qov/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. AIRS Point Pollutant CAS# Uncontrolled Reportable Controlled Emissions Emissions (lb/yr) (Ib/yr) 002 Benzene 71432 459.9 Yes 23 n-Hexane 110543 1445.4 Yes 72.3 Benzene 71432 356.7 Yes 356.7 003 n-Hexane 110543 1588.9 Yes 1588.9 Toluene 108883 907.9 Yes 907.9 Ethylbenzene 100414 291.8 Yes 291.8 Xylenes 1330207 907.9 Yes 907.9 Benzene 71432 68.1 No 68.1 004 n-Hexane 110543 319.7 Yes 319.7 Toluene 108883 151 No 151 Ethylbenzene 100414 50.5 No 50.5 Xylenes 1330207 152.3 No 152.3 005 Benzene 71432 969.6 Yes 48.5 n-Hexane 110543 5952.1 Yes 297.6 Toluene 108883 614.7 Yes 30.7 006 Benzene 71432 55.2 No 2.8 n-Hexane 110543 772.1 Yes 38.6 007 Benzene 71432 176.6 No 8.8 n-Hexane 110543 2467.8 Yes 123.4 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Emission Factors Pollutant Uncontrolled Source lb/BBL Produced Water Throughput AIRS ID: 123/9BC6 Page 10 of 14 olor Depa en . - 'Ii Health and Environment •it Pollution Control Division r • Uncontrolled Pollutant Source lb/BBL Produced Water Throughput VOC 0.262 CDPHE n-Hexane 0.022 CDPHE Benzene 0.007 CDPHE Note: The controlled emissions factors for point 002 are based on the flare control efficiency of 95%. Point 003: Emission Factors - Uncontrolled Pollutant lb/BBL loaded Source VOC 0.39 AP-42 Benzene 0.004286015 AP-42 n-hexane 0.019092248 AP-42 Toluene 0.010909856 AP-42 Ethylbenzene 0.003506739 AP-42 Xylenes 0.010909856 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 = 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) = 10.16 psia M (vapor molecular weight) = 64 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 liquids by the VOC emission factor. • Point 004: Component Gas Service Light Oil Water/Oil Service Connectors 909 382 297 Flanges 41 10 12 Open-ended Lines 29 3 1 Pump Seals 2 0 1 Valves 131 51 35 Other* 62 8 12 VOC Content(wt. 0.3423 0.9977 1.000 fraction) Benzene Content(wt. 0.0002 0.0110 0.0012 fraction) Toluene Content(wt. 0.0001 0.0279 0.0003 fraction) Ethylbenzene (wt. 0.0001 0.0090 0.0001 AIRS ID: 123/9BC6 Page 11 of 14 olor Depa en li ealth and Environment it Pollution Control Division fraction) Xylenes Content(wt. 0.0001 0.0283 0.0001 fraction) n-hexane Content(wt. 0.0023 0.0488 0.0001 fraction) 'Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors (kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R95-017 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 005: Weight Emission CAS# Pollutant Fraction of Factors Source Gas(%) Uncontrolled (lb/mmscf) NOx 0.068 AP-42 lb/MMBtu CO _0.37 lb/MMBtu AP-42 • VOC 33.9 53778.3995 Engineering Calculation 71432 Benzene 0.14 121.1994 Engineering Calculation 108883 Toluene 0.09 76.8322 Engineering Calculation 100414 Ethylbenzene 0.01 10.9251 Engineering Calculation 1330207 Xylenes 0.02 16.8079 Engineering Calculation 110543 n-hexane 0.83 744.0131 Engineering Calculation Note: Controlled emission factors are based on a flare control efficiency of 95%. AIRS ID: 123/9BC6 Page 12 of 14 • k; °,' olor ,Depa en . P 'Ii Health" and Environment ' � it Pollution Control Division I dl. •Point 006: �s;t';•"w xrvn: ;;a3 ..iI . ...,. Emission Factors -Uncontrolled CAS# Pollutant lb/MMscf vented Source VOC 22207 All emission factors 108883 Toluene 8.8 are based on the 1330207 Xylenes 9.5 displacement 110543 n-Hexane 147 equation and the Pronghorn 41-11- 71432 Benzene 10.5 9HZ wet gas analysis. Note: Controlled emissions are based on a flare control efficiency of 95%. Point 007: Weight Emission CAS # Pollutant Fraction of Factors Source Gas(%) Uncontrolled (Ib/mmscf) NOx 0.068 AP-42 lb/MMBtu CO --- 0.37 lb/MMBtu AP-42 VOC 34.23 22206.4625 Engineering Calculation 71432 Benzene 0.02 10.5122 Engineering Calculation 108883 Toluene 0.01 8.7530 Engineering Calculation 100414 Ethylbenzene 0.01 2.2411 Engineering Calculation 1330207 Xylenes 0.01 9.5245 Engineering Calculation 110543 n-hexane 0.23 146.8926 Engineering Calculation Note: Controlled emissions are based on a 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, n-Hexane NANSR Synthetic Minor Source of: VOC AIRS ID: 123/9BC6 Page 13 of 14 Depa en li Health and Environment it Pollution Control Division 8) Full text of the TitlDolor ' f e is Co 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 DOD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart 7777-Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado.qov/cdphefoilqaspermits AIRS ID: 123/9BC6 Page 14 of 14 • Division Information • Engineer: Peter Armington Control Engineer: Stefanie Rucker Review Date: 03/11/2014 Application Date: 10/29/2013 Facility Identifiers Permit No. 14WE0160 AIRS County# 123 Weld Facility# 98C6 Facility Type: exploration and production facility E Located in the 8-hour non-attainment area? Q True Minor Synthetic Minor for: V0C F N0x r CO Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Pronghorn P-8 Production Facility Source Location: NWNE Section 8 T5N R61W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address Address 2: 410 17th Street, Suite 1500 ty, State Zip: Denver, CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@bonanzacrk.com 'Section 02: Requested Action Self Certification Required? Yes Issuance Number 1 Source Description: • Oil and gas exploration and production facility known as the Pronghorn P-8 Production Facility, located in the NWNE Section 8 T5N R61W, Weld County, Colorado. Point Name Type Control 002 PW Tanks Water Tanks Flare 003 TL Loadout None 004 FUG Fugitives None 005 HLP Sep-1 Separator Venting Flare 006 P-1 Pump Flare 007 FL-1 Separator Venting Flare 002 One(1) above ground 400 bbl and one(1)60 bbl vault for produced water storage. Emissions Calculations Pollutant E.F. Source VOC 0.262 lb/bbl CDPHE Benzene 0.007 lb/bbl CDPHE n-Hexane 0.022 lb/bbl CDPHE Requsted Throughput 65700 bbl • Control O No Control ®Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 8.6067 tpy 0.430335 tpy Benzene 459.9 lb/yr 22.995 lb/yr n-Hexane 1445.4 lb/yr 72.27 lb/yr 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. ' R 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. 003 Truck Condensate Loadout Calculations AP-42: Chapter 5.2 Equation 1 L= 12.46*S*P*M/T L= loading losses in lb per 1000 gallons loaded S=Saturation Factor P =true vapor pressure of liquid loaded [psia] M = molecular weight of vapors [lb/lb-mole] T=temperature of bulk liquid loaded [deg. R] 1 degree Fahrenheit =460.67 degree Rankine Source S 0.6 Submerged loading: ded AP-42 P 10.16 psia Sales Oil Analysis M 64 lb/lb-mole AP-42 T 524 deg. R Field Data L 9.28 lb/10^3 gal 3.90E-01 lb/bbl Annual requested Throughput 83220 BBL/yr 3495240 gal/yr Annual requested VOC emissions 32426 lb/yr 16.21 tpy Regulatory Considerations I his facility is not condisdered a terminal (in Reg. 7) because average daily throughput will be below 20,000 gallons at 3,956 gallons per day. This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. NCRPs Component Mass Frac. lb/yr Emission Factor Benzene 0.011 356.68 0.004286015 lb/bbl n-hexane 0.049 1588.86 0.019092248 lb/bbl Toluene 0.028 907.92 0.010909856 lb/bbl Ethylbenzene 0.009 291.83 0.003506739 lb/bbl Xylenes 0.028 907.92 0.010909856 lb/bbl oT ^ .° 6o '^ t° o, 00 o0oo0om .. 0o4. - mn -din ry cm d .v 0 „ a .. < o d d dd d o00000 ° m 0 o Z 0 II:S ry ry ^ b ry 0q000 O O O O o O m .. o o ! p' I - 3 3 `° o N ~m o « N o N ^ .+ e o d d 0 o o ti d d d 0 d „ •0 m • a S.. 0 .-0000 o m• °° t° 1.9 ° .: o 0000000. o `° o ' 3 .. o .Jo0oedmadrio '000odooco00 on ° 0c K $ 72 1r .. o ., ao 00 .. ^. 0 °9 °? .o m o 0 o o o o O m .. o o $ el $ m _ n $ i ... o .. o0 .. 'Y oea n ^ o. 000000m .vooem me 3 - .. o o r 0 2 1 0 0 d o o d o 0 0 d $ 0 • „ `o_ a 2 L_ O. O 'I O O .. O V. °. 0 0 0 0 0 0 0 i° N W u t� -i d 'i o O O N O 2 N 0 O 0 O d 0 0 0 0 O66666O2 OO y• Cj S Cb ` O O j. .. O V O .. 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I z 3 .w z° a z E z E 3 N E N r m cc • 005 Separator controlled by a VRU with a backup flare.Flare has a minimum combustion efficiency of 95%. Equipment Description This source vents natural gas from: a low pressure separator Emissions from this source are: routed to a flare Natural gas venting from a low pressure separator.Emissions from this source are routed to a flare. • 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(0) 8 MMscf/yr 913.2 scf/hr 0.68 MMscf/mo MW 33.900 lb/lb-mol 0.022 MMscf/d mole X MW Ibx/Ibmol mass fraction E Ibmr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.58 44.01 1.135 0.033 C02 2.7 23967 11.98 N2 0.14 28.013 0.039 0.001 N2 0.1 828 0.41 methane 36.2348 16.041 5.812 0.171 methane 14.0 122690 61.34 ethane 21.724 30.063 6.531 0.193 ethane 15.7 137855 68.93 propane 24.0702 44.092 10.6130 0.313 propane 25.6 224022 112.01 isobutane 2.5189 58.118 1.4639 0.043 iwvitane 3.5 30901 15.45 n-butane 8.0091 58.118 4.6547 0.137 n-butane 11.2 98253 49.13 isopentane 1.3574 72.114 0.9789 0.029 isopentane 2.4 20662 10.33 n-pentane 1.6714 72.114 1.2053 0.036 n-pentane 2.9 25442 12.72 cyclopentane 0.1315 70.13 0.0922 0.003 cyclopentane 0.2 1947 0.97 n-Hexane 0.3272 86.18 0.2820 0.008 n-Hexane 0.7 5952 2.98 cyclohexane 0.0815 84.16 0.0686 0.002 cyclohexane 0.2 1448 0.72 Other hexanes 0.5765 86.18 0.4968 0.015 Other hexanes 1.2 10487 5.24 heptanes 0.264 100.21 0.2646 0.008 heptanes 0.6 5584 2.79 methylcyclohexane 0.061 98.19 0.0599 0.002 methylcyclohexane 0.1 1264 0.63 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 2 0.00 1 Benzene 0.0588 78.12 0.0459 0.001 Benzene 0.1 970 0.48 ) Toluene 0.0316 92.15 0.0291 0.001 Toluene 0.1 615 0.31 Ethylbenzene . 0.0039 106.17 0.0041 0.000 Ethylbenzene 0.0 87 0.04 Xylenes 0.006 106.17 0.0064 0.000 Xylenes 0.0 134 0.07 C8+Heavies 0.1398 83.247 0.1164 0.003 C8+Heavies 0.3 2457 1.23 VOC mass fraction: 0.6012 Total VOC Emissions(Uncontrolled) 215.1 33.900 Notes Mole%,MW,and mass fractions from the Pronghom P,T-22HNB inlet to VRU gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average M1:k/of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0100 Serial Number 2,093,320,934 Gas Heating Value 1938 Btu/scf Throughput 15504 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make Model Requested Control Efficiency Annual Bypass Time Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42: Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 0.53 tpy NOX 2.87 tpy CO Emissions Summary • 0.5 tpy NOX Uncontrolled/PTE 2.9 tpy CO 215.1 tpy VOC Controlled 10.8 tpy VOC Uncontrolled Scenario A Controlled Total Total (Ib/yr) Bin Reportable? (lb/yr) Benzene 970 A , Yes 48 Toluene 615 C No 31 Ethylbenzene 87 C No 4 Xylenes 134 C No 7 n-hexane 5952 C Yes 298 224-TMP 2 C No 0 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 AQCC Regulation 2 Section I.A applies to all emission sources. "No person, wherever located, shall cause or allow the emission AQCC Regulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled INOX I 131.784 IIb/MMscf 006 - One (1) water transfer pump, rated at 600 scf/hr. Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2091613 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled Q Flare Section 05: Emission 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 Q sod scf/hr MW 24.5 Ib/I b-mol Hours of Op. 8760 hoursryr Requested Throughput 5.256 MMscf/yr • Component mole% MW mass fraction Component lb/hr lb/yr tpy nitrogen 0.64 28 0.0073 nitrogen 0.284 2485.159 1.243 C02 2.65 44 0.0476 C02 1.846 16170.174 8.085 methane 67.52994 16.04 0.4421 methane 17.148 150216.236 75.108 ethane 12.9918 30.07 0.1595 ethane 6.185 54177.493 27.089 propane 9.6357 44.09 0.1734 propane 6.726 58916.850 29.458 isobutane 1.0292 58.12 0.0244 isobutane 0.947 8295.480 4.148 n-butane 3.5372 58.12 0.0839 n-butane 3.255 28510.273 14.255 isopentane 0.7232 72.15 0.0213 isopentane 0.826 7236.206 3.618 n-pentane 0.8753 72.15 0.0258 n-pentane 1.000 8758.090 4.379 cyclopentane 0.0473 72.15 0.0014 cyclopentane 0.054 473.275 0.237 n-hexane 0.0646 86.18 0.0023 n-hexane 0.088 772.067 0.386 cyclohexane 0.0073 84.18 0.0003 cyclohexane 0.010 85.221 0.043 Other hexanes 0.1715 86.18 0.0060 Other hexane5 0.234 2049.683 1.025 heptanes 0.0226 100.21 0.0009 heptanes 0.036 314.077 0.157 methylcyclohexa 0.006 98.19 0.0002 methylcyclohe 0.009 81.702 0.041 224-TMP o 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 0.0051 78.11 0.0002 Benzene 0.006 55.245 0.028 Toluene 0.0036 92.14 0.0001 Toluene 0.005 46.001 0.023 Ethylbenzene 0.0008 106.17 0.0000 Ethylbenzene 0.001 11.779 0.006 Xylenes 0.0034 106.17 0.0001 Xylenes 0.006 50.061 0.025 C8+ Heavies 0.028 273.68601 0.0031 C8+Heavies 0.121 1062.739 0.531 Mass Fraction VOC: 0.3435 Total 58.359 Heating Value I 14oz BTU/scf—I Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMBtu 0.37 I lb CO/MMBtu Notes Mole%, MW.and mass fractions from extended gas analysis from Pronghorn 41-11-9HZ facility dated 6/18/2013 Emissions Summary Uncontrolle tpy NOX ncontrolle d/PTE 1.4 tpy CO 58.4 tpy VOC Controlled 2.9 tpy VOC Scenario A Controlled CAS# Total (Ib/yr) Bin Reportable Total n-hexane 110543 772.1 C No 39 224-TMP 540841 0.0 C No 0 Benzene 71432 55.2 I A Yes 3 Toluene 108883 46.0 C No 2 E-Benzene 100414 11.8 C No 1 Xylenes 1330207 50.1 C No 3 Resultant Emission Factors VOC 22206.763 lb/MMscf natural gas used Benzene 10.511 lb/MMscf natural gas used n-hexane 146.893 lb/MMscf natural gas used Toluene 8.752 lb/MMscf natural gas used E-Benzene 2.241 lb/MMscf natural gas used Xylenes 9.524 lb/MMscf natural gas used 224-TMP 0.000 lb/MMscf natural gas used Emergency gas emissions controlled by a candlestick flare.Flare has a minimum combustion efficiency of 95%. The flare is 007 not enclosed. 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. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(104-3) Ex=O'MW'Xx/C Ex=emissions of pollutant x C=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-mot)at 60F and 1 atm Throughput(0) 17 MMecf/yc 1917.8 scf/hr 1.43 MMsd/mo MW 24.500 Ibllb-mol 0.046 MMsd/d • mole% MW Ibxllbmol masa fraction E Iblhr Ibyr fey Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.65 44.01 1.166 0.048 CO2 5.9 51697 25.85 • • N2 0.64 28.013 0.179 0.007 N2 0.9 7947 3.97 methane 67.52994 16.041 10.832 0.442 methane 54.8 480173 240.09 ethane 12.9918 30.063 3.906 0.159 ethane 19.8 173130 86.56 propane 9.6357 44.092 4.2486 0.173 propane 21.5 188327 94.16 isobutane 1.0292 58.118 0.5982 0.024 isobutane 3.0 26514 13.26 n-butane 3.5372 58.118 2.0557 0.084 n-butane 10.4 91126 45.56 isopentane 0.7232 72.114 0.5215 0.021 isopentane 2.6 23118 11.56 n-pentane 0.8753 72.114 0.6312 0.026 n-pentane 3.2 27980 13.99 cyclopentane 0.0473 70.13 0.0332 0.001 cyclopentane 0.2 1470 0.74 n-Hexane 0.0646 86.18 0.0557 0.002 n-Hexane 0.3 2468 1.23 cyclohexane 0.0073 84.16 0.0061 0.000 cyclohexane 0.0 272 0.14 Otherhexanes 0.1715 86.18 0.1478 0.006 Otherhexanes 0.7 6551 3.28 heptanes 0.0226 100.21 0.0226 0.001 heptanes 0.1 1004 0.50 methylcyclohexane 0.006 98.19 0.0059 0.000 methylcycohexane 0.0 261 0.13 224-TMP 0 114.23 0.0000 0.000 224-TMP 0.0 0 0.00 Benzene 0.0051 78.12 0.0040 0.000 Benzene 0.0 1177 0.09 Toluene 0.0036 92.15 0.0033 0.000 Toluene 0.0 147 0.07 Ethylbenzene 0.0008 106.17 0.0008 0.000 Ethylbenzene 0.0 38 0.02 Xylenes 0.0034 106.17 0.0036 0.000 Xylenes 0.0 160 0.08 C8+Heavies 0.028 278.386 0.0779 0.003 C8+Heavies 0.4 3455 1.73 • VOC mass fraction: 0.3435 Total VOC Emissions(Uncontrolled) 186.5 24.500 Nat Mole%,MW,and mass fractions from extended gas analysis from Pronghorn 41-11-9HZ facility dated 6/18/2013 Emissions we 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. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer TBD , Model TBD Serial Number TBD Gas Heating Value 1402 Btu/scf Throughput 23553.6 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make Model Requested Control Efficiency Annual Bypass Time Backup Overall Control 95.00% Combustion emission factor source: AP-42: Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 0.80 tpy NOX 4.36 tpy CO Emissions Summary 0.8 tpy NOX Uncontrolled/PTE 4.4 tpy CO 186.5 tpy VOC Controlled 9.3 tpy VOC Uncontrolled Scenario A Controlled Total Total (lb/yr) Bin Reportable? (Ib/yr) Benzene 177 A Yes 9 Toluene 147 C No 7 Ethylbenzene 38 C No 2 Xylenes 160 C No 8 n-hexane 2468 C Yes 123 224-TMP 0 C No 0 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 AQCC Regulation 2 Section I.A applies to all emission sources. "No person, wherever located, shall cause or allow the emission AQCC Regulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled INOX I 95.336 IIb/MMscf Y. L 2 41 CC k,C tiO. a El E z .e. L on n or. �1 1 — C c u, z a' tv r�tv V r ,. < a a. 0' w y ^•O •Z -7 94 L t, u 5 > 'C Q N CL .. t t0 0 3 « n _ o eC �7 V . r E c `^ o = `iI .c O O C L tot ` e 40 V N V E G w aC, c r 0 S - co 41 a a on �. J. Mcc cb 4 e ., C ` C a V C w `. `� C O0. O y I C m w r c• c,, • c E I o c r o " a V r li .. Ld .. .., �; E 9 c:� E r " Lw a •° b e a N E.7 W u', t h Qa z 0. t.' Cr E.n N . v `v a rJw. 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