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Home My WebLink About20142202.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH 0c Coto Executive Director and Chief Medical Officer .40c, Dedicated to protecting and improving the health and environment of thepeople of Colorado \ P 9 4300 Cherry Creek Dr.S. Laboratory Services Division x�`ta -ss�i 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 10, 2014 Dear Sir or Madam: On July 16, 2014, the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—Pronghorn P-22,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 1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, f 7t 'w . . RECEIVED • Clara Gonzales JUL 1 8 2014 Public Notice Coordinator Stationary Sources Program WELD COUNTY Air Pollution Control Division COMMISSIONERS Enclosure P' Oe: pj('mMjr t (to) P1 -1' 23- J, � e � 3M) 2014-2202 7 STATE OF COLORADO John W.Hickenlooper,Governor pF Cor Larry Wolk,MD,MSPH �; o4 Executive Director and Chief Medical Officer Ne g J,*Dedicated to protecting and improving the health and environment of the people of Colorado * . { 4300 Cherry Creek Dr.S. Laboratory Services Division s I » 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 Website Title: Bonanza Creek Energy Operating Company LLC—Pronghorn P-22—Weld County Released To: The Greeley Tribune On: July 10, 2014 Published: July 16,2014 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-22 Wellpad NWNW Section 22 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 III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No.3,Part B, Section III.C.l.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 13WE2975 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 r Ill i STATE OF COLORADO op co, •LO- • •• D - • `T` •F P - C HEALTH AND ENVIRONMENT �Q AIR POLLUTION CONTROL DIVISION tom' 'i'6 TELEPHONE: (303)692-3150 ',l : *1876• CONSTRUCTION PERMIT PERMIT NO: 13WE2975 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-22 Production Facility, located in the NWNE Section 22 T5N R61 W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Truck 005 Truck Condensate Loadout Loadout FUG 006 Fugitive VOC leak emissions Separator controlled by a VRU with four backup flares. VRU has a HLP Sep-1 007 50% downtime. Flares have a minimum combustion efficiency of 95%. P-1 008 One (1) pneumatic water transfer pump, rated at 600 scf/hr. FL-1 009 Emergency flare for sales gas. Flare has a minimum combustion efficiency of 95%. The flare is not enclosed. Point 008: 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 II 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 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. AIRS ID: 123/9BC4 Page 1 of 14 olor Depa en li Health and Environment it Pollution Control Division 2. Within one hu d ' 80 ance is 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 007: 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 009: 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 Equipment ID Point NO VOC CO Emission Type Truck Loadout 005 --- 10.9 — Point FUG 006 --- 9.4 --- Fugitive AIRS ID: 123/9BC4 Page 2 of 14 olor- Depa en . • •li Health and Environment 'Jr Pollution Control Division HLP Sep-1 607 "'--- .4 Point P-1 008 --- 1.6 1.2 Point FL-1 009 --- 4.7 3.6 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 006: 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 Pollutants Equipment Control Device Point Controlled + ID o HLP Sep-1 007 Enclosed Flare VOC P-1 008 Enclosed Flare VOC FL-1 009 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 Facility AIRS Process Parameter Annual Limit Equipment Point AIRS ID: 12319BC4 Page 3 of 14 olor Depa en li Health and it Pollution ControlEnvironment Division ID Truck 005 Condensate Loaded 83,220 BBL Loadout HLP Sep-1 007 Gas Vented from Separator 18.9 MMSCF P-1 008 Natural Gas 5.3 MMSCF FL-1 009 Gas Vented from Separator 15.9 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. Points 005, 007, 008, 009: 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 XVII.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 005: This source is located in an ozone non-attainment or attainment-maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Pall B, III.E) 17. Point 005: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. AIRS ID: 123/9BC4 Page 4 of 14 olor. Depa en • di Health and Environment it Pollution Control Division c The o , •pe s per ' equi• ., 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 005: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 19. Point 006: 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 006: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by 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 semi-annual basis. The first AVO inspection shall 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: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. AIRS ID: 123/9BC4 Page 5 of 14 olor epa en li Health and Environment it Pollution Control Division • s • ctio as 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. Points 005, 007, 008, 009: 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 006: Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 23. Point 009: The owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.1 &4) Periodic Testing Requirements 24. Point 006: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 25. Point 008: 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. 26. Point 008: 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. AIRS ID: 123/9BC4 Page 6 of 14 olor- Depa . en . • .Ii ''Health and Environment it Pollution Control Division 27. Point 008: Al , ep .tal -perat- ,.--r the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 28. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30`" whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO,) in ozone nonattainment areas emitting less than 100 tons of VOC or NO„ per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. ' 29. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). 30. 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 AIRS ID: 123/9BC4 Page 7 of 14 epa en lit Health and EnvironmentDivisioni Pollution Control31. This permit aDolor t and e 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. 32. 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. 33. 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. 34. 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. 35. 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. 36. 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. 37. 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: AIRS ID: 123/9BC4 Page 8 of 14 olor Depa en P •li Health and Environment •it Pollution Control Division tWa: Peter s mow Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BC4 Page 9 of 14 olor Depa en linment it Pollutionealthand ControlEnviro Division Notes to Permit Holder me 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. I 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C°/02FCBONAddLinkView&cid=12515993896418Oagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? _ (lb/yr) Benzene 71432 406.1 Yes 406.1 n-Hexane 110543 2452 Yes 2452 005 Toluene 108883 1031.9 Yes 1031.9 Ethylbenzene 100414 131.5 No 131.5 Xylenes 1330207 660.4 Yes 660.4 Benzene 71432' 141 No 141 n-Hexane 110543 809.1 Yes 809.1 006 Toluene 108883 290.2 Yes 290.2 Ethylbenzene 100414 43 No 43 Xylenes 1330207 201 No 201 Benzene 71432 2290.7 Yes 57.3 007 n-Hexane 110543 14061.8 Yes 351.5 Benzene 71432 117 No 5.8 008 n-Hexane 110543 670.5 Yes 33.5 Benzene 71432 354 Yes 336.3 009 n-Hexane 110543 2028.3 Yes 101.4 AIRS ID: 123/9BC4 Page 10 of 14 Ill olor- Depa en . P •li Health and Environment it Pollution Control Division 5) The emission level .r d i •_ • ' - b- folio - ission factors: Point 005: Emission Factors - Uncontrolled Pollutant lb/BBL loaded Source VOC 0.262 AP-42 Benzene 0.0049 AP-42 n-hexane 0.029 AP-42 Toluene 0.012 AP-42 Ethylbenzene 0.0016 AP-42 Xylenes 0.0079 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) = 6.47 psia M (vapor molecular weight) =67.65 Ib/Ib-mol T(temperature of liquid loaded) = 524 °R Point 006: Component Gas Service Light Oil Water/Oil Service Connectors 1101 527 437 _ Flanges 53 14 16 Open-ended Lines 33 6 1 Pump Seals 4 0 1 Valves 148 66 44 Other* 81 7 16 VOC Content(wt. 0.2109 0.9963 1.0000 fraction) 0 Benzene Content(wt. 0.0004 0.019 0.0012 fraction) Toluene Content(wt. 0.0003 0.043 0.0003 fraction) Ethylbenzene (wt. 0.0001 0.006 0.0001 fraction) Xylenes Content(wt. 0.0001 0.030 0.0001 fraction) n-hexane Content(wt. 0.0023 0.112 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 AIRS ID: 123/9BC4 Page 11 of 14 I orDepHealth andControl EnvironmentDivision ConnectorsD2.R: 4Ff:0luti0h1 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 007: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled (lb/mmscf) (lb/mmscf) NOx 0.068 0.068 AP-42 Ib/MMBtu Ib/MMBtu CO 0.37 AP-42 0.37 lb/MMBtu lb/MMBtu VOC 60.04 53699.0776 1342.4769 Engineering Calculation Benzene 0.14 121.1994 3.0300 Engineering Calculation Toluene 0.09 76.8322 1.9208 Engineering Calculation Ethylbenzene 0.01 10.9251 0.2731 Engineering Calculation Xylenes 0.02 16.8079 0.4202 Engineering Calculation n-hexane 0.83 744.0131 18.6003 Engineering Calculation Note: The uncontrolled VOC and HAP emissions for this point were calculated using a Promax model to estimate the VOC and HAP content of the stream vented from the low-pressure separator. The controlled VOC and HAP emissions factors for point 007 are based on the flare control efficiency of 95%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,701 BTU/scf was used for calculations. Point 008: Emission Emission Factors Factors - -Controlled Uncontrolled lb/MMscf lb/MMscf vented Source • Pollutant vented VOC 11838.580 591.929012 All emission factors Benzene 22.258 1.11291293 are based on the n-hexane 127.565 6.37822955 displacement AIRS ID: 123/9BC4 Page 12 of 14 olor- Depa en ' •li Health and Environment •it Pollution Control Division Factors - Controlled Uncontrolled lb/MMscf lb/MMscf vented Source Pollutant vented _ equation and the Toluene 17.504 0.87520844 Pronghorn P T- 22HNB wet gas E-Benzene 3.081 0.15407256 analysis. Xylenes 5.323 0.26612533 Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas (°to) Uncontrolled Controlled (lb/mmscf) (Ib/mmscf) NOx 0.068 0.068 AP-42 lb/MMBtu lb/MMBtu CO 0.37 AP-42 0.37 lb/MMBtu lb/MMBtu VOC 20.96 11837.6090 591.8804 Engineering Calculation Benzene 0.04 22.2611 1.1131 Engineering Calculation Toluene 0.03 17.5061 0.8753 Engineering Calculation Ethylbenzene 0.01 3.0815 0.1541 Engineering Calculation Xylenes 0.01 5.3225 0.2661 Engineering Calculation n-hexane 0.23 127.5646 6.3782 Engineering Calculation 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 tolthe 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 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.dpoaccess.gov/ AIRS ID: 123/9BC4 Page 13 of 14 Depa en Ii Health and Environment it Pollution Control Division Part 60: StandarDolor e S ourc 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 7777-Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXX)O( 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.00v/cdphe/oilciaspermits t AIRS ID: 123/9BC4 Page 14 of 14 Division Information Engineer: Peter Armington Control Engineer: Stefanie Rucker Review Date: 03/10/2014 Application Date: 10/29/2013 Facility Identifiers Permit No. 13WE2975 AIRS County# 123 Weld Facility# 9BC4 Facility Type: exploration and production facility 2 Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: F V0C r N0x r CO • Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: Pronghorn P-22 Production Facility Source Location: NWNE Section 22 T5N R61W SIC: 1311 Mailing Address 1: Bonanza Creek Energy Operating Company LLC Address Address 2: 410 17th Street, Suite 1500 /,State Zip: Denver, CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pvoung@bonanzacrk.com ISection 02: Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Pronghorn P-22 Production Facility, located in the NWNE Section 22 T5N R61W, Weld County, Colorado. • Point Name Type Control 005 TL Loadout None 006 FUG Fugitives None 007 HLP Sep 1 Separator Venting Flare 008 P-1 Pump Flare 009 FL 1 Separator Venting Flare 005 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 6.47 psia Sales Oil Analysis M 67.65 lb/lb-mole AP-42 T 524 deg. R Field Data L 6.24 lb/10^3 gal 2.62E-01 lb/bbl Annual requested Throughput 83220 BBL/yr 3495240 gal/yr Annual requested VOC emissions 21827 lb/yr 10.91 tpy Regulatory Considerations This facility is not condisdered a terminal (in Seg. 7) because averrge 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 0.018606 406.11 0.004879917 lb/bbl n-hexane 0.11234 2452.01 0.029464142 lb/bbl Toluene 0.047276 1031.88 0.012399384 lb/bbl Ethylbenzene 0.006026 131.53 0.001580478 lb/bbl Xylenes 0.030256 660.39 0.007935438 lb/bbl a 52 b- o ^' o "`0000 0o eo moor. 5 ei • ▪a_ N m o m N m 21 6 -...d 6 d d 6 6 o d 55 m e m • U )1 255 I 0 p p C O` e N of T m O m O m 0 e - e m g ea n gee,-; • 0 0 0 0 0 d 6 m 0 Jlte en 555 O 2. m O O e O •. 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O O g" O O ti O O O ='O O O O O O n O O O > a 5 E, 0 0 0 O O = b m „ - o a o o o o 0 0 o 0 0 0 O ::o O O O O O O o - O b e m moon ,' 0 L e 0 0 0 0 0 0 0 0 0 O O „ 8 8 8 8 00 o- 0 [506066 0000000000000 ':d d d d o o d d 66 a U O tj 0 0 0 0 0 o b CD O.u et Li. a o a 00000000 Z oh m CO 0 r 0 e g o • • E 5 `m te 0 ale � w rvm rv .. i. N .. "• " mN• .. -.• rvN ry . < v _ Tc w ._ n w = e 1- w x > 40 w 000800000 88 oo : 0 0 T2 L p w w w ()zoo, a n $ v q' m .4 .. em P (nN N onm -. mmNin rvw ui 0 tl — ¢ . C - M • m o g e e 'm n e o n N = o o= - o 0 0 o a .- 0 o m .- q 5,2 S 8 8 a o o c. C00 -- • w c0i > _ _ = &a ° &a O t Q C c - „ - „ O _ - „ v I y -, w e O _ p a a > N £ O vdi „ v a vdi „ b in w vdi „ v a 0 „ b „ ° I- F 0 I- N >E p O `a 0 U I E c o q Lc ≥ E c o c `a 2 E r a `a ? E c `co c `a OF ° OF Q m p a w• o y o > a o u u o >> a o o m o> a o u o 0> a 0 u s 0 m 0 o i 3 — 0 0 U▪ 4. u .. 0 28 fti ° b co 0 at 7 o VUi LL C0U = 3 1 2 i Z ' m 8 N ym 4 `o m 3 E m m CC Separator controlled by a VRU with four backup flares.VRU has a 50%downtime. Flares have a minimum combustion 007 efficiency of 95%. Equipment Description This source vents natural gas from. a low-pressure separator Emissions from this source are: recompressed Natural gas venting from a low-pressure separator.Emissions from this source are recompressed. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q'MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(O) 19 MMscf/yr 2157.5 scf/hr 1.61 MMscf/mo MW 33.900 Ibllb-mol 0.052 MMscf/d mole% MW Ibx/Ibmol mass fraction E lb/hr 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 CO2 6.5 56623 28.31 N2 0.14 28.013 0.039 0.001 N2 0.2 1956 0.98 methane 36.2348 16.041 5.812 0.171 methane 33.1 289854 144.93 ethane 21.824 30.063 6.561 0.194 ethane 37.3 327182 163.59 propane 24.0702 44.092 10.6130 0.313 propane 60.4 529251 264.63 isobutane 2.5189 58.118 1.4639 0.043 isobutane 8.3 73004 36.50 n-butane 8.0091 58.118 4.6547 0.1373 n-butane 26.5 232122 116.06 isopentane 1.3574 72.114 0.9789 0.0289 isopentane 5.6 48815 24.41 n-pentane 1.6714 72.114 1.2053 0.0356 n-pentane 6.9 60107 30.05 cyclopentane 0.1315 70.13 0.0922 0.0027 cyclopentane 0.5 4599 2.30 n-Hexane 0.3272 86.18 0.2820 0.0083 n-Hexane 1.6 14062 7.03 cyclohexane 0.0815 84.16 0.0686 0.0020 cyclohexane 0.4 3420 1.71 Other hexanes 0.5765 86.18 0.4968 0.0147 Other hexanes 2.8 24776 12.39 heptanes 0.264 100.21 0.2646 0.0078 heptanes 1.5 13193 6.60 methylcyclohexane 0.061 98.19 0.0599 0.0018 methylcyclohexane 0.3 2987 1.49 224TMP 0.0001 114.23 0.0001 0.0000 224TMP 0.0 6 0.00 Benzene 1 0.0588 78.12 0.0459 0.0014 Benzene 0.3 2291 1.15, Toluene 0.0316 92.15 0.0291 0.0009 Toluene 0.2 1452 0.73 Ethylbenzene 0.0039 106.17 0.0041 0.0001 Ethylbenzene 0.0 206 0.10 Xylenes 0.006 106.17 0.0064 0.0002 Xylenes 0.0 318 0.16 C8+Heavies 0.1398 61.743 0.0863 0.0025 C8+Heavies 0.5 4304 2.15 VOC mass fraction: 0.6004 Total VOC Emissions(Uncontrolled) 507.5 33.900 Notes Mole 46,MW,and mass fractions from Pronghorn P T-22HNB gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas while VRU system is down. Manufacturer Leed Model L30-0010-000 Serial Number 21278,21275,21274,21279 Gas Heating Value 1938 Btu/scf Throughput 18314.1 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare - Overall Control 97.50% Combustion emission factor source: AP-42: Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 0.62 tpy NOX 3.39 tpy CO Emissions Summary 0.6 tpy NOX Uncontrolled/PTE 3.4 tpy CO 507.5 tpy VOC Controlled 12.7 tpy VOC Uncontrolled Scenario A Controlled Total Total (Ib/yr) Bin Reportable? (Ib/yr) Benzene 2291 A Yes 57 Toluene 1452 C Yes 36 Ethylbenzene 206 C No 5 Xylenes 318 C No 8 n-hexane 14062 C Yes 352 224-TMP 6 C No 0 Regulatory Applicability A CC Re ulation 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 _ NOX 65.892 lb/MMscf CO 358.53 lb/MMscf VOC 53699.0776 lb/MMscf Benzene 121.1994 lb/MMscf Toluene 76.8322 lb/MMscf Ethylbenzene 10.9251 lb/MMscf 008 One (1) water transfer pump, rated at 600 scf/hr. Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2091584 Information Pump capacity 9.1 gallons per minute pumped _ natural gas 600 scf/hour used consumptio Control O Uncontrolled ®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 600 scf/hr MW 214 lb/lb-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole% MW mass fraction Component lb/hr lb/yr tpy nitrogen 0.95 28 0.0124 nitrogen 0.421 3688.908 1.844 CO2 2.41 44 0.0496 nitrogen 1.679 14705.706 7.353 methane 76.72364 16.04 0.5751 methane 19.483 170667.061 85.334 ethane 10.9089 30.07 0.1533 ethane 5.193 45491.529 22.746 propane 6.1942 44.09 0.1276 propane 4.324 37874.026 18.937 isobutane 0.5019 58.12 0.0136 isobutane 0.462 4045.377 2.023 n-butane 1.4696 58.12 0.0399 n-butane 1.352 11845.159 5.923 isopentane 0.2279 72.15 0.0077 isopentane 0.260 2280.325 1.140 n-pentane 0.2769 72.15 0.0093 n-pentane 0.316 2770.610 1.385 cyclopentane 0.0217 72.15 0.0007 n-pentane 0.025 217.126 0.109 n-hexane 0.0561 86.18 0.0023 n-hexane 0.077 670.479 0.335 cyclohexane 0.0144 84.18 0.0006 cyclohexane 0.019 168.108 0.084 Other hexanes 0.0979 86.18 0.0039 Other hexane! 0.134 1170.052 0.585 heptanes 0.0495 100.21 0.0023 heptanes 0.079 687.911 0.344 methylcyclohexa 0.012 98.19 0.0006 methylcyclohe 0.019 163.405 0.082 224-TMP 0.0001 114.22 0.0000 224-IMP 0.000 1.584 0.001 Benzene 0.0108 78.11 0.0004 Benzene 0.013 116.989 0.058 Toluene 0.0072 92.14 0.0003 Toluene 0.011 92.002 0.046 Ethylbenzene 0.0011 106.17 0.0001 Ethylbenzene 0.002 16.196 0.008 Xylenes 0.0019 106.17 0.0001 Xylenes 0.003 27.975 0.014 C8+Heavies 0.034 16.171865 0.0003 C8+Heavies 0.009 76.253 0.038 Mass Fraction VOC: 0.2097 Total 31.112 Heating Value I 1235 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 Pronghorn P T-22HNB gas analysis. Emissions Summary Uncontrolle tpy NOX ncontrolle d/PTE 1.2 tpy CO 31.1 tpy VOC Controlled 1.6 tpy VOC Scenario A Controlled CAs# Total (Ib/yr) Bin Reportable Total n-hexane 110543 670.5 C No 34 224-TMP 540841 1.6 C No 0 Benzene 71432 117.0 A Yes 6 Toluene 108883 92.0 C No 5 E-Benzene 100414 16.2 C No 1 Xylenes 1330207 28.0 C No 1 Resultant Emission Factors VOC 11838.580 lb/MMscf natural gas used 591.929012 Benzene 22.258 lb/MMscf natural gas used 1.11291293 n-hexane 127.565 lb/MMscf natural gas used 6.37822955 Toluene 17.504 lb/MMscf natural gas used 0.87520844 E-Benzene 3.081 lb/MMscf natural gas used 0.15407256 Xylenes 5.323 lb/MMscf natural gas used 0.26612533 224-TMP 0.301 lb/MMscf natural gas used 009 Emergency flare for sales gas.Flare has a minimum combustion efficiency of 95%. The flare is 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(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(O) 16 MMscf/yr 1815.1 scf/hr 1.35 MMscf/mo MW 21.400 Ib/Ib-mol 0.044 MMscf/d mole% MW Ibxllbmol mass fraction E Ib/hr Ib/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.41 44.01 1.061 0050 CO2 5.1 44497 22.25 N2 0.95 28.013 0.266 0 012 N2 1.3 11165 5.58 methane 76.72364 16.041 12.307 0.575 methane 58.9 516320 258.16 ethane 10.9089 30.063 3.280 0.153 ethane 15.7 137585 68.79 propane 6.1942 44.092 2.7311 0.1276 propane 13.1 114578 57.29 isabutane 0.5019 58.118 0.2917 0.0136 isobutane 1.4 12237 6.12 n-butane 1.4696 58.118 0.8541 0.0399 n-butane 4.1 35832 17.92 isopentane 0.2279 72.114 0.1643 0.0077 isopentane 0.8 6895 3.45 n-pentane 0.2769 72.114 0.1997 0.0093 n-pentane 1.0 8377 4.19 cyclopentane 0.0217 70.13 0.0152 0.0007 cyclopentane 0.1 638 0.32 n-Hexane 0.0561 86.18 0.0483 0.0023 n-Hexane 0.2 2028 1.01 cyclohexane 0.0144 84.16 0.0121 0.0006 cyclohexane 0.1 508 0.25 Other hexanes 0.0979 86.18 0.0844 0.0039 Other hexanes 0.4 3540 1.77 heptanes 0.0495 100.21 0.0496 0.0023 heptanes 0.2 2081 1.04 methylcyclohexane 0.012 98.19 0.0118 0.0006 methylcyclohexane 0.1 494 0.25 224-TMP 0.0001 114.23 0.0001 0.0000 224-TMP 0.0 5 0.00 / Benzene 0.0108 78.12 0.0084 0.0004 Benzene 0.0 354 0.18 l Toluene 0.0072 92.15 0.0066 00003 Toluene 00 278 0.14 Ethylbenzene 0.0011 106.17 0.0012 0.0001 Ethylbenzene 0.0 49 0.02 Xylenes 0.0019 106.17 0.0020 0.0001 Xylenes 0.0 85 0.04 08+Heavies 0.034 16.668 0.0057 0.0003 C8+Heavies 0.0 238 0.12 VOC mass fraction: 0.2096 Total VOC Emissions(Uncontrolled) 94.1 Notes Mole%,MW.and mass fractions from Pronghom P T-22HNB gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. 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 1235 Btu/scf Throughput 19636.5 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 0.67 tpy NOX 3.63 tpy CO Emissions Summary 0.7 tpy NOX Uncontrolled/PTE 3.6 tpy CO 94.1 tpy VOC Controlled 4.7 tpy VOC Uncontrolled Scenario A Controlled Total Total(lb/yr) Bin Reportable? (Ib/yr) Benzene 354 A Yes 336 Toluene 278 C No 14 Ethylbenzene 49 C No 2 Xylenes 85 C No 4 n-hexane 2028 C Yes 101 224-TMP 5 C No 0 Regulatory Applicability A CC R ulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a AQCC Re ulation 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 NOX 83.98 Ib/MMscf CO 456.95 lb/MMscf VOC 11837.6090 lb/MMscf Benzene 22.2611 lb/MMscf Toluene 17.5061 lb/MMscf Ethylbenzene 3.0815 lb/MMscf ^ v .. 3 'p 3 3 : ` m .-1 54 r z $ G $ C C -C E O*0 �I �I 8 c C y a , _ ar- -1 tI a v a p gQ E Z v _� .:3" 771 7 aou L. " CI 9S arc 4s�'j `co = .`� o e • a ❑ ❑ ❑❑❑ p. > U o L ��' -, 9 s N C V h ._• "' O O O O O .. 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