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Home My WebLink About20141679.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD,MSPH !oF i, Executive Director and Chat Medical Officer ;e/ a14: 1V X1 Dedicated to protecting and improving the health and environment of the people of Colorado , '1/ 4300 Cherry Creek Dr.S. Laboratory Services Division 1gj6 r 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.govtcdphe and Environment Weld County- Clerk to the Board 1150 O St PO Box 758 Greeley, CO 80632 May 29,2014 Dear Sir or Madam: On June 2,2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—State Antelope J-12, 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 ♦''1 Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure qu- 6f-i e1A9-L° ce p i Lru.rv `?(A.C --42 ,cH-I gym) t(p6) 2014-1679 �- t-ao��l li -y- �`� STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD.MSPH oe cotS Executive Director and Chief Medical Officer /A.C7:74;17 Dedicated to protecting and improving the health and environment of the people of Colorado ii ' I,; 4300 Cherry Creek Dr.S. Laboratory Services Division 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 I lealth www.colorado.gov/cdphe and Environment • Website Title: Bonanza Creek Energy Operating Company LLC—State Antelope J-12 — Weld County Released To: The Greeley Tribune On: May 29, 2014 Published: June 2,2014 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 I LC Facility: State Antelope J-12 oil and gas production facility SFSW Sec 12 T SN R62W Weld County The proposed project or activity is as follows: The source proposes to operate a new oil and gas exploration and production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B. Section I II.C 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 13 WE-2849 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 applicahle 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: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-Bl Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us STATE OF COLORADO an jam c0Teci. COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692-3150 18]8/ CONSTRUCTION PERMIT PERMIT NO: 1 3WE2849 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State Antelope J-12 Production Facility, located in the SESW Section 12, Township 5N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID One (1) 400 bbl and one (1) 60 bbl fixed roof atmospheric PW Tanks 004 produced water storage tanks. The tanks are controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. Truck 005 Truck Condensate Loadout Loadout FUG 006 Fugitive VOC equipment leak emissions HLP Sep-1 007 One low pressure separator controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One (1) pneumatic water transfer pump, rated at 600 scf/hr P-1 008 (Sandpiper, Model G1 F, Serial number 2091610)controlled by two enclosed flares. Each flare has a minimum combustion efficiency of 95%. One emergency flare with a minimum combustion efficiency of FL-1 009 95%. The flare is not enclosed. The emergency flare is used during periods when the sales gas cannot be routed to the pipeline. 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 AIRS ID: 123/9BB2 Page 1 of 15 olor Depa en P li ealth and Environment it Pollution Control Division CONTROL ACT C.R. 10 s T NE ERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. AIRS Point 009: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. AIRS Point 009: The following information shall be provided to the Division within fifteen (15) days after commencement of operation. • 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.) 3. AIRS Point 009: Within one hundred and eighty days (180) after commencement of operation, 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). 4. AIRS Points 004 — 008: 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. 5. AIRS Points 004 — 008: 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). 6. 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, I I I.F.4.) AIRS ID: 123/9BB2 Page 2 of 15 olors Depa en P li ealth and Environment it Pollution Control Division 7. AIRS Point 00 inn y nce o 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 ninety (90) days after issuance of this permit. 8. 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.) 9. 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 10. 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 PW Tanks 004 0.3 Point Truck Loadout 005 7.0 Point FUG 006 7.3 Fugitive HLP Sep-1 007 1.1 23.5 5.8 Point P-1 008 --- 1.9 1.2 Point FL-1 009 --- 4.1 2.6 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. 11. AIRS Point 006: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent extended 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 AIRS ID: 123/9BB2 Page 3 of 15 olor Depa en `. P`y.li " ealth and Environment A it Pollution Control Division sampling eve . .._, o -' la''� al „1' n,- and ta- a:-tes that these counts and events were completed. These records shall be provided to the Division upon request. 12. 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 pen-nit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID PW Tanks 004 Enclosed Flare VOC HLP Sep-1 007 Enclosed Flare VOC P-1 008 Enclosed Flare VOC FL-1 009 Open Flare VOC PROCESS LIMITATIONS AND RECORDS 13. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Equipment Point Process Parameter Annual Limit ID PW Tanks 004 Produced water throughput 43,800 BBL Truck 005 Condensate Loaded 70,080 BBL Loadout HLP Sep-1 007 Gas Vented from Low Pressure Separator 15.3 MMSCF P-1 008 Natural Gas Consumed 5.3 MMSCF FL-1 009 Gas Vented from Separator 11.1 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. 14. AIRS Point 007: Upon installation of the flow meter required under Condition 7, 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 13 and to calculate emissions as described in this permit. AIRS ID: 123/9882 Page 4 of 15 A olora .Depa , en P li ealth and Environment it Pollution Control Division STATE AND FEDERAL REGULATORY REQUIREMENTS 15. AIRS Points 004, 005, 007, 008, and 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) 16. 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.) 17. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 18. 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. 19. AIRS 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, Part B, III.E) 20. AIRS 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. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 20 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. AIRS 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. 22. AIRS 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: AIRS ID: 123/9BB2 Page 5 of 15 olor Depa en . P .11 " ealth and Environment •it Pollution Control Division a. Direct --cti- : '-. .-na-. = descr 4="- 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 must be completed 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. • 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 23. AIRS Points 004, 006, 007, 008, and 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 24. AIRS 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 AIRS ID: 123/9882 Page 6 of 15 A olor s DeparAnenL P li ealth and Environment tPolluton Control Divison number of co s t e »_ . eddt ea' y liquidice", "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. 25. AIRS 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 26. AIRS 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 27. AIRS 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. 28. AIRS 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. 29. AIRS Point 008: 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 (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. AIRS ID: 123/9662 Page 7 of 15 olor Depa en - P •li ealth and Environment •it Pollution Control Division b When e i ,.<- -`. ,.- th-. - mar ope =K 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. 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). I GENERAL TERMS AND CONDITIONS 32. 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. 33. 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. 34. 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. 35. 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. 36. 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: 123/9BB2 Page 8 of 15 41, olor pea en" P ili Ar Pollutionealth Controland DivisionEnvironment permit, conditicstj in s ® mit fasted by,, 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. 37. 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. 38. 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: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BB2 Page 9 of 15 D. olor Depa en P 'Ii " ealth and Environment n it Pollution Control Division '" Notes to Permit Holder ' `='` me o ` '.e '` a - 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) Benzene 71432 307 Yes 15 004 n-Hexane 110543 964 Yes 48 Benzene 71432 255 Yes 255 Toluene 108883 616 Yes 616 005 Ethylbenzene 100414 168 No 168 Xylenes 1330207 635 Yes 635 n-Hexane 110543 1320 Yes 1320 Benzene 71432 105 No 105 n-Hexane 110543 535 Yes 535 006 Toluene 108883 219 No 219 Ethylbenzene 100414 58 No 58 Xylenes 1330207 217 No 217 Benzene 71432 2474 Yes 124 Toluene 108883 1450 Yes 72 007 Ethylbenzene 100414 133 No 7 Xylenes 1330207 240 No 12 AIRS ID: 123/9862 Page 10 of 15 olor • _ Depa en bf P lic'Health and Environment it Pollution Control Division n-H- . 4:.--' art'-105Sza$1 i44976`64444 I -;Y4S 749 Benzene 71432 189 No I 9 n-Hexane 110543 1119 Yes 56 008 Toluene 108883 152 No 8 Ethylbenzene 100414 21 No 1 Xylenes 1330207 62 No 3 Benzene 71432 397 Yes 20 Toluene 108883 321 Yes 16 009 Ethylbenzene I 100414 43 No 2 Xylenes Ir 1330207 130 No 7 n-Hexane 110543 2358 Yes 118 5) The emission levels contained in this permit are based on the following emission factors. Point 004: Emission Emission Factors - Factors - Uncontrolled Uncontrolled Pollutant Ib/BBL loaded lb/BBL loaded Source VOC 0.262 0.0131 CDPHE PS Memo 09-02 Benzene 0.007 0.0004 CDPHE PS Memo 09-02 n-Hexane 0.022 0.0011 i CDPHE PS Memo 09-02 Point 005: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.199 AP-42 Benzene 0.0036 AP-42 Toluene 0.0088 AP-42 Ethylbenzene 0.0024 I AP-42 Xylenes 0.0091 1 AP-42 I n-Hexane 0.0188 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)=4.89 psia M (vapor molecular weight) = 68 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 stable condensate by the VOC emission factor. AIRS ID: 123/9BB2 Page 11 of 15 olor-. Depa en P li ealth and Environment it Pollution Control Division Point 006: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 881 0 338 267 Flanges 49 0 8 10 Open-ended Lines 27 0 3 1 Pump Seals 4 0 0 1 Valves 123 0 45 29 Other* 62 0 7 10 VOC Content(wt. 0.2507 1.0 0.9965 1.0 fraction) Benzene Content(wt. 0.0006 0 0.0183 0 fraction) Toluene Content(wt. 0.0005 0 0.044 0 fraction) Ethylbenzene (wt. 0.00007 0 0.012 0 fraction) Xylenes Content(wt. 0.0002 0 0.0454 0 fraction) n-hexane Content(wt. 0.0036 0 0.0945 0 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 I 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 I 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 extended gas analysis. Point 007: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled NOx 0.068 0.068 AP-42 lb/MMBtu lb/MMBtu CO 0.37 AP-42 ___ 0.37 lb/MMBtu lb/MMBtu AIRS ID: 123/9662 Page 12 of 15 olor. : Depa . en P li ealth and Environment 'hig :• it Pollution Control Division t m, ., rill rrS ' on 2, Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled VOC 64.8 61,350 3067.5 Engineering lb/mmscf lb/mmscf Calculation Benzene 0.17 161.39 8.0697 Engineering lb/mmscf lb/mmscf Calculation Toluene 0.10 94.581 4.7291 Engineering lb/mmscf lb/mmscf Calculation Ethylbenzene 0.01 8.6841 0.4342 Engineering lb/mmscf lb/mmscf Calculation Xylenes 0.02 15.687 0.7844 Engineering lb/mmscf lb/mmscf Calculation n-hexane 1.03 977.09 48.854 Engineering lb/mmscf lb/mmscf Calculation Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 9/11/2013 of the gas vented from the low pressure separator at State Antelope J-F-12HNB to estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow. 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 2,053 BTU/scf was used for calculations. Point 008: Emission Factors- Emission Factors- Uncontrolled Controlled Pollutant Ib/MMscf vented Ib/MMscf vented Source NO„ 0.068 Ib/MMBTU AP-42 Table 13.5-1 CO 0.37 Ib/MMBTU AP-42 Table 13.5-1 VOC 14,735 736.76 All emission factors Toluene 28.934 1.4467 are based on the Xylenes 11.766 0.5883 stated consumption n-Hexane 212.84 10.642 and the average of sales gas analysis from State Antelope Benzene 35.865 1.7933 J-F-12HNB dated 8/26/2013 The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4-3)." Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,285 BTU/scf was used for calculations. Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas (%) Uncontrolled Controlled NOx 0.068 0.068 AP-42 lb/MMBtu lb/MMBtu AIRS ID: 123/9BB2 Page 13 of 15 , '; olor. Depa r, en •a P •+li ealth and Environment t it Pollution Control Division Pollutant Fraction of Factors Factors Source Gas (TO) Uncontrolled Controlled CO 0.37 AP-42 ___ 0.37 lb/MMBtu lb/MMBtu VOC 2a 07 14,735 736.76 Engineering lb/mmscf lb/mmscf Calculation Benzene 0.06 35.865 1.7933 Engineering lb/mmscf lb/mmscf Calculation Toluene 0.05 28.934 1.4467 Engineering lb/mmscf lb/mmscf Calculation Ethylbenzene 0.01 3.9218 0.1961 Engineering lb/mmscf lb/mmscf Calculation Xylenes 0.02 11.766 0.5883 Engineering lb/mmscf lb/mmscf Calculation n-hexane 0.36 212.84 10.642 Engineering lb/mmscf lb/mmscf Calculation Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,285 BTU/scf was used for calculations. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division. A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC and n-hexane NANSR Synthetic Minor Source of: VOC MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.2poaccess.eov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD AIRS ID: 123/9BB2 Page 14 of 15 a � 472-11 color •:° Depa tnentelf P' licHealth and Environment Es ' it Pollution Control Division Li MACT 63.120O44419 *S EEE tt PPP '-z MACT 63.1440-63.6175 Subpart OOO-Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ- 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.gov/cdphe/oilgaspermits AIRS ID: 123/9BB2 Page 15 of 15 Division Information Engineer: Carissa Money Control Engineer: Chris Laplante Review Date: 04/10/2014 Application Date: 10/18/2013 Facility Identifiers Permit No. 13W E2849 AIRS County# 123 Weld Facility# 9882 Facility Type: exploration and production facility E Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: 1 VOC F NOx J CO Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Antelope J-12 Production Facility Source Location: SESW Section 12, Township 5N, Range 62W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address Address 2: 410 17th Street Suite 1500 r, 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 State Antelope J-12 Production Facility, located in the SESW Section 12, Township 5N, Range 62W,Weld County, Colorado. Point Name Type Control • 005 Truck Loadout None Loadout 006 FUG Fugitives None 007 HLP Sep 1 Separator Venting Flare 008 P1 Pump Flare 009 FL1 Separator Venting Flare This is an emergency flare I I 004 Two produced water tanks Throughput 43800 bbl/yr 1839600 gal/yr Control Efficiency 95% Uncontrolled Emissions Pollutant EF-lb/bbl lb/yr tpy Source EF-lb/1000 gal VOC 0.262 11475.6 5.74 6.2381 Division, PS Memo Benzene 0.007 306.6 0.15 0.1667 09-02 n-hexane 0.022 963.6 0.48 0.5238 Controlled Emissions Pollutant EF-lb/bbl lb/yr tpy Source -EF-lb/1000 gal VOC 0.0131 573.78 0.29 0.3119 Division, PS Memo Benzene 0.00035 15.33 0.01 09-02 0.0083 n-hexane 0.0011 48.18 0.02 0.0262 • • 123/9882 13WE2849.CP1 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: dedIAP-42 P 4.89 psia Sales Oil Analysis documenting RVP 7 and AP-42 Fi M 68 lb/lb-mole AP-42,Table 7.1-2 for gasoline RVP 7 T 523.67 deg. R Field Data L 4.75 lb/10^3 gal 1.99E-01 lb/bbl Annual requested Throughput 70080 BBL/yr 2943360 gal/yr Annual requested VOC emissions 13972 lb/yr 6.99 tpy Regulatory Considerations I his facility is not condisdered a terminal On keg. 7) because average daily throughput will be below 20,000 gallons at 8064 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 tpy Emission Factor lb/1000 gal Benzene 0.018259 255.12 0.13 0.0036 lb/bbl 0.086677496 n-hexane 0.094481 1320.13 0.66 0.0188 lb/bbl 0.448511777 Toluene 0.044055 615.56 0.31 0.0088 0.209133967 Ethylbenzene 0.012047 168.33 0.08 0.0024 0.057188444 Xylene 0.045413 634.53 0.32 0.0091 0.215580543 123/9882 13WE2649.CP1 1 I r_— I 3 2 oa l0a r I — i o 0 03 oii ,� m o a,o =I0 „ 38 'loi� o e � m ao a a Ea l I mf`, .I. 015 0 010 0 . 5 i o oio O 4 o elm m all m EE85;oom o , m ol0 € aaCIO C. C a F _ , Flo' fo a a �L�� a ml8o 00000 00 re al,n to EIS,o r a ,, a o 0 0 0 o m a a 3 coo . . 23 . 03, a c a o o a o alo 0 0 s a s U 0 m�4 _ an P N oa on .. o _ oac... o oolco oa -rr ' ° oioaoi a a al oc 8 o a o o o o o o al o o a o a� ';' .. .14.q (22037820 N l > a7 mo .. o m o ,o n — 000 mm o o o goo = E m u m `� a N f a 3I U � w;� w mEl c S '.C d I— `i Ea- a < of to al E E �� E _ aIAa l° ° LL AL of 3'5 ,E �hlmo3� >I 0 6 0 a h �I m L J z 3 w 2 ,4 3 E sc z z op E Ec ci E a.0 mE r ? 2 3v Ec 6 O rn > One low pressure separator controlled by two enclosed flares.Each flare,as a min-mum combustion efficiency 0`95%. 007 The`lore is 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 the source are routed to a flare. I Emission Calculation Method EPA Emission Inventory Imorovement Program Puolicetiors Volume II,C.napter'0-Displacement Equation(10.4-3) Ex=O'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 sof/lb-mcl)at 60E and 1 atm Throughout(O) 15 MMscf/yr 17497 scf/hr 1 30 MMscf/mo I MW 35.900 lb/lb-moil 0.042 MMscf/d mole% IMW Ibx/Ibmol mass fraction E ,lb/hr Ib/yr tpy Helium 0.01! 4.0026 0.000 a 0.000 Helium 0.0 16 0.01 OO2 2.25 44.01 D.990 0.028 CO2 4.6 40046 20.02 N2 0.2 28.013 0.056 0.002 N2 0.3 2266 1.13 methane 32.158 16041 5.158 0.144 methane 23.8 208617 104.31 ethane 21.4003 30.063 6434 0.179 ethane 29.7 260185 130.09 propane 24.9]95 44092 11O140 0.307 propane 50.8 445423 222.71 isobutane 2.9815 58.118 1.7330 0.048 IsobLaane 8.0 70004 35.04 n-butane 9.837 58.118 5.71]1 0.159 n-butane 26.4 231208 115.60 isopentane 1.7925 72.114 1.2926 0.036 isopentane 6.0 52277 26.14 n-pentane 2.3049 72.114 1.6622 0.046 a-pentane 7.7 67220 33.61 cyciopentane 0.1774 70.13 0.1244 0.003 nyclopentane 0.6 5031 2.52 n-Hexane 0.4297 86.18 0.3703 0.010 n-Hexane 1.7 14976 7.49 cyclohexane 0.1022 84.16 0.0060 0.002 oyclohexane 0.4 3478 1.74 Other hexanes 07455 86.18 0.6425 0.018 Other hexanes 3.0 25983 12.99 heptanes 0.2894 100.21 0.2900 0.008 heptanes 1.3 11728 5.86 met8yicyclohexane 0.0653 98.19 0.0641 0.002 methylcyciohexane 0.3 2593 1.30 224-TMP 0.0002 114.23 0.0002 0.000 224-TMP 0.0 9 0O0 Benzene 0.0783 78.12 0.0612 0.0017 Benzene 0.3 2474 1.24 Toluene 40389 92.15 0.0358 0.0010 Toluene 0.2 1450 0.72 Ethylbenzene 0.0031 106.17 0.0033 0O001 Ethylbenzene 0.0 133 0.07 Xylenes 0.0056 105.17 0.0059 0.0002 Xylenes 0.0 240 0.12 OB+Heavies 0.1285 116.000 0.1491 0.0042 CST Heavies 0.7 6028 3.01 VOC mass fraction: 0.6477 Total VOC Emissions(Uncontrolled) 470.2 35.890 Notes Mole 15 and MW are based on ges sample of inlet to VRU at State Antelope J-P-O2HNB,dated 9/11/2013 Emissions are based on 8760 hours of operation per year. Mates the average MW of EST based on the average MW on the analyes for the gas 8 emissions are 0.2 tpy higher.Source used MW of 116. Since minims..difference,I used the source's calculations I Flaring Information Equipment Description Manufacturer ILeed Model L30-0100 Serial Number 21125&21124 Gas Heating Value 2053 Btu/scf Throughout 31467.1522 MMBtu/yr 523/9882 '3W62849 Col VRU Information-Not applicable Equipment Description 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 1.07 tpy NOX 5.82 tpy CO _ Emissions Summary • 1.1 tpy NOX • Uncontroiled/PTE 5.8 tpy CO 470.2 tpy VOC Controlled 23.5 tpy VOC Uncontrolled Controlled Total Total(lb/yr) tpy Reportable? (Iblyr) Benzene 2474 1.237 Yes 124 Toluene 1450 0.725 Yes 72 Ethylbenzene 133 0.067 No 7 Xylenes 240 0.120 No 12 n-hexane 14976 7.488 Yes 749 224-TMP 9 0.005 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 1.A apolies to all emission sources.''No person,wherever located,shall cause or allow the emission AQCC Regulation 3 s public comment Public Comment Required required", • Emission Factors For Permit NOX 139.604 lb/MMscf CO 759.61 IbIMMscf VOC 61350.0402 lb/MMscf Benzene 161.3930 lb/MMscf Toluene 94.5814 lb/k4Mscf Ethylbenzene 8.6841 lb/MMscf Xylenes 15.6874 lb/MMscf n-Hexane 977.0856 lb/MMscf 224-TMP 0.6028 lb/MMscf Controlled NOX 139.604 lb/MMscf CO 759.61 Ib/MMscf VOC 3067.5020 lb/MMscf Benzene 8.0697 lb/MMscf Toluene 4.7291 lb/MMscf Ethylbenzene 0.4342 lb/MMscf Xylenes 0.7844 lb/MMscf n-Hexane 48.8543 lb/MMscf 224-IMP 0.0301 Ib/MMscf 123/9BB2 13 W E 284?.CA One (1) water transfer pump, rated at 600 scf/hr (Sandpiper. Model G1 F. 008 Serial number 2091610). Section 04: Pump Information Manufactur Sandpiper Model Number: GlF Serial Pump Number: 2091610 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O uncontrolled * la-e 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/Ib-mol) at 60F and 1 atm C coo scf/hr MW 227 Ib/Ib-mol Hours of 06 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole 94 MW mass fraction Component lb/hr lb/yr tpy CO2 2.35 44 0.0464 CO2 1.637 14339.588 7.170 nitrogen 0.82 28 0.0103 nitrogen 0.363 3184.110 1.592 methane 74.30979 16.04 0.5345 methane 18.870 165297.599 82.649 ethane 11.6698 30.07 0.1574 ethane 5.555 48664.581 24.332 propane 6.9439 44.09 0.1373 propane 4.847 42458.017 21.229 isobutane 0.6437 58.12 0.0168 isobutane 0.592 5188.302 2.594 n-butane 1.9641 58.12 0.0512 n-butane 1.807 15830.891 7.915 isopentane 0.3384 72.15 0.0109 isopentane 0.387 3385.963 1.693 n-pentane 34348 72.15 0.0141 n-pentane 0.497 4350.523 2.175 cyclopentane 0.0344 72.15 0-0011 n-pentane 0.039 344.200 0.172 n-hexane 0.0936 86.18 0.0036 n-hexane 0.128 1118.661 0559 123/9992 13WE2849.CP1 cyclohexane 0024; 84.18 0.0009 cyclohexane 0.032 281.347 0.141 Other hexanes 0.1573 86.18 0.0061 Other hexanes 0.215 1885.948 0.943 heptanes 0.0802 100.21 0.0036 heptanes 0.127 1114.555 0.557 methylcyclohexa 0.0189 98.19 0.0008 methylcyclohe 0.029 257.362 0.129 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 Benzene 0.0174 78.11 0.0006 Benzene 0.022 188.483 0.094 Toluene 0.0119 92.14 0.0005 Toluene 0.017 152.059 0.076 Ethylbenzene 0.0014 106.17 0.0001 Ethylbenzene 0.002 20.613 0.010 Xylenes 0.0042 106.17 0.0002 Xylenes 0.007 61.840 0.031 C8+ Heavies 0.051 116 0.0027 C8+ Heavies 0.094 820.435 0.410 Mass Fraction VOC: 0.2505 Total 38.730 Heating Value I 1285 BTU/scf Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMBtu 0.37 I lb CO/MMBtu I Notes Mole 55,MW,and mass fractions from: State Antelope J-F-I2HNB.`acility sales gas analysis,dated 8/26/2013 Emissions Summary Uncontrolle tpy NOX ncontrolle d/PTE 1.2 tpy CO 38.7 tpy VOC Controlled 1.9 tpy VOC Reportable Controlled CAS# Total (lb/yr) tpy ? Total n-hexane ':10543 1118.7 0.5593 Yes 56 224-TMP 540841 1.6 0.0008 No 0 Benzene 71432 188.5 0.0942 No 9 Toluene 108883 152.1 0.0760 No 8 E-Benzene 100414 20.6 0.0103 No 1 Xylenes 1330207 61.8 0.0309 No 3 Resultant Emission Factors VOC 14737.594 lb/MMscf natural gas used Benzene 35.861 lb/MMscf natural gas used n-hexane 212.835 lb/MMscf natural gas used Toluene 28.931 lb/MMscf natural gas used E-Benzene 3.922 lb/MMscf natural gas used Xylenes 11.766 lb/MMscf natural gas used 224-TMP 0.301 lb/MMscf natural gas used 123/9882 13WE2849.CP1 009 One ememeecr Clare with a minimum combustion ficlencv of :%. The flare P not enclosed. Equipment Description This source vents natural gas from: is well head separator when pipeline not available Emissions from this source are. I routed to a flare Natural gas venting from a well head separator wnen pipeline not availaole_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=O'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 set/lb-mop at 608 and 1 atm Throughput 101 11 MMscf/yr 1264.7 sot/nr 0.94 MMsctmo MW 22.300 10/Ibmol 0.030 MMsofld mole W. ]MW Ibx/lbmol mass fraction E lb/hr Ib/yr tpy Helium bet; 40026 0.000 0.000 Helium 0.0 12 0.01 C02 235 44.01 1.034 0.046 C02 3.5 30233 15.12 N2 082 28.013 0.230 0.010 NO 0.8 o 6715 3.36 methane I 74.30979 16.041 11.920 8535 methane 39.8 348455 174.23 ethane 1 n 6690 30.063 3.508 0.157 ethane 11.7 102557 51.28; propane 6.9439 44.092 3.0617 0.137 propane 10.2 89502] 44.75 13obutene 0.9437 58.118 0.3741 0.017 isobatane 0.2 10936 547 n-butane 19641 58.118 1.1415 0.051 h.-butane 3.8 33369 16.68 isopentane 433384 72.114 0.2440 0.011 Ilsopentane 0.8 7134 3.57 n-pentane• 84348 72.114 0.3136 0.014 ]n-pentane 1.0 9166 4.58 cyclopentane C.5344 70.13 0.0241 0.001 Icyclopentane 0.1 705 0.35 n-Hexane 0.0535 86.18 0D807 0.0036 in-Hexane 0.3 2358 1.18 cyclohexane 00240 84.16 0.0203 0.001 Icyclohexane 0.1 593] 0.30 Other hexanes 01578 86.18 0.1360 0.006 'Other hexanes 0.5 3975 1.99 heotanes 00803 100.21 0.0804 o 0.004 Iheptanes 0.3 2349 1.17 methylcyclohexane 0 018 98.19 0.0186 0.001 Imethylcyclohexane 0.1 542; 0.27 224-TMP opool '.14.23 0.0001 0.000 224-TMP 0.0 a] 0.00 Benzene 00174 7812 0.C136 0.0006 'Benzene 0.0 397] 0.20 Toluene 0t119 92.'5 C.0110 00005 Toluene 0.0 3211 0.16 Ethylbenzene 00014 106.17 0.0015 00001 Ethylbenzene 0.0 43] 0.02 Xylenes 0.0042 106.:7 0.0045 0O002 Xylenes 0.0 1301 007 • 08+Heavies o es1 116.000 0.0592 0.0027 08+Heavies ] D.2 1729 0.86 vOC mass fraction: 02004 Total VOC emissions(uncontrolled) 816 22.277 Notes More Pe end MW are based or.State Antelope 3-F-12HNe facility sales gas analysis,dated 8/22572013 Emosions are based on 384 flours or operation per year. i calculated the average MW of 08+based on the average MW on me analysis for the gas but source used 116.Used source's value since minimal difference. Flaring Information Equipment Description Flare to combust produced gas when pipeline is not available Manufacturer TOD Model TED Serial Numner TOD Gas Heating Value 1285 Btu/scf Throughput 14236.772 MMBtu/yr 123/9352 1390'21849.291 VRU Information-Not applicable Equipment Description 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, 0.48 tpy NOX 2.63 tpy CO Emissions Summary 0.5 tpy NOX tJncontrolled/PTE 2.6 tpy CO 81.6 tpy VOC Controlled 4.1 tpy VOC Uncontrolled Controlled Total Total(Ib/yr) Reportable? (Ib/yr) Benzene 397 Yes 20 Toluene 321 Yes 16 Ethylbenzene 43 1 No 2 Xylenes 130 No 7 n-hexane 2358 Yes 118 224-TMP 3 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 LA applies to all emission sources."No person,wherever located,shall cause or allow the emission AQCC Regulation 3 Is puo'.c comment Public Comment Required requ'red? Emission Factors for Permit controlled NOX 87.38 -1b/MMscf CO 475.45 Ib/MMscf VOC 14735.2497 Ib/MMscf Benzene 35.8651 lb/MMscf Toluene 28.9336 lb/MMscf Ethylbenzene 3.9218 lb/MMscf Xylenes 11.7655 Ib/MMscf n-Hexane 212.8350 Ib/MMscf 224-TMP 0.3014 lb/MMscf Controied NOX 87.38 lb/MMscf CO 475.45 lb/MMscf VOC 736.7625 lb/MMscf • Benzene 1.7933 lb/MMscf Toluene 1.4467 lb/MMscf Ethylbenzene 0.1961 lb/MMscf Xylenes 0.5883 Ib/MMscf n-Hexane 10.6418 lb/MMscf 224-TMP 0.0151 lb/MMscf 123/9882 13W tss49.CP1 C) II 2 d cc CC o O w O) cc cc cn u. U cn c c a) CI a)(Oct 00000 a) co O Z vC > > > > > > Z )- ZZZ Z Z Z > > ›- Cc O 0 0 0 0 C O C C O c E h 0 E C on c o o 2.U w' Mn co co ≥. r (O M r CO r c.; r c9L m r )n O C'J O Ln o — m r) Lc) r-. N N w 40 - Lo 0 r 0 CO N m N r ,- UJ ( V CO 0 H N CO 0 `� N r 0 a. m 0 CO N cn o ` m ar r cn cn U C a, d n (n C'] ifJ �. O] CV r to mc. N CO N N • O• a) '2 r m w — an r C cc c- m N O) ,— 2) N r G _ v) N c" an m .n N r Lc C T T ) J ^ U z w CO a cc a) c 0 To m '`n . c 7 'N o 2 E a U G w J r co N N N Zr V N• 0 O O S a N • O 0 O In In r— a In LO U O O O N N N N N CO 0 LL N co n E E E 'n `n (n a co - y r r O a) a) N a] a) N aJ al C) N a) N a) a) 2 2 2 a a a n a c c a- c n n u_ u) (n O C 0 C Ca C (C 0 C N (0 (c s c t s c C) en Lin c daa UGC) CU c» 2 Vo' r00 o w w W o (n = = ZNN NNN NN � ONNN CO Op-d 2 C C. C V Q v V (1) N O E O ❑ O o a o d d . .1 d c To ti 0 G w U U U C < < < Q I < Q . ; CO cc 0-5 < < _ m m O) 0 CD U U U U U U U O O C C C co 0 0 0 0 N .n N N CO N 'n j( _ Z 0 a 'N o_ 0 0 0 0 o o_ o o > a > > > > 2 Z U c .n o) may o� _o L In _O n . . . . _0 a a _O _0 70 _O w r r m a) co a a r co co cn co r a cc cc V O - O O (D 0 m C) CO 0 CO C) r 0 c N N C m n) CO. LO O r C O O V C o c 0 Nn r c Ln — V r O : ; r (c sr 0 r m — C .. 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