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Address Info: 1150 O Street, P.O. Box 758, Greeley, CO 80632 | Phone:
(970) 400-4225
| Fax: (970) 336-7233 | Email:
egesick@weld.gov
| Official: Esther Gesick -
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20143890.tiff
* CDPHE COLORADO CO .- Department of Public Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board RECEIVED 1150 O St PO Box 758 Greeley, CO 80632 DEC ; 1 2y,° December 8, 2014 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On December 10, 2014, the Air Pollution Control Division will begin a 30-day public notice period for Bonanza Creek Energy Operating Company LLC - North Platte 44-13 Production Facility (COGCC #310744). A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30) days from the beginning of the public notice period. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health Et Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 6ff:CO T 4300 Cherry Creek Drive S., Denver,CO 80246.1530 P 303-692-2000 www-colorado.gov/cdphe �� `° `Qi" John W. Hickenlooper, Governor I Larry Wolk,MD,MSPH,Executive Director and Chief Medical Officer .' ;;" 12-/-7- 1 C� �C , 1/2 2014-389 0 CDPHE Air Pollution Control Division co lof Notice of a Proposed Project or Activity Warranting Public ' Comment Website Title: Bonanza Creek Energy Operating Company LLC - North Platte 44-13 Production Facility (COGCC #310744) - Weld County Notice Period Begins: December 10, 2014 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: North Platte 44-13 Production Facility (COGCC #310744) Oil and gas exploration and production facility SESE Section 13, T5N, R63W Weld County The proposed project or activity is as follows: Oil and gas exploration and production facility including a low-pressure separator, condensate loading into trucks, a pneumatic pump, flare venting and associated fugitive emissions. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application, the Division's analysis, and a draft of Construction Permit 13WE2974 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: Christian Lesniak Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 1 I ®Y COLORADO oAwms..atoa..' STATE OF COLORADO •LO- • ■• D - • -T' •F P = C HEALTH AND ENVIRONMENT Rbop �° AIR POLLUTION CONTROL DIVISION n A A TELEPHONE: (303) 692-3150 „ *; 'slues: CONSTRUCTION PERMIT PERMIT NO: 1 3WE2974 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 North Platte 44-13 Production Facility, located in the SESE Section 13, Township 5N, Range 63W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID TL 005 Truck Condensate Loadout FUG 006 Fugitive equipment leaks HLP Sep-1 007 Separator controlled by a flare stack. Flare has a minimum combustion efficiency of 95%. The flare is enclosed. One (1) pneumatic pump used for water transfer (Make: P-1 008 Sandpiper,Model: G1F, Serial Number: 2091630) rated at 600 scf/hr. Controlled by a flare stack. Flare has a minimum combustion efficiency of 95%. The flare is enclosed. FL-1 009 Emergency Flare, controlling separator. 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 1. 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 AIRS ID: 123/7401 Page 1 of 15 olor Depa en li ealth and Environment it Pollution Control Division owner or oper li f-c lianc ' 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). 2. 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.) 3. AIRS 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. 4. 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 5. 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 TL 005 9.0 Point FUG 006 10.3 Fugitive HLP Sep-1 007 0.4 7.1 2.0 Point P-1 008 0.2 2.0 1.3 Point FL-1 009 1.0 9.1 5.7 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. 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. 6. 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 AIRS ID: 123/7401 Page 2 of 15 I olor- Depa en . P .li `Health and Environment A •it Pollution Control Division shall maintain. . - of - e-=: . c. - , count- _:' 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. 7. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit (Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID HLP Sep-1 007 Flare VOC, HAPs P-1 008 Flare VOC, HAPs FL-1 009 Flare VOC, HAPs PROCESS LIMITATIONS AND RECORDS 8. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Equipment Point Process Parameter Annual Limit ID TL 005 Oil Loaded 83220 BBL HLP Sep-1 007 Gas Vented from Separator 5.9 MMSCF P-1 008 Natural Gas 5.3 MMSCF FL-1 009 Gas Vented from Separator 23.3 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. 9. AIRS Point 007: Upon installation of the flow meter required under Condition 03, 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 08 and to calculate emissions as described in this permit. AIRS ID: 123/7401 Page 3 of 15 olor Depa en li ealth and Environment it Pollution Control Division STATE AND FEDE G T E NT 10. Points 007 — 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) 11. 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.) 12. This source is subject to the odor requirements of Regulation No. 2, (State only enforceable) 13. 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) 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 13 (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. 14. 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. 15. 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. 16. 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: 123/7401 Page 4 of 15 olorl Depa en . - .eh ' Health and Environment •it Pollution Control Division a. Direct. _ --cti = -na° - - •escr'- n 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. H. 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. Hi. 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 17. Points 007-009: 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 18. Point 006: Within one hundred and eighty days (180) after issuance of this permit, the owner or operator shall complete the initial extended gas analysis of gas samples that AIRS ID: 123/7401 Page 5 of 15 Depa en li ealth and Environment it Pollution Control Division • are representDolor •' r m C) t ay be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 19. 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. 20. Point 009: The owner or operator shall demonstrate compliance with opacity standards, using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.1 &4) Periodic Testing Requirements 21. 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 1. 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. 2. 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. 3. 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 22. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, 'LC) 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 (NOV.) in ozone nonattainment areas emitting less than 100 tons of VOC or NOx per AIRS ID: 123/7401 Page 6 of 15 olor.� Depa en . di "Health and Environment A it Pollution Control Division year, -, - in < a ': - e - _:'• -f one 'n 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. f. Within 14 calendar days of commencing operation of a permanent replacement engine under the alternative operating scenario outlined in this permit as Attachment A. The APEN shall include the specific manufacturer, model and serial number and horsepower of the permanent replacement engine, the appropriate APEN filing fee and a cover letter explaining that the owner or operator is exercising an alternative-operating scenario and is installing a permanent replacement engine. 23. 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). 24. 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 25. 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. 26. 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 AIRS ID: 123/7401 Page 7 of 15 epa en li Health and Environment it Pollution Control Division III.G. Final aDolor n an he o ' n 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. 27. 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. 28. 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. 29. 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. 30. 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. 31. 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: • Christian Lesniak Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/7401 Page 8 of 15 olor.i Depa en . P .Ii Health and Environment it Pollution Control Division Notes to Permit Holder I o ...- 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&childpaqename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper AIRS ID: 123/7401 Page 9 of 15 olor Depa en li Health and Environment it Pollution Control Division 4) The following emis ' n • le ' s are ted 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) 005 Benzene 71432 321.9 Yes 321.9 005 n-Hexane 110543 1932.6 Yes 1932.6 005 Toluene 108883 769.4 Yes 769.4 005 Xylenes 1330207 •609.8 Yes 609.8 006 Benzene 71432 149.9 No 149.9 006 n-Hexane 110543 855.2 Yes 855.2 006 Toluene 108883 307.6 Yes 307.6 006 Ethylbenzene 100414 49.7 No 49.7 006 Xylenes 1330207 233.4 No 233.4 007 Benzene 71432 740.6 Yes 37 007 n-Hexane 110543 4484.9 Yes 224.2 007 Toluene 108883 596.8 Yes 29.8 007 Ethylbenzene 100414 62.8 No 3.1 007 Xylenes 1330207 213.2 No 10.7 008 Benzene 71432 211.2 _No, 10.6 008 n-Hexane 110543 1227.4 Yes 61.4 008 Toluene 108883 191.7 No 9.6 008 Ethylbenzene 100414 23.6 No 1.2 008 Xylenes 1330207 67.7 No 3.4 009 Benzene 71432 936.5 Yes 46.8 009 n-Hexane 110543 5441.2 Yes 272.1 009 Toluene 108883 849.8 Yes 42.5 009 Ethylbenzene 100414 104.4 No 5.2 - 009 Xylenes 1330207 300.2 Yes 15 AIRS ID: 123/7401 Page 10 of 15 olor-k Depa en • P •li Health and Environment •it Pollution Control Division 5) The emission level :;.- d i p- L - b- .• >- folio - -- ission factors: Point 005: Emission Factors - Uncontrolled Pollutant lb/BBL loaded Source VOC 0.2152 AP-42 Benzene 0.0039 AP-42 n-Hexane 0.0232 AP-42 Toluene 0.0093 AP-42 Xylenes 0.0073 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) = 5.28 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 vapors by the VOC emission factor. AIRS ID: 123/7401 Page 11 of 15 olor epa en lift and Pollutionealth ControlEnvironment Division Point 006: Component Gas Heavy Oil Light Oil Water/Oil Connectors 1195 0 480 333 Flanges 62 0 12 14 Open-ended Lines 38 0 4 1 Pump Seals 4 0 0 1 Valves 177 0 64 39 Other 82 0 10 14 VOC Content(wt. 0.2598 0 0.9947 1 fraction) Benzene Content(wt. 0.0007 0 0.018 0.0012 fraction) Toluene Content(wt. 0.0006 0 0.043 0.0003 fraction) Ethylbenzene(wt. 0.0001 0 0.0069 0.0001 fraction) Xylenes Content(wt. 0.0002 0 0.0341 0.0001 fraction) n-hexane Content(wt. 0.0039 0 0.1079 0.0001 fraction) *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors(kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: Standard EFs-EPA-453/R-95-017 Table 2-4 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 and liquids analyses. AIRS ID: 123/7401 Page 12 of 15 olorl Depa en - ' di 'Health and Environment it Pollution Control Division Point 007: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx Ob/MMBTU) --- 0.068 0.068 AP-42 (lb/MMBTU) CO(lb/MMBTU) --- 0.37 0.37 AP-42 VOC 55.20 47770.234 2388.5117 Gas Analysis Benzene 0.00145 125.5279 6.2764 Gas Analysis Toluene 0.00117 101.1462 5.0573 Gas Analysis Ethylbenzene 0.00012 10.645 0.5323 Gas Analysis Xylenes 0.00042 36.137 1.8069 Gas Analysis n-hexane 0.0088 760.1576 38.0079 Gas Analysis _ 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 1,871 BTU/scf was used for calculations. Point 008: Emission Emission Factors- Factors- Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (lb/MMBTU) VOC 15555.0654 777.7533 Gas Analysis_ Benzene 40.1885 2.0094 Gas Analysis n-Hexane 233.5273 11.6764 Gas Analysis Toluene 36.467 1.8234 Gas Analysis Xylenes 12.8861 0.6443 Gas Analysis 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 are based on AP-42 Table 13.5-1. A HHV of 1,314 BTU/scf was used for calculations. AIRS ID: 123/7401 Page 13 of 15 R: APFTolIUt1O' loearth CoandnEnvironmenttrol Division Point 009: Weight Emission Emission Fraction of Factors Factors Pollutant Gas(%) Uncontrolled Controlled Source Ib/MMscf lb/MMscf NOx --- 0.068 0.068 AP-42 (Ib/MMBTU) CO — 0.37 0.37 AP-42 (lb/MMBTU) VOC 25.98 15554.833 777.7417 Gas Analysis I Benzene 0.0672 40.1937 2.0097 Gas Analysis Toluene 0.0610 36.471 1.8236 Gas Analysis Ethylbenzene 0.0075 4.4821 0.2241 Gas Analysis Xylenes 0.0215 12.8861 0.6443 Gas Analysis n-hexane 0.3903 233.5273 11.6764 Gas Analysis 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 are based on AP-42 Table 13.5-1. A HHV of 1,314 BTU/scf was used for calculations. AIRS ID: 123/7401 Page 14 of 15 olor- Depa en - P 'Ii 'Health and Environment •it Pollution Control Division 6) In accordance with -7- ' P• - t'ssion (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, HAPs PSD or NANSR Synthetic Minor Source of: VOC, HAPs MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.g poacceSs.o ov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart ZZZZ—Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXJ( 9) A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/7401 Page 15 of 15 Division Information Engineer: Christian Lesniak Control Engineer: Stefanie Rucker Review Date: 11/06/2014 Application Date: 10/29/2013 Facility Identifiers Permit No. 13WE2974 AIRS County It 123 Weld Facility ft 7401 Facility Type: exploration and production facility 9 Located in the 8-hour non-attainment area? O True Minor ®Synthetic Minor for: F VOC F NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: North Platte 44-13 • Source Location: SESE Section 13,Township 5N, Range 63W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street,Suite 1500 Address ty,State Zip: Denver,CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: Pvoung(WBonanzaCrk.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the North Platte 44-13, located in the SESE Section 13, Township 5N,Range 63W,Weld County,Colorado. Point Name Type Control Action Newly 005 TL Loadout None reported source Newly 006 FUG Fugitives None reported source Newly 007 HLP Sep-1 Separator Venting Flare reported source Newly 008 P-1 Pump Flare reported Source Newly 009 FL-1 Separator Venting Flare reported source 005 Truck Condensate Loadout SCC: 40600132:Crude Oil: Submerged Loading (Normal Service) Calculations L= 12.46*S*P*M/T(AP-42:Chapter 5.2, Equation 1) L= loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source 5 Saturation Factor 0.6 AP-42 P True Vapor Pressure 5.28 psia Sales Oil Analysis M Molecular Weight of Var 68 lb/lb-mole AP-42 Rankine 460 T Liquid Temperature 524 deg. R Field Data Deg F 64 L 5.12 lb/10^3 gal 2.15E-01 lb/bbl Annual requested Throughput 83220 BBL/yr 3495240 gal/yr Annual requested VOC emissions 17904 lb/yr 8.95 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0180 n-hexane 0.1079 Toluene 0.0430 Xylenes 0.0341 224 TMP 0.0122 Source: Pressurized oil analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2151 lb/bbl 8.95 tpy 8.95 tpy - AP-42 Benzene 0.0039 lb/bbl 321.94 lb/yr 321.94 lb/yr AP-42 n-Hexane 0.0232 lb/bbl 1932.57 lb/yr 1932.57 lb/yr AP-42 Toluene 0.0092 lb/bbl 769.38 lb/yr 769.38 lb/yr AP-42 Xylenes 0.0073 lb/bbl 609.82 lb/yr 609.82 lb/yr AP-42 224 TMP 0.0026 lb/bbl 217.82 lb/yr 217.82 lb/yr AP-42 Regulatory Review, ti firiab n V :ei tie Man-tc C,`t)r n6a,nn fjp', ' n 6,7 k3 This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. 006 FugINe equipment leaks Regulation 7 IntonnatIon Operating Hours: 8760 hours/year Emission Factor Source Standard EFs-EPA-453/R-95-017 Table 2-4 Control Efficiency Source: None Calculations Emission Factor(kg/hr- Emissions Service Component Type Count source) Control(%) Pollutant Mass Fraction (tpy) Table 2-4 Table 2-8 Reg.3 Connectors 1195 200E-04 100E-05 0.0% VOC 0.2598 48833807 Flanges 62 3.90E-04 5.70E-06 0.0% Benzene 0.0007 00126188 Open-Ended Lines 38 200E-03 150E-05 0 Toluene 0.0006 00108161 Gas Pump Seals 4 240E-03 350E-04 0.0% Elhylbenzene 00001 0.0018027 Valves 177 4.50E-03 2.50E-05 0.0% Xylenes 0.0002 0.0036054 Omer 82 8.80E-03 1.20E-04 0.0% n-Hexane 0.0039 0.0703048 Connectors 0 7.50E-06 7.50E-06 0.0% VOC 0 0 Flanges 0 3.90E-07 3.90E-07 0.0% Benzene 0 0 open-Ended Lines 0 1.40E-04 7.20E-06 0.0% Toluene 0 0 Heavy Oil Pump Seals 0 000E+00 000E+00 0.0% Ethylbenzene 0 0 Valves 0 800E-06 8.40E+06 0.0% Xylenes 0 0 Omer 0 3.20E-05 3.20E-05 0.0% n-Hexane 0 0 Connectors 480 2.10E-04 7.50E-05 0.0% VOC 0.9947 3.2918155 Flanges 12 1.10E-04 2240E-06 0.0% Benzene 0.018 0.0595684 Light Oil Open-Ended Lines 4 140E-03 1.40E-05 0.0% Toluene 0.043 0.1423023 Pump Seals 0 1.30E-02 5.10E-04 0.0% Elhylbenzene 00069 00228345 Valves 64 2.50E+03 1.90E-05 0.0% Xylenes 0.0341 0.112849 Other 10 7.50E-03 1.10E-04 0.0% n-Hexane 0.1079 0.3570794 Connectors 333 1.IDE-04 1.00E-05 0 VOC 1 2.2862533 Flanges 14 2.90E-06 2.90E-06 00% Benzene 0.0012 0.0027435 Water/Oil Open-Ended Lines 1 2.50EM 3.50E-06 0.0% Toluene 0.0003 0.0006859 Pump Seals 1 2.40E-05 240E-05 0.0% Elhylbenzene 0.0001 0.0002286 Valves 39 9.80E-05 9.70E-06 0.0% Xylenes 0.0001 0.0002286 Other 14 140E-02 5.90E-05 00% n-Hexane 0.0001 0.0002286 Emisalons Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source VOC 10.26 spy 1026 Ipy Standard EFs-EPA-453/R-95-017 Table 2-4 Benzene 149.86 lb/yr 149.86 Ib/r Standard EFs-EPA-453/R-95-017 Table 2-4 Toluene 307.61 lb/yr 307.61 lb/yr Standard EFs-EPA-453/R-95-017 Table 2-4 Elhylbenzene 49.73 lb/yr 4973 Ils/yr Standard EFs-EPA-453/R-95-017 Table 2-4 XNenes 23337 lb/yr 233.37 bar Standard EFs-EPA-453/R-95-017 Table 2-4 n-Hexane 855.23 lbryr 855.23 lb/yr Standard EFs-EPA-453/R-95-017 Table 2-4 Regulatory Applicability Reg.3 Operator has agreed on the Division's standard conditions for RAC]. Separator controlled by a flare stack.Flare has a minimum combustion efficiency of 95%. The flare is 007 enclosed. SCC 31000205 Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare • Natural gas venting from a well head separator.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas`MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(CO 5.9 MMsGyr 6715159817 sd/hr MW 32.8 IbAb-mol 0.016164384 MMsd/d mole% MW Ibx/Ibmol mass traction IbAr Ibyr Ipy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.69 44.01 1.184 0.038 2.10 18429.82 9.21 N2 0.19 28.013 0.053 0.002 0.09 828.58 0.41 methane 38.05 16.041 6.103 0.188 10.85 95009.73 47.50 ethane 24.48 30.063 7.360 0.224• 13.08 114582.59 57.29 propane 20.89 44.092 9.210 0.281 18.37 14338124 71.69 isobutene 2.32 58.118 1.350 0.041 2.40 21014.38 10.51 n-butane 6.83 58.118 3.968 0.121 7.05 61766.55 30.88 isopentane 125 72.114 0.899 0.027 1.60 14002.43 7.00 n-pentane 1.60 72.114 1.152 0.035 2.05 17933.84 8.97 cydopentane 0.11 70.13 0.077 0.002 0.14 1202.00 0.60 n-Hexane 0.33 88.18 0.288 0.0088 0.51 4484.93 2.24 cydohexane 0.09 84.18 0.075 0.002 0.13 1168.65 0.58 Other haxanes 0.54 86.18 0.469 0.014 0.83 7303.61 3.65 heptanes 0.26 100.21 - 0.265 0.008 0.47 4121.51 2.06 me864cydohexa a 0.07 98.19 0.069 0.002 0.12 1068.93 0.53 224-TMP 0.0002 114.23 0.000 0.00001 0.00 3.56 0.00 Benzene 0.0609 78.12 0.048 0.00145 0.08 740.61 0.37 Toluene 0.0416 92.15 0.038 0.00117 0.07 596.76 0.30 E6tylbenzene 0.0038 106.17 0.004 0.00012 0.01 62.81 0.03 )(ylenes 0.0129 106.17 0.014 0.00042 0.02 213.21 0.11 08+Heavies 0.15 115.7 0.179 0.00545 0.32 2781.37 1.39 VOC mass frad 0.5520 Total VOC(Uncontrolled) 140.92 32.80565437 Notes Mole%,MW,and mass fractions from North Platter T-P-13HNB L.P.Separator gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of Ce+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model Two L30-0100 Serial Number 20948&20949 Gas Heating Value 1871 Btu/scf Throughput 11038.9 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make Model Requested Control 0.00% Annual Bypass Tim 0.00% Backup None Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.068 lb NOX/MMBtu 0.37 llb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 47770.23 lb/MMscf 2388.51 lb/MMscf 140.92 tpy 7.05 tpy Gas Analysis box 0.068 Ib/MMBTU 0.07 Ib/MMBTU 0.38 tpy 0.38 tpy AP-42 CO 0.370 Ib/MMBTU 0.37 Ib/MMBTU 2.04 tpy 2.04 tpy AP-42 Benzene 125.53 lb/MMsd 6.28 lb/MMscf 740.61 lb/yr 37.03 lb/yr Gas Analysis n-Hexane 760.16 Ib/MMsd 38.01 lb/MMscf 4484.93 lb/yr 224.25 lb/yr Gas Analysis Toluene 101.15 lb/MMscf 5.06 lb/MMscf 596.76 lb/yr 29.84 lb/yr Gas Analysis Xylenes 36.14 Ib/MMsd 1.81 lb/MMsd 213.21 lb/yr 10.66 lb/yr Gas Analysis Ethylbenzene 10.65 lb/MMscf 0.53 lb/MMscf 62.81 lb/yr 3.14 lb/yr Gas Analysis Source will be required to install flow meter. Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section ILA.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AQCC Regulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air." One(1)heat trace circulation pump(Make:Sandpiper,Model:GI F,Serial 008 Number 2091630)rated at 600 scf/hr. Pump Information 'Manufactur Sandpiper Model Number.GlF Serial Pump Number 2091630 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control Fare 95.00%Efficiency Calculations . 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/valume 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 sc/Ib-mol)at 60F and 1 atm • • Q 600 sd/hr MW 22.679 Ib/Ib-md Hours 0109. 8760 901.91/11 Requested Throughput 5.256 MMsd/yr Component mole% MW mass fraction Component lb/hr lb/yr spy . CO2 2.29 44 0.0444 CO2 1.595 13973.471 6.987 nitrogen 052 28 0.0064 nitrogen 0.231 2019.192 1.010 methane 72.45754 16.04 0.5125 methane 18.399 161177.381 80.589 ethane 13.3297 30.07 0.1767 ethane 6.345 55586.579 27.793 propane 7.2375 44.09 0.1407 propane 5.052 44253.214 22.127 isobutane 0718 58.12 0.0184 isobutane 0.661 5787.169 2.894 n-butane 20491 58.12 0.0525 n-butane 1.884 16507.941 8.254 isopentane 0362 72.15 0.0115 Isopentane 0.413, 3622.105 1.811 n-pentane 0401 72.15 0.0147 n-pentane 0.527 4612.681 2.306 cyclopentane 0.0324 70.15 0.0010 cyclopentane 0.036 315.202 0.158 n-hexane 0.1027 86.18 0.0039 n-hexane 0.140 1227.420 0.614 cydohexane 0.0284 84.18 0.0011 cydohexane 0.038 331.546 0.166 Other hexanes o.ie85 86.18 0.0063 Other hexanes 0.227 1989.926 0.995 heptanes lime 100.21 0.0038 heptanes 0.138 1207.666 0.604 methylcyclohexa 0.0237 98.19 0.0010 methylcyclohe 0.037 322.724 0.161 224-IMP 0.5001 114.22 0.0000 224-IMP 0.000 1.584 0.001 Benzene 0.0195 78.11 0.0007 Benzene 0.024 211.231 0.106 Toluene 0015 92.14 0.0006 Toluene 0.022 191.671 0.096 Ethylbenzene o.mt9 106.17 0.0001 Ethylbenzene 0.003 23.558 0.012 Xylenes 0.8046 106.17 0.0002 Xylenes 0.008 67.729 0.034 C84 Heavies 0.0939 122.33054 0.003447 C8. Heavies 0.124 1084.056 0.542 Mass Fraction VOC 0.2599 Total VOC 40.879 _Heating Value I 1314 BTU/sd I Combustion emission M1cbr source: AP-42:Chapbr 13.5 0.07 I n NOXIMMBN 0.37 I I CMAMON BWs Mole%,MW,and mass fractions from North Plots T-P-131we Sales LYw gam eml)m.PedwmN September 20.2013 Emissions Summary Table Pollutant Uncontrolled Emission Fac Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 15555.07 Ib/MMscf 777.75 lb/MMsd 40.88 tpy 2.04 tpy Gas Analysis Not 0.07 Ib/MMBIII 0.0716/MMBTU 0.23 tpy 0.23 tpy AP-42 CO 0.37 Ib/MMBIU 0.37 lb/MMBTU 1.28 tpy 1.28 tpy AP-42 Benzene 40.19 lb/MMsd 2.01 lb/MMsd 211.23 lb/yr 10.56 NM Gas Analysis • n-Hexane 233.53 lb/MMscf 11.68 lb/MMsd 1227.42 lb/yr 61.37 lb/yr Gas Analysis Toluene 36.47 lb/MMsd 1.82 lb/MMsd 191.67 lb/yr 9.58 lb/yr Gas Analysis Xylenes 12.89 lb/MMscf 0.64 lb/MMsd 67.73 lb/yr 3.39 lb/yr Gas Analysis Ethylbenzene 4.48 lb/MMscf 0.22 lb/MMsd 23.56 lb/yr 1.18 lb/yr Gas Analysis Emergency Flare,controlling separator.Flare has a minimum combustion efficiency of 95%. The flare is/is 009 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. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW*Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(O) 23.3 MMscfNr 2659.817352 scf/hr MW 22.679 lb/lb-mol 0.063835616 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.01 4.0026 0000 0.000 0.00 24.61 0.01 CO2 219 44.01 1.008 0.044 7.07 61958.88 3098 N2 0.52 28.013 0.146 0.006 1.02 8955.29 4.48 methane 72.45754 16.041 11.623 0.512 81.57 714548.54 357.27 ethane 13.3297 30.063 4.007 0.177 28.12 246359.55 123.18 propane 72375 44.092 3.191 0.141 22.40 196184.68 98.09 isobulane 0.718 58.118 0417 0.018 2.93 25653.81 12.83 n-butane 2.0481 58.118 1.190 0.052 8.35 73177.66 36.59 isopentane 0.362 72.114 0.261 0.012 1.83 16048.89 8.02 n-pentane 0.461 72.114 0.332 0.015 2.33 20437.94 10.22 cydopentane 00324 70.13 0.023 0.001 0.16 1396.90 0.70 n-Hexane 0.1027 86.18 0.089 0.004 0.62 5441.19 2.72 cyclohexane 0.0284 84.16 0.024 0.001 0.17 1469.40 0.73 Otherhexanes 0.1665 86.18 0.143 0.006 1.01 8821.40 4.41 heptanes 0.0869 100.21 0.087 0.004 0.61 5353.62 2.68 methylcyclohexane 0.0237 98.19 0.023 0.001 0.16 1430.65 0.72 224-TMP 0.0001 114.23 0.000 0.000 0.00 7.02 0.00 Benzene 0.0195 78.12 0.015 0.001 0.11 936.51 047 Toluene 0.015 92.15 0.014 0.001 0.10 849.77 0.42 Ethylbenzene 0.0016 106.17 0.002 0.000 0.01 104.43 0.05 Xylenes 0.0046 106.17 0.005 0.000 0.03 300.25 0.15 C8+Heavies 00639 122.5299994 0.078 0.003 0.55 4813.49 2.41 VOC mass frail 0.2599 Total VOC(Uncontrolled) 181.21 Notes Mole%,MW,and mass fractions from North Platte T-P-I3HNB Sales Line gas analysis.Performed September 20,2013 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 pi line is available at this wellhead facility.Manufacturer TBD Model TBD Serial Number TBD Gas Heating Value 1314 Btu/scf Throughput 30616.2 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make Model Requested Control I 0.00% Annual Bypass 11 0.00% Backup None Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 IIb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 15554.83 lb/MMscf 777.74 lb/MMscf 181.21 tpy 9.06 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 1.04 tpy 1.04 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 5.66 tpy 5.66 tpy AP-42 Benzene 40.19 lb/MMscf 2.01 lb/MMscf 936.51 lb/yr 46.83 lb/yr Gas Analysis n-Hexane 233.53 lb/MMscf 11.68 lb/MMscf 5441.19 lb/yr 272.06 lb/yr Gas Analysis Toluene 36.47 lb/MMscf 1.82 lb/MMscf 849.77 lb/yr 42.49 lb/yr Gas Analysis Xylenes 12.89 lb/MMscf 0.64 lb/MMscf 300.25 lb/yr 15.01 lb/yr Gas Analysis Ethylbenzene 4.48 lb/MMscf 0.22 lb/MMscf 104.43 lb/yr 5.22 lb/yr Gas Analysis Regulatory Applicability AQCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' 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