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Home My WebLink About20142248.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD,MSPH . cot° Executive Director and Chief Medical Officer l,e vo Dedicated to protecting and improving the health and environment of the people of Colorado * v 4300 Cherry Creek Dr.S. Laboratory Services Division ./876 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.gov/cdphe and Environment Weld County - Clerk to the Board 1150O St PO Box 758 Greeley, CO 80632 RECEIVED July 17, 2014 JUL 2 3 2014 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On July 23, 2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy— North Platte K-22 Production Facility, 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, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure emu, koi;a,,, &,_; el IMirrifI ) PIA (WI UDE 2014-2248 -7-23-► f STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH oF c,ozoR Executive Director and Chief Medical Officer Re90 Dedicated to protecting and improving the health and environment of the people of Colorado {" o P 9 P P + �*+ 4300 Cherry Creek Dr.S. Laboratory Services Division r 1876• Denver,Colorado 80246-1530 8100 Lowry Blvd. Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department • Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy—North Platte K-22 Production Facility—Weld County Released To: The Greeley Tribune On: July 17, 2014 Published: July 23, 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 Facility: North Platte K-22 Production Facility Exploration and Production Facility NWNE Sec. 22 T5N R63W Weld County The proposed project or activity is as follows: The applicant proposes to operate a new oil and gas production facility The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3,Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3,Part B, Section II1.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 14WE0494 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at www.colorado.gov/cdphe/AirPublicNotices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: David V. Thompson Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South,APCD-SS-B 1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us . STATE OF COLORADO . COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT ,� AIR POLLUTION CONTROL DIVISION II ri TELEPHONE: (303)692-3150 .�* � as . CONSTRUCTION PERMIT PERMIT NO: 14WE0949 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 PlatteK-22 Production Facility (COGCC#433629), located in the NWNE, SEC22, T5N, R63W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Condensate Six (6) above ground 500 bbl atmospheric condensate storage Tank 003 tank One (1) above ground 400 bbl and two (2) 60 bbl concrete vaults PW Tanks 004 used to store produced water. The 400 bbl tank is controlled by an enclosed flare TL 005 Truck Condensate Loadout FUG 006 Fugitive VOC leak emissions FL-1 007 Flare used before sales gas could be sent to the sales gas pipeline. The flare is not enclosed. FL-2 008 Emergency Flare. The flare is not enclosed Sep-1 009 Separator controlled by a 40' flare stack. Flare has a minimum combustion efficiency of 95%. The flare is enclosed. Separator controlled by a 40' flare stack. Flare has a minimum Sep-2 010 combustion efficiency of 95%. The flare is enclosed. P-1 011 One (1) Sandpiper Cl F pneumatic pump used for water transfer Point 011: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. AIRS ID: 123/9BDF Page 1 of 16 olor Depa en Ii Health and Environment it Pollution Control Division THIS PERMIT IS G R REG ONS 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. Points 003, 004, 005, 006, 009, 010, 011: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, l 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. Point 008: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after startup by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at I 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. 3. Points 003, 004, 005, 006, 009, 010, 011: 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). 4. Point 008: Within one hundred and eighty days (180) after startup, 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). 5. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 6. 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. R f r n : Regulation No. 3, Part B, Section III.E.eeece ) ( 9 7. Point 008: The following information shall be provided to the Division within fifteen (15) days after start-up. • manufacturer • model number • serial number AIRS ID: 123/9BDF Page 2 of 16 olor Depa en . P .li Health and Environment •it Pollution Control Division This informati.,� �e ;' .e i""e • he-•iF>>,..: ' Start a _.-bmitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 8. 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 9. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Emission Type VOC CO Equipment ID Point NO, Condensate 003 5.3 Point Tank PW Tanks 004 --- 0.8 --- Point TL 005 --- 18.7 --- Point FUG 006 --- 12.1 --- Fugitive FL-1 007 0.1 0.4 0.3 Point FL-2 008 0.5 3.7 2.4 Point Sep-1 009 0.4 9.3 1.8 Point Sep-2 010 0.4 9.3 1.8 Point P-1 011 0.3 2.0 1.3 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. 10. 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 and liquids analyses, as required in the Compliance Testing and Sampling section of this AIRS ID: 123/9BDF Page 3 of 16 olor Depa en li Health and Environment it Pollution Control Division permit. The sh a ec e res f component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. 11. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Point Cont r Equipment ID of Device Pollutants Controlled Condensate Tank 003 Enclosed Flare VOC, HAPs PW Tanks (400 bbl tank only) 004 Enclosed Flare VOC, HAPs FL-1 007 Open Flare VOC, HAPs FL-2 008 Open Flare VOC, HAPs Sep-1 009 Enclosed Flare VOC, HAPs Sep-2 010 Enclosed Flare VOC, HAPs P-1 011 Enclosed Flare VOC, HAPs PROCESS LIMITATIONS AND RECORDS 12. 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 Point Process Parameter Annual Limit Equipment ID Condensate Tank 003 Condensate Throughput 162060 BBL PW Tanks 004 Produced Water Throughput 109500 BBL TL 005 Oil Loaded 162060 BBL FL-1 007 Gas Vented from Separator 1.1 MMSCF FL-2 008 Gas Vented from Separator 10 MMSCF Sep-1 009 Gas Vented from Separator 11.1 MMSCF Sep-2 010 Gas Vented from Separator 11.1 MMSCF P-1 011 Natural Gas 5.3 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. STATE AND FEDERAL REGULATORY REQUIREMENTS AIRS ID: 123/9BDF Page 4 of 16 olor Depa en P li Health and Environment it Pollution Control Division 13. Points 003, I=° 0 01 a per . umber and AIRS ID point number (e.g. 123/4567/890) shall be marked on all applicable equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 14. Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 4.) 15. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 16. Point 003: No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 17. Point 003: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 18. Point 003: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 19. 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. 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 18 (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. AIRS ID: 123/9BDF Page 5 of 16 olor Depa en li Health and Environment it Pollution Control Division 21. Point 005: car li ' ad' tions, rdless 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. 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. 23. Point 006: Minor sources in designated nonattainment or attainment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection shall 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 AIRS ID: 123/9BDF Page 6 of 16 = olor Depa en �f PI•li .Health and Environment , a it Pollution Control Division si th ithin .acalendar 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 24. Points 003, 004, 005, 007, 008, 009, 010, 011: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on l, 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 25. 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 are representative of volatile organic compound (VOC) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 26. 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. 27. Points 008: Within one hundred and eighty days (180) after startup, 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) 28. Point 011: The owner or operator shall complete an initial extended gas analysis and submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. (Reference: Regulation No. 3, Part B, Section III.E.) Periodic Testing Requirements 29. 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 011: 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 AIRS ID: 123/9BDF Page 7 of 16 Depa enli Health and Environment Tit Pollution Control Division this permit orDolor io like- � eplacement pump shall be the same make, model and capacity as authorized in this permit. 2. Point 011: 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 011: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 30. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NOx) in ozone nonattainment areas emitting less than 100 tons of VOC or NOx per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 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). GENERAL TERMS AND CONDITIONS AIRS ID: 123/9BDF Page 8 of 16 olor Depa en P li Health and Environment it Pollution Control Division 32. This permit a tt t and e available for inspection upon request. The permit may be reissued to a new owner by the APCD as provided in AQCC Regulation No. 3, Part B, Section II.B upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 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 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. 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: AIRS ID: 123/9BDF Page 9 of 16 R: AFTP Health and Environment ollution Control Division David T D Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BDF Page 10 of 16 olor Depa en f P li Health and Environment it Pollution Control Division Notes to Permit Holder me o e an . 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.qov/cs/Satellite?c=Document C&childpaqename=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 # (lb/yr) reportable? (Ib/yr) 003 Benzene 71432 1279.2 Yes 64.0 003 n-Hexane 110543 8457.6 Yes 422.9 004 Benzene 71432 766.5 Yes 38.3 004 n-Hexane 110543 2409 Yes 120.5 005 Benzene 71432 379.0 Yes 379.0 005 n-Hexane 110543 2254.5 Yes 2254.5 005 Toluene 108883 1136.9 Yes 1136.9 005 Xylenes 1330207 1010.5 Yes 1010.5 006 Benzene 71432 107.4 No 107.4 006 n-Hexane 110543 624 Yes 624 006 Toluene 108883 257.6 Yes 257.6 006 Ethylbenzene 100414 23.6 No 23.6 006 Xylenes 1330207 217.2 No 217.2 007 Benzene 71432 34.2 No 1.7 007 n-Hexane 110543 237.9 No 11.9 007 Toluene 108883 28.9 No 1.4 AIRS ID: 123/9BDF Page 11 of 16 olor Depa en li Health and Environment it Pollution Control Dmivision 007 Ethyl.- 4 0.1 007 Xylenes 1330207 9.6 No 0.5 008 Benzene 71432 311.2 Yes 15.6 008 n-Hexane 110543 2162.5 Yes 108.1 008 Toluene 108883 262.6 Yes 13.1 008 Ethylbenzene 100414 19.6 No 1 008 Xylenes 1330207 86.8 No 4.3 009. Benzene 71432 43.8 No 2.2 009 n-Hexane 110543 262.8 No 13.2 010 Benzene 71432 43.8 No 2.2 010 n-Hexane 110543 262.8 No 13.2 011 Benzene 71432 163.6 No 8.2 011 n-Hexane 110543 1136.6 Yes 56.8 011 Toluene 108883 138 No 6.9 011 Ethylbenzene 100414 10.3 No 0.5 011 Xylenes 1330207 45.6 No 2.3 5) The emission levels contained in this permit are based on the following emission factors: I Point 003: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput VOC 1.29 0.0645 Site Specific n-Hexane 0.008 0.0004 Site Specific Benzene 0.052 0.0026 Site Specific Note: The controlled emissions factors for point 003 are based on the flare control efficiency of 95%. Point 004: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL Produced lb/BBL Source Water Throughput Condensate Throughput VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE AIRS ID: 123/9BDF Page 12 of 16 fir. " n Ya olor Depa ; en +.f cmIli 'r Health and Environment '' it Pollution Control Division Note: The co .,y= is =° _ f- r's,-12r p., +� - bas..; ,the flare control efficiency of 95%. Point 005: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.231 AP-42 Benzene 0.0023 (tpy)(wt%)/100 n-Hexane 0.0139 (tpy)(wt%)/100 Toluene 0.0070 (tpy)(wt%)/100 Xylenes 0.0062 (tpy)(wt%)/100 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) = 5.67 psia M (vapor molecular weight) = 68 lb/lb-mol T (temperature of liquid loaded) = 524 °R Point 006: Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 1384 606 467 Flanges 66 16 18 Open-ended Lines 42 6 1 Pump Seals 4 0 1 Valves 199 78 50 Other* 98 10 18 VOC Content(wt. fraction) 24.76 99.75 100 Benzene Content(wt fraction) 0.05 1.01 0.12 Toluene Content(wt. fraction) 0.04 3.04 0.03 Ethylbenzene(wt. fraction) <0.01 0.24 <0.01 Xylenes Content(wt. fraction) 0.01 2.70 <0.01 n-hexane Content(wt. fraction) 0.36 6.02 <0.01 *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 ervi S 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 AIRS ID: 123/9BDF Page 13 of 16 olor Depa en •li Health and Environment it Pollution Control Division Pump Seals 3 s .- -02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R95-017 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 007: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas(/•) NOx — 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 24.7558 14,729.5 lb/mmscf 736.5 lb/mmscf Engineering Calculation Benzene 0.0523 31.1 lb/mmscf 1.6 lb/mmscf Engineering Calculation Toluene 0.0441 26.3 lb/mmscf 1.3 lb/mmscf Engineering Calculation Ethylbenzene 0.0033 2.0 lb/mmscf 0.1 lb/mmscf Engineering Calculation Xylenes 0.0146 8.7 lb/mmscf 0.4 lb/mmscf Engineering Calculation n-hexane 0.3635 216.3 lb/mmscf 10.8 lb/mmscf Engineering Calculation Note: the gas heat content of the emergency flare gas is 1298 Btu/scf Point 008: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (%) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO -- 0.37 Ib/MMBtu 0.37 lb/MMBtu AP-42 VOC 24.7558 14,729.5 lb/mmscf 736.5 lb/mmscf Engineering Calculation Benzene 0.0523 31.1 lb/mmscf 1.6 lb/mmscf Engineering Calculation Toluene 0.0441 26.3 lb/mmscf 1.3 lb/mmscf Engineering Calculation Ethylbenzene 0.0033 2.0 lb/mmscf 0.1 lb/mmscf Engineering Calculation Xylenes 0.0146 8.7 lb/mmscf 0.4 lb/mmscf Engineering Calculation n-hexane 0.3635 216.3 lb/mmscf 10.8 lb/mmscf Engineering Calculation Note: the gas heat content of the emergency flare gas is 1298 Btu/scf Point 009: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas(%) NOx --- 0.068 lb/MMBtu 0.068 Ib/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 42.8695 33,268.5 lb/mmscf 1,663.4 lb/mmscf Engineering Calculation Benzene 0.013 10.1 lb/mmscf 0.5 lb/mmscf Engineering Calculation Toluene 0.0025 1.9 lb/mmscf 0.1 lb/mmscf Engineering Calculation AIRS ID: 123/9BDF Page 14 of 16 olor Depa en . P .li ''Health and Environment it Pollution Control Division r r . ry ,v - rt 11 I ! ma7y+ ac x't x ' 7fv�sslon -�eay�r3 Fraction of Uncontrolled Controlled Pollutant Gas (%) Source Ethylbenzene <0.0001 0.1 lb/mmscf 0.01 lb/mmscf Engineering Calculation Xylenes 0.0004 0.3 lb/mmscf 0.02 lb/mmscf Engineering Calculation n-hexane 0.0642 49.8 lb/mmscf 2.5 lb/mmscf Engineering Calculation Note: the gas heat content of the flare gas is 1,670 Btu/scf Point 010: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (°y.) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 42.8695 33,268.5 lb/mmscf 1,663.4 lb/mmscf Engineering Calculation Benzene 0.013 10.1 lb/mmscf 0.5 lb/mmscf Engineering Calculation Toluene 0.0025 1.9 lb/mmscf 0.1 lb/mmscf Engineering Calculation Ethylbenzene <0.0001 0.1 lb/mmscf 0.01 lb/mmscf Engineering Calculation Xylenes 0.0004 0.3 lb/mmscf 0.02 lb/mmscf Engineering Calculation n-hexane 0.0642 49.8 lb/mmscf 2.5 lb/mmscf Engineering Calculation Note: the gas heat content of the flare gas is 1,670 Btu/scf Point 011: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (°y.) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 24.67 14,729.5 lb/mmscf 736.5 lb/mmscf Engineering Calculation Benzene 0.05 31.2 lb/mmscf 1.6 lb/mmscf Engineering Calculation Toluene 0.04 26.3 lb/mmscf 1.3 lb/mmscf Engineering Calculation Ethylbenzene <0.01 2.0 lb/mmscf 0.1 lb/mmscf Engineering Calculation Xylenes 0.01 8.7 lb/mmscf 0.4 lb/mmscf Engineering Calculation n-hexane 0.36 216.3 lb/mmscf 10.8 lb/mmscf Engineering Calculation Note: the gas heat content of the flare gas is 1,437 Btu/scf 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's, HAPs, n-Hexane AIRS ID: 123/9BDF Page 15 of 16 r olor Depa en li Health and Environment it Pollution Control Division NANSR 'yn rc VOC's, HAPs, n-Hexane 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.zpoaccess.gov/ Part 60: Standards of Performance for New Stationary Sources NSPS 60.1-End Subpart A—Subpart KKKK NSPS Part 60,Appendixes Appendix A—Appendix I Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories MACT 63.1-63.599 Subpart A—Subpart Z MACT 63.600-63.1199 Subpart AA—Subpart DDD MACT 63.1200-63.1439 Subpart EEE—Subpart PPP MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY MACT 63.6580-63.8830 Subpart 7777-Subpart MMMMM MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX 9) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado.qov/cdphe/oilqaspermits AIRS ID: 123/9BDF Page 16 of 16 Division Information Engineer: David Thompson Control Engineer: Chris Laplante Review Date: 05/28/2014 Application Date: 02/28/2014 06/28/2014 Facility Identifiers Permit No. 14WE0494 AIRS County# 123 Weld Facility# 9C07 Facility Type: exploration and production facility ['Located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: { VOC r NOx t" CO Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: North PlatteK-22 Production Facility(COGCC#433629) Source Location: NWNE, SEC22, T5N, R63W SIC: 1311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street, Suite 1500 Address :ity,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 North PlatteK-22 Production Facility(COGCC#433629), located in the NWNE, SEC22, T5N, R63W, Weld County, Colorado, Point Name Type Control 003 Condensate Condensate Tanks Flare Tank 004 PW Tanks Water Tanks Flare 005 TL Loadout None 006 FUG Fugitives None 007 FL-1 Separator Venting Flare 008 FL-2 Separator Venting Flare 009 Sep-1 Separator Venting Flare 010 Sep-2 Separator Venting Flare 011 P-1 Pump Flare 002 Six(6)above ground 500 bbl atmospheric condensate storage tank Emissions Calculations Pollutant E.F. Source VOC 1.29 lb/bbl E&P TANK 0.0645 Benzene 0.008 lb/bbl E&P TANK 0.0004 n-Hexane 0.052 lb/bbl E&P TANK 0.0026 Requsted Throughput 162,060 bbl Control Q No Control ® Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 104.5287 tpy 5.226435 tpy Benzene 1296.48 lb/yr 64.824 lb/yr n-Hexane 8427.12 lb/yr 421.356 lb/yr Regulatory Review Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II.A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7)or more volumes of odor free air. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons (471 bbl) NSPS OOOO: for storage vessels in the natural gas production,transmission, and processing segments. This source is not subject because each tank emits less than 6 tpy VOC. Re ulation 7-Volatile Or anic Co m ounds XII. VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is not subject to the emission control requirements for condensate tanks since it is located in an attainment area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS. (Applicant is not currently subject to this since actual uncontrolled emissions are less than 20 tpy of VOC.) 003 One (1) above ground 400 bbl and two (2) 60 bbl concrete vaults used to store produced water. Emissions Calculations Pollutant E.F. Source VOC 0.262 lb/bbl CDPHE 0.0131 Benzene 0.007 lb/bbl CDPHE 0.00035 n-Hexane 0.022 lb/bbl CDPHE 0.0011 Requsted Throughput 109500 bbl Control O No Control ® Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 14.3445 tpy 0.717225 tpy Benzene 766.5 lb/yr 38.325 lb/yr n-Hexane 2409 lb/yr 120.45 lb/yr Regulatory Review Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A (July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. 004 Truck Condensate Loadout Calculations AP-42: Chapter 5.2 Equation 1 L= 12.46*S*P*M/T L= loading losses in lb per 1000 gallons loaded S=Saturation Factor P =true vapor pressure of liquid loaded [psia] M =molecular weight of vapors [lb/lb-mole] T=temperature of bulk liquid loaded [deg. R] 1 degree Fahrenheit=460.67 degree Rankine Source S 0.6 Submerged loading:ded AP-42 P 5.67 psia Sales Oil Analysis M 68 lb/lb-mole AP-42 T 524 deg. R Field Data L 5.50 lb/10^3 gal 2.31E-01 lb/bbl Annual requested Throughput 162060 BBL/yr 6806520 gal/yr Annual requested VOC emissions 37442 lb/yr 18.72 tpy Regulatory Considerations this facility is not condisdered a terminal (in Reg. 7) because average daily throughput will be below 20,000 gallons at 3,956 gallons per day. This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. NCRPs Component Mass Frac. lb/yr Emission Factor Benzene 0.010125 379.10 0.002339237 lb/bbl n-hexane 0.060241 2255.52 0.013917827 lb/bbl Touene 0.030378 1137.40 0.007018405lb/bbl Xylenes 0.026999 1010.89 0.006237735lb/bbl 0200 02€ 0 00 0 0 0 0 0 0 m e • U O 0 311 2 43 CI O C i. ry O ry CD O CO 0 0 0 0 OO O vt n O O O et ,y r O m N O� 0 0 0 0 0 0 0 0 0 Q CI a' 0 0 00 n . 0 o O m 0 O O O O O O O O O O O N N UO 6662 X _ < m m m c MI c.. N o 00 m e. O o O O e. O O ti 0 b P O O co O 0 0 0 O O N N 2 3 o ' Na c c r▪ n 4300000043431000- 0 0 a a 0 0 0 0 0 0 a N N • a 0 CI L_ W- O\ O n do O m O m N O OO 06660606606Q O O O O O 0 2 O O N N O $, m e+ O O n m ^ P n e. -a 062666 ;46 P n .2d066666646606 ; N • U a tr.; 0 2 Lc -ege - 666666 ;16 .3E: 4 46 606666 . 6066g n 3 52� E 2 u c' O a' > O pc - 26 E`a m O w n O m a N o e. coo O O o (n n o n om a n m O_ '26 O o CO O 66 O m e. n .. ° ° ° ° ° ° ° ° dOO C \E6 6666 r. a o O 00 n 0 0 0 0 0 .. 0 006060660666 F,o 0 0 00 00 O 2 J _ 2 T2-a I O 0 0 0 00 00 OLC ` o o h n6606o —ice= . 666 3 0 0 0 0 0 '9 m t o a ,, a''. O O L 0. cocoon e 0 o O o n O o 0 o n g o 0 O. o n c N O U O O O O o 0 0 0 o O O 0 O O O O O O O O O a q OO O O O d y tu W O O O O o 0 O I8 OW u E ap 0ew OF t P n m rn 6 n n e1 n n .. ti n m e. m n e. n n n ry a v i O Y h i m a w x c m 'y a j 'E w o S F- = Qa 0 a w e H ry .. P n m m m n o m a m .. CI C• b — C en a ❑ o o m o o P 3 N O O P n O Q a 066 e c- 6. LLj 0 ac W d T O 6 T LL U a O C _ _ _ _ a '2 J '' -2 co O a 0 0 0' cof, ° a i a T r a > — o 0 o O E n > E t cw ? E c cv ? E c 2 E t i OF OF Pill O OF E h O A . 0 LL 0• ` m a > o o 8 c' o > a o 3 2 a >' d o O 2 o 3 a o O p o 3 y ,3 i 3 O o 0 a O 2 a o a o ai ui m` - x 3 w z° 2 d 2 N I 0 2 05 2 Rg d8 E m c `a v p v `o 2:> o l Ea 0w m 5a a a-E oa E13 a a E 28 $▪ ' a v g a r y c • 8 a C 006 Separator controlled by a 4O flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: Sales gas routed to a candle stick flare in case of emergency Emissions from this source are: routed to a flare Natural gas venting from Sales gas routed to a candle stick flare in case of emergency.Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q`MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow rateNolume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm • Throughput(Q) 1 MMscf/yr 125.6 scf/hr 009 MMscf/mo MW 22.600 Ib/Ib-mol 0 O03 MMscf/d mole% MW Ibx/Ibmol mass fraction E Ib/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.27 44.01 0.999 0.044 CO2 0.3 2900 1.45 N2 0.63 28.013 0.176 0.008 N2 0.1 512 0.26 methane 72.2819 16.041 11.595 0.513 methane 3.8 33652 16.83 ethane 13.9364 30.063 4.190 0.185 ethane 1.4 12160 6.08 propane 6.8941 44.092 3.0397 0.135 propane 1.0 8822 4.41 isobutane 0.7208 58.118 0.4189 0.019 isobutane 0.1 1216 0.61 n-butane 1.9447 58.118 1.1302 0.050 n-butane 0.4 3280 1.64 isopentane 0.3605 72.114 0.2600 0.012 isopentane 0.1 755 0.38 n-pentane 0.4433 72.114 0.3197 0.014 n-pentane 0.1 928 O46 cyclopentane 0.0245 70.13 0.0172 0.001 cyclopentane 0.0 50 0.02 n-Hexane 0.0951 86.18 0.0820 0.004 n-Hexane 0.0 238 0.12 cyclohexane 0.0243 84.16 0.0205 0.001 cyclohexane 0.0 59 0.03 Other hexanes 0.1554 86.18 0.1339 0.006 Other hexanes 0.0 389 0.19 heptanes 0.0731 100.21 0.0733 0.003 heptanes 0.0 213 0.11 methylcyclohexane 0.0201 98.19 0.0197 0.001 methylcyclohexane 0.0 57 0.03 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 0 0.00 Benzene 0.0151 78.12 0.0118 0.001 Benzene 0.0 34 0.02 Toluene 0.0108 92.15 0.0100 0.000 Toluene 0.0 29 0.01 Ethylbenzene 0.0007 106.17 0.0007 0.000 Ethylbenzene 0.0 2 0.00 Xylenes 0.0031 106.17 0.0033 0.000 Xylenes 0.0 10 0.00 C8+Heavies 0.0341 290.666 0.0991 0.004 C8+Heavies 0.0 288 0.14 VOC mass fraction: 0.2496 Total VOC Emissions(Uncontrolled) 8.2 22.600 Notes Mole%,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Candle Stick Flare Model TBD Serial Number TBD Gas Heating Value 1298 Btu/scf Throughput 1427.8 MMBtu/yr • VRU Information Equipment Description Engine to recompress gas to sales line. Make Candle Stick Flare Model tbd Requested Control Efficiency 95.00% Annual Bypass Tme 50.00% 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 • 0.05 tpy NOX 0.26 tpy CO Emissions Summary 0.0 tpy NOX Uncontrolled/PTE 0.3 tpy CO 8.2 tpy VOC Controlled 0.4 tpy VOC • Uncontrolled Controlled Total Total(Ib/yr) Reportable? (Ib/yr) Benzene 34 No 2 Toluene 29 No 1 Ethylbenzene 2 No 0 • Xylenes 10 No 0 n-hexane 238 No 12 224-TMP 0 No 0 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 AQCC Regulation 2 [Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled NOX 88.264 b/MMscf CO 480.26 b/MMscf VOC 14881.4026 b/MMscf Benzene 31.1243 b/MMscf Toluene 26.2591 b/MMscf Ethylbenzene 1.9609 b/MMscf Xylenes 8.6841 b/MMscf n-Hexane 216.2459 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 88.264 b/MMscf _ CO 480.26 b/MMscf VOC 744.0701 b/MMscf Benzene 1.5562 b/MMscf Toluene 1.3130 b/MMscf Ethylbenzene 0.0980 b/MMscf Xylenes 0.4342 b/MMscf n-Hexane 10.8123 b/MMscf 224-TMP 0.0151 b/MMscf 007 Separator controlled by a 40'flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: gas from low pressure separator Emissions from this source are: routed to a flare Natural gas venting from gas from low pressure separator. Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=O*MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow rateNolume of gas processed MW=Molecular weight of gas=SG of gas*MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm Throughput(Q) 10 MMscf/yr 1141.6 scf/hr 0.85 MMsc1/mo I MW 22.600 Ib/Ib-mot 0.027 MMscf/d mole% MW Ibx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.27 44.01 0.999 0.044 CO2 3.0 26360 13.18 N2 0.63 28.013 0.176 0.008 N2 0.5 4657 2.33 methane 72.2819 16.041 11.595 0.513 methane 34.9 305930 152.96 ethane 13.9364 30.063 4.190 0.185 ethane 12.6 110546 55.27 propane 6.8941 44.092 3.0397 0.135 propane 9.2 80204 40.10 isobutane 0.7208 58.118 0.4189 0.019 isobutane 1.3 11053 5.53 n-butane 1.9447 58.118 1.1302 0.050 n-butane 3.4 29821 14.91 isopentane 0.3605 72.114 0.2600 0.012 isopentane 0.8 6859 3.43 n-pentane 0.4433 72.114 0.3197 0.014 n-pentane 1.0 8435 4.22 cyclopentane 0.0245 70.13 0.0172 0.001 cyclopentane 0.1 453 0.23 n-Hexane 0.0951, 86.18 0.0820 0.004 n-Hexane 0.2 2162 1.08 cyclohexane 0.0243 84.16 0.0205 0.001 cyGohexane 0.1 540 0.27 Other hexanes 0.1554 86.18 0.1339 0.006 Other hexanes 0.4 3534 1.77 heptanes 0.0731 100.21 0.0733 0.003 heptanes 0.2 1933 0.97 methylcyclohexane 0.0201 98.19 0.0197 0.001 methylcyclohexane 0.1 521 0.26 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 3 0.00 Benzene 0.0151 78.12 0.0118 0.001 Benzene 0.0 311 0.16 Toluene 0.0108 92.15 0.0100 0.000 Toluene 0.0 263 0.13 Ethylbenzene 0.0007 106.17 0.0007 0.000 Ethylbenzene 0.0 20 0.01 Xylenes 0.0031 106.17 0.0033 0.000 Xylenes 0.0 87 0.04 C8+Heavies 0.0341 290.666 0.0991 0.004 C8+Heavies 0.3 2615 1.31 VOC mass fraction: 0.2496 Total VOC Emissions(Uncontrolled) 74.4 22.600 Notes Mole%,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0010-000 Serial Number 21242,21281,21277,21243 Gas Heating Value 1697 Btu/scf Throughput 16970 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 0.58 tpy NOX 3.14 tpy CO Emissions Summary 0.6 tpy NOX Uncontrolled/PTE 3.1 tpy CO 74.4 tpy VOC • Controlled 3.7 tpy VOC • Uncontrolled Controlled Total Total(Ib/yr) Reportable? (lbtyr) Benzene 311 Yes 16 Toluene 263 Yes 13 Ethylbenzene 20 No 1 Xylenes 87 No 4 n-hexane 2162 Yes 108 224-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 I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required required? • Emission Factors for Permit jincgnlrolled NOX 115.396 b/MMscf CO 627.89 b/MMscf VOC 14881.4026 b/MMscf Benzene 31.1243 b/MMscf Toluene 26.2591 biMMscf Ethylbenzene 1.9609 b/MMscf Xylenes 8.6841 b/MMscf n-Hexane 216.2459 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 115.396 b/MMscf CO 627.89 b/MMscf VOC 744.0701 b/MMsd Benzene 1.5562 b/MMscf _ Toluene 1.3130 b/MMscf Ethylbenzene 0.0980 b/MMscf • Xylenes 0.4342 b/MMsd n-Hexane 10.8123 b/MMsd 224-TMP 0.0151 b/MMscf 009 Separator controlled by a 40'flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: recompressed Natural gas venting from a well head separator.Emissions from this source are recompressed. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q'MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas"MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mol)at 60F and 1 atm Throughput(O) 11 MMscf/yr 1267.1 scf/hr 0.94 MMscf/mo I MW 29.400 Ib/Ib-mol 0.030 MMscf/d mole/ MW Ibx/lbmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.27 44.01 0.999 0.034 CO2 3.3 29259 14.63 N2 0.63 28.013 0.176 0.006 N2 0.6 5169 2.58 methane 72.2819 16.041 11.595 0.394 methane 38.6 339582 169.79 ethane 13.9364 30.063 4.190 0.143 ethane 14.0 122706 61.35 propane 6.8941 44.092 3.0397 0.103 propane 10.2 89027 44.51 isobutane 0.7208 58.118 0.4189 0.014 isobutane 1.4 12269 6.13 n-butane 1.9447 58.118 1.1302 0.038 n-butane 3.8 33101 16.55 isopentane 0.3605 72.114 0.2600 0.009 isopentane 0.9 7614 3.81 n-pentane 0.4433 72.114 0.3197 0.011 n-pentane 1.1 9363 4.68 cyclopentane 0.0245 70.13 0.0172 0.001 cyclopentane 0.1 503 0.25 n-Hexane 0.0642 86.18 0.0553 0.002 n-Hexane 0.2 1620 0.81 cyclohexane 0.0243 64.16 0.0205 0.001 cyclohexane 0.1 599 0.30 Other hexanes 0.1554 86.18 0.1339 0.005 Other hexanes 0.4 3922 1.96 heptanes 0.0731 100.21 0.0733 0.002 heptanes 0.2 2145 1.07 methylcyclohexane 0.0201 98.19 0.0197 0.001 methylcyclohexane 0.1 578 0.29 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 3 0.00 Benzene 0.013 78.12 0.0102 0.000 Benzene 0.0 297 0.15 Toluene 0.0025 92.15 0.0023 0.000 Toluene 0.0 67 0.03 Ethylbenzene 0 106.17 0.0000 0.000 Ethylbenzene 0.0 0 0.00 Xylenes 0.0004 106.17 0.0004 0.000 Xylenes 0.0 12 0.01 C8+Heavies 0.0341 20347.934 6.9386 0.236 C8+Heavies 23.2 203216 101.61 VOC mass fraction' 0.4231 Total VOC Emissions(Uncontrolled) 182.2 • 29.400 Notes Mole%,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Tornado Model 40'Flare Stack Serial Number 12345678 Gas Heating Value 1670 Btu/scf Throughput 9268.5 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Tme 50.00% 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 0.32 tpy NOX 1.71 tpy CO Emissions Summary 0.3 tpy NOX Uncontrolled/PTE 1.7 tpy CO 185.1 tpy VOC Controlled 9.3 tpy VOC Uncontrolled Controlled Total Total(Iblyr) Reportable? (Ib/yr) Benzene 297 Yes 15 Toluene 67 No 3 Ethylbenzene 0 No 0 Xylenes 12 No 1 n-hexane 1620 Yes 81 224-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 A CC Re ulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required/Public Comment not required required? Emission Factors for Permit Uncontrolled NOX 56.78 b/MMscf CO 308.95 b/MMscf VOC 32823.3551 b/MMscf Benzene 26.7958 b/MMscf Toluene 6.0785 b/MMscf Ethylbenzene 0.0000 b/MMscf Xylenes 1.1205 b/MMscf n-Hexane 145.9830 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 56.78 b/MMscf CO 308.95 b/MMscf VOC 1641.1678 b/MMscf Benzene 1.3398 b/MMscf Toluene 0.3039 b/MMscf Ethylbenzene 0.0000 b/MMscf Xylenes 0.0560 b/MMscf n-Hexane 7.2992 b/MMscf 224-TMP 0.0151 b/MMscf 010 Separator controlled by a 40'flare stack.Flare has a minimum combustion efficiency of 95%. The flare isfis not enclosed. Equipment Description This source vents natural gas from: a well head separator Emissions from this source are: recompressed Natural gas venting from a well head separator. Emissions from this source are recompressed. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q"MW"Xx/C Ex=emissions of pollutant x Q=Volumetric flow rateNolume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/Ib-mop at 60F and 1 atm Throughput(0) 11 MMscf/yr 1267.1 scf/hr 0.94 MMscf/mo MW 29.400 Ib/Ib-mat 0.030 MMscf/c1 mole% MW Ibx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.27 44.01 0.999 0.034 CO2 3.3 29259 14.63 N2 0.63 28.013 0.176 0.006 N2 0.6 5169 2.58 methane 72.2819 16.041 11.595 0.394 methane 38.8 339582 169.79 ethane 13.9364 30.063 4.190 0.143 ethane 14.0 122706 61.35 propane 6.8941 44.092 3.0397 0.103 propane 10.2 89027 44.51 isobutane 0.7208 58.118 0.4189 0.014 isobutane 1.4 12269 6.13 n-butane 1.9447 58.118 1.1302 0.038 n-butane 3.8 33101 16.55 isopentane 0.3605 72.114 0.2600 0.009 isopentane 0.9 7614 3.81 n-pentane 0.4433 72.114 0.3197 0.011 n-pentane 1.1 9363 4.68 cyclopentane 0.0245 70.13 0.0172 0.001 cyclopentane 0.1 503 0.25 n-Hexane 0.0642 86.18 0.0553 0.002 n-Hexane 0.2 1620 0.81 cyclohexane 0.0243 84.16 0.0205 0.001 cyclohexane 0.1 599 0.30 Other hexanes 0.1554 86.18 0.1339 0.005 Other hexanes 0.4 3922 1.96 heptanes 0.0731 100.21 0.0733 0.002 heptanes 0.2 2145 1.07 methylcyclohexane 0.0201 98.19 0.0197 0.001 methylcyclohexane 0.1 578 0.29 224-TMP 0.0001 114.23 0.0001 0.000 224-TMP 0.0 3 0.00 • Benzene 0.013 78.12 0.0102 0.000 Benzene 0.0 297 0.15 Toluene 0.0025 92.15 0.0023 0.000 Toluene 0.0 67 0.03 Ethylbenzene 0 106.17 0.0000 0.000 Ethylbenzene 0.0 0 0.00 Xylenes 0.0004 106.17 0.0004 0.000 Xylenes 0.0 12 0,01 C8+Heavies 0.0341 20347 934 6.9386 0.236 C8+Heavies 23.2 203216 101.61 VOC mass fraction: 0.4231 Total VOC Emissions(Uncontrolled) 182.2 29.400 Notes Mole%,MW,and mass fractions from Critter Creek 2-03H gas analysis. Emissions are based on 8760 hours of operation per year. I calculated the average MW of O8+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 Tornado Model 40'Flare Stack Serial Number 12345678 Gas Heating Value 1670 Btu/scf Throughput 9268.5 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% • Annual Bypass Tme 50.00% 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 0.32 tpy NOX 1.71 tpy CO Emissions Summary 0.3 tpy NOX • Uncontrolled/PTE 1.7 tpy CO 182.2 tpy VOC Controlled 9.1 tpy VOC Uncontrolled Controlled Total Total(Ibyr) Reportable? (Ib/yr) Benzene 297 Yes 15 Toluene 67 No 3 Ethylbenzene 0 No 0 Xylenes 12 No 1 n-hexane 1620 Yes 81 224-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 A CC Re ulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required/Public Comment not required required? • Emission Factors for Permit Uncontrolled NOX 56.78 b/MMscf CO 308.95 b/MMscf VOC 32823.3551 b/MMscf Benzene 26.7958 b/MMscf Toluene 6.0785 b/MMscf Ethylbenzene 0.0000 b/MMscf Xylenes 1.1205 b/MMscf n-Hexane 145.9830 b/MMscf 224-TMP 0.3014 b/MMscf Controlled _ NOX 56.78 b/MMscf CO 308.95 b/MMscf VOC 1641.1678 b/MMscf Benzene 1.3398 b/MMscf Toluene 0.3039 b/MMscf Ethylbenzene 0.0000 b/MMscf Xylenes 0.0560 b/MMscf n-Hexane 7.2992 b/MMscf 224-TMP 0.0151 b/MMscf One (1) methanol injection pump, rated at 50 scf/hr, and one (1) heat trace circulation pump (make, model, and serial number: to be provided) rated at 011 600 scf/hr. Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2091535 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled ® Flare Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex= Q* MW * Xx/C Ex= emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW= Molecular weight of gas =SG of gas * MW of air Xx= mass fraction of x in gas C= molar volume of ideal gas (379 scf/lb-mol) at 601 and 1 atm Q soo scf/hr MW 22.6 Ib/Ib-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component mole % MW mass fraction Component lb/hr lb/yr tpy CO2 2.27 44 0.0442 CO2 1.581 13851.432 6.926 nitrogen 0.63 28 0.0078 nitrogen 0.279 2446.328 1.223 methane 72.2819 16.04 0.5130 methane 18.355 160786.681 80.393 ethane 13.9364 30.07 0.1854 ethane 6.634 58116.597 29.058 propane 6.8941 44.09 0.1345 propane 4.812, 42153.518 21.077 isobutane 0.7208 58.12 0.0185 isobutane 0.663, 5809.738 2.905 n-butane 1.9447 58.12 0.0500 n-butane 1.789 15674.524 7.837 isopentane 0.3605 72.15 0.0115 isopentane 0.412 3607.096 1.804 n-pentane 0.4433 72.15 0.0142 n-pentane 0.506 4435.578 2.218 cyclopentane 0.0245 72.15 0.0008 n-pentane 0.028 245.142 0.123 n-hexane 0.0951 86.18 0.0036 n-hexane 0.130 ' 1136.588 0.568 cyclohexane 0.0243 84.18 0.0009 cyclohexane 0.032 283.682 0.142 Other hexanes 0.1554 86.18 0.0059 Other hexanes 0.212 1857.264 0.929 heptanes 0.0731 100.21 0.0032 heptanes 0.116 1015.885 0.508 methylcyclohexa 0.0201 98.19 0.0009 methylcyclohe 0.031 273.703 0.137 224-TMP 0.0001 114.22 0.0000 224-TMP 0.000 1.584 0.001 Benzene 0.0151 78.11 0.0005 Benzene 0.019 163.569 0.082 Toluene 0.0108 92.14 0.0004 Toluene 0.016 138.003 0.069 Ethylbenzene 0.0007 106.17 0.0000 Ethylbenzene 0.001 10.307 0.005 Xylenes 0.0031 106.17 0.0001 Xylenes 0.005 45.644 0.023 C8+ Heavies 0.0341 288.772053 0.0044 C8+Heavies 0.156 1365.607 0.683 Mass Fraction VOC: 0.2496 Total 39.109 Heating Value I 1298 BTU/scf Combustion emission factor source: AP-42:Chapter 13.5 0.07 I lb NOX/MMBtu 0.37 I lb CO/MMBtu Notes Mole%,MW,and mass fractions from: Buffalo Ditch 1-32H facility gas analysis,dated 2/1/2008 Emissions Summary Uncontrolle tpy NOX ncontrolle d/PTE 1.3 tpy CO 39.1 tpy VOC Controlled 2.0 tpy VOC Reportable Controlled CAS* Total (lb/yr) ? Total n-hexane 110543 1136.6 Yes 57 224-TMP 540841 1.6 No 0 Benzene 71432 163.6 No 8 Toluene 108883 138.0 No 7 E-Benzene 100414 10.3 No 1 Xylenes 1330207 45.6 No 2 Uncontrolled Emission Factors Controlled Emission Factors VOC 14881.551 lb/MMscf 744.0775409 lb/MMscf Benzene 31.120 lb/MMscf 1.55601715 lb/MMscf • n-hexane 216.246 lb/MMscf 10.81229288 lb/MMscf • Toluene 26.256 lb/MMscf 1.312812665 lb/MMscf E-Benzene 1.961 lb/MMscf 0.098046174 lb/MMscf Xylenes 8,684 lb/MMscf 0.434204485 lb/MMscf 224-TMP � `0.301 lb/MMscf 0.015068602 lb/MMscf a 0 0. Y K a M W K O b 0 a O Y w Eaa e a r b s Z w J o o M xi o 0 K 5 I- z w 0O .00 e • 2 LL > Z O ¢a Z F5 < ] h m N- N e r N .- e Q 0 o m N m e 0 00 n w a IU >O - m x 0 u Z Z a O O N N N m o ° o o o o o u u , Z o -Z w b ' 0 0 z 3 3 a a . o u 0 i a ¢ c LL 0 0 a s o b a O W yaa J C 2 a Q s n'r rM ca W 0 ori.- .- ,- mm U U 0 O cc J U O O 0 0 U.WZ CC~ LL 8 O O Z > 2 O r r c.,.rroJe.r,.n _o 3 U 0 N o g mm N b 0 U 0 ' >yh J 0 f o W co co co < O >0 d % e00 Z 0000 0 ‘- .- E U Z a c u !-_F L 0 LLb m a a°3To o c u aaIZ `b c a`� rn a o U Y N co c c c c Y N F y y v y U0 s >>>> a m C w 5 o u) o m o _`o 167-i o `o To c ca yjo n cF o m m m m 'm a be T Z a u a co a= 1° n CO-b 0 in o Enc. COa E 0Zi3 o 0>JLLN w ow o < o o e V V V a 00 CO 01 a CD COMM 0 0 .E 0000000000 w w w w w w w w w ta a a?'v>'e aaeovo a 0 F m Z M O- O o r 03 03 0 0. O 000000000 a E N e Y Y O r O o O O m s m m Y Y O Y O O m O O O N 0 0 0 0 0 0 0 m .- Y CI O O r r r O O m _ i r a a N r y m 0 r 0 0 0 0 N O m Y 0 N Y O O n O m a O O N O O O O O O O m a Y r N 00 r r r O O CI O O I- F v N n 0 0 0 r m m n o m t 0 O 0 0 0 n n n r O m ,' fp lV O N(V 0 0 Y 0 0 m N m N N n n Y O m M O h O N r 0 0 0 n 0 a N N 0 N m 0 0 0 b o e n N r 0 O n N N m 0 0 Y W Y r n . 0 Oi O r N r r r H O F H O O O O w Q W 0 0 0 a O O I I o M 2 a O a o a o 2 2 ✓ i- Y e N N Y 0 Y 0 0 r 0 N Y 0 N N 5 .'220;8 r A N N Y N N m M fp Or N o• N I m N N R Ra j t F ro`�i C rr 0 N 0 m CO 0N O 0 N Or-6,i O O n 0 rr m O m ee ON ON F Y X 0 C N X r r n ore a 0 N O O NO O N N m 0 i W ood I Y O r 0 Y r n Y 0 00 O O y f m O E O N N O oi r y r N r N N H [7mm WM f Onn O O O O O O O o Q QOCOON N Y memo m O O y m 0 m Oy Cl r N n m 0 5 - m mm C e e 0 rrm 0 RRP a a O i 1 s n; as 0 0 m c 0 0 N m t O O -.; aE To aE U =LL = u c U o O O O U ELL 153 0 e m yc m ca F w g m m O2w = I i ? 5 5 E $ 6 a� E a o 2 $ b . I E 3 Z2 8 l 12 N W U y 9 9 m°iz3 (3 L3 � � 2 (.3 LLLfwciflo. o m m C O O 41 mmmmmm E mmmmmm owwwwmrn mm WWWW m m wwwwww888 0 "IL w3S8 m 33333333 3 33e Y Y Y Y Y e e e o S no 0 F 3 R p 2 c 2 OU\1 S 0 o 0 Y 0 m n m m O r 0 m m m 0 n m m o r o N 0000000o • X000000000 0000000000 o 000 AIRS (County/Plant) 123/9C07 Permit No. 14WE0494 Date 5/28/2014 Uncontrolled Emission Point# SCC Pollutant or CAS Factor 003 40400311 VOC 30.7143 lb/1000 ga 003 40400311 Benzene 0.1905 lb/1000 ga 003 40400311 n-Hexane 1.2381 lb/1000 ga 004 40400315 VOC 6.2381 lb/1000 ga 004 40400315 Benzene 0.1667 lb/1000 ga 004 40400315 n-Hexane 0.5238 lb/1000 ga 005 40600132 VOC 5.500852 lb/10^3 ga 005 40600132 Benzene 0.0557 lb/1000 ga 005 40600132 n-Hexane 0.3314 lb/1000 ga 005 40600132 Toluene 0.1671 lb/1000 ga 005 40600132 Xylenes 0.1485 lb/1000 ga 006 31000220 VOC --- --- 006 31000220 Benzene --- --- 006 31000220 n-Hexane --- --- 006 31000220 Toluene --- --- 006 31000220 Ethylbenzene --- --- 006 31000220 Xylenes --- --- 007 31000205 VOC 14881.40261 lb/MMscf 007 31000205 Nox 88.264 lb/MMscf 007 31000205 CO lb/MMscf lb/MMscf 007 31000205 Benzene 31.124327 Ib/MMscf 007 31000205 n-Hexane 216.245858 Ib/MMscf 007 31000205 Toluene 26.259103 lb/MMscf 007 31000205 Ethylbenzene 1.960923 lb/MMscf 007 31000205 Xylenes 8.68409 lb/MMscf 008 31000205 VOC 14881.40261 Ib/MMscf 008 31000205 Nox 115.396 lb/MMscf 008 31000205 CO lb/MMscf lb/MMscf 008 31000205 Benzene 31.124327 lb/MMscf 008 31000205 n-Hexane 216.245858 lb/MMscf 008 31000205 Toluene 26.259103 lb/MMscf 008 31000205 Ethylbenzene 1.960923 lb/MMscf 008 31000205 Xylenes 8.68409 lb/MMscf 009 31000205 VOC 32823.35512 lb/MMscf 009 31000205 Nox 56.78 lb/MMscf 9 31000205 CO lb/MMscf lb/MMscf 9 31000205 Benzene 26.795778 lb/MMscf 9 31000205 n-Hexane 145.983008 lb/MMscf 9 31000205 Toluene 6.078496 lb/MMscf 9 31000205 Ethylbenzene 0 lb/MMscf 9 31000205 Xylenes 1.120528 lb/MMscf 10 31000205 VOC 32823.3551 lb/MMscf 10 31000205 Nox 56.78 lb/MMscf 10 31000205 CO Ib/MMscf Ib/MMscf 10 31000205 Benzene 26.795778 lb/MMscf 10 31000205 n-Hexane 145.983008 lb/MMscf 10 31000205 Toluene 6.078496 Ib/MMscf 10 31000205 Ethylbenzene 0 Ib/MMscf 10 31000205 Xylenes 1.120528 lb/MMscf 11 31000299 VOC 14881.5508 Ib/MMscf 11 31000299 Nox 0.068 lb NOX/MA 11 31000299 CO 0.37 lb CO/MME 11 31000299 Benzene 31.120343 lb/MMscf 11 31000299 Toluene 26.256253 lb/MMscf 11 31000299 EthylBenzene 1.960923 lb/MMscf 11 31000299 Xylenes 8.68409 lb/MMscf 11 31000299 n-Hexane 216.245858 lb/MMscf Controlled Controlled Actual Requested NCRP = Emissions Emissions Ctrl. reportable Emisison Factor Source (tpy)* (tpy)* PTE (tpy)" Eff% ? E&P TANK 5.2 104.5 95% Yes E&P TANK 64.8 1296.5 95% Yes E&P TANK 421.4 8427.1 95% Yes CDPHE 0.7 14.3 95% Yes CDPHE 38.3 766.5 95% Yes CDPHE 120.4 2409 95% Yes AP-42: Chapter 5.2 18.7 18.7 0% Yes AP-42: Chapter 5.2 379.1 379.1 0% Yes AP-42: Chapter 5.2 2255.5 2255.5 0% Yes AP-42: Chapter 5.2 1137.4 1137.4 0% Yes AP-42: Chapter 5.2 1010.9 1010.9 0% Yes --- 12.1 12.1 0% Yes --- 107.4 107.4 0% No --- 624 624 0% Yes --- 257.6 257.6 0% Yes --- 23.6 23.6 0% No --- 217.2 217.2 0% No --- 0.4 8.2 95% Yes AP-42: Chapter 13.5 0 0 No AP-42: Chapter 13.5 0.3 0.3 0% No --- 1.7 34.2 95% No --- 11.9 237.9 95% No --- 1.4 28.9 95% No --- 0.1 2.2 95% No --- 0.5 9.6 95% No --- 3.7 74.4 95% Yes AP-42: Chapter 13.5 0.6 0.6 0% No AP-42: Chapter 13.5 3.1 3.1 0% Yes --- • - 15.6 311.2 95% Yes --- 108.1 2162.5 95% Yes --- 13.1 262.6 95% Yes --- 1 19.6 95% No -- 4.3 86.8 95% No --- 9.3 185.1 95% Yes AP-42: Chapter 13.5 0.3 0.3 0% No AP-42: Chapter 13.5 1.7 1.7 0 No --- 14.9 297.4 0.95 Yes --- 81 1620.4 0.95 Yes --- 3.4 67.5 0.95 No --- 0 0 No --- 0.6 12.4 0.952 No --- 9.1 182.2 0.95 Yes AP-42: Chapter 13.5 0.3 0.3 0 No AP-42: Chapter 13.5 1.7 1.7 0 No 14.9 297.4 0.95 Yes - 81 1620.4 0.95 Yes 3.4 67.5 0.95 No 0 0 No 0.6 12.4 0.952 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 2 39.1 0.949 Yes AP-42: Chapter 13.5 0.2 0.2 0 No AP-42: Chapter 13.5 1.3 1.3 0 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 8.2 163.6 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 6.9 138 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 0.5 10.3 0.951 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 2.3 45.6 0.95 No Buffalo Ditch 1-32H facility gas analysis, dated 2/ 56.8 1136.6 0.95 Yes Air Pollutant Emission Notice(APEN)—and—Application for Construction Permiy--- OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BAT/TE`YRECEIVED Current Status(Check all that apply) Reason for MEN Submittal(Check all that apply) f tB 2 8 2p 4 AIRS ID#1: 123/9C07/o 0 3 ❑ APEN update only° i ® New or previously unreported battery ❑ Modification to existing sources t? j O Previously grandfathered battery ❑ Registration for coverage under general permit no. t I O Synthetic minor facility &cancellation request for individual permit6: - ® Located in the 8-hr Ozone Control Area? ® Application for or Modification of an individual permit ❑ Registered under general permit no.GPOI ❑ Administrative permit amendment' O Permitted under individual permit: l4 WEmy94 ❑ Other. For individual permit applications,check if you wants: ®A copy of the preliminary analysis conducted by the Division ®To review a draft of the permit prior to issuance Company Name': Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address]°: 410 17th Street,Suite 1500 pyoung@BonanzaCrk.co City: Denver State: CO Zip: 80202 E-mail: m Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name°: North Platte K-22 Production Facility(COGCC#433629) Number of tanks: 6-500 bbl Location12(QQ Sec.Twp.Range.): NW/NE,Sec 22,T5N,R63W County: Weld Total tank capacity[bbl]: 3,000 Calendar year for which"Actual"data applies13: 2013 Year(s)tank(s)were placed in services: 2013 Control Description1s: Four(4)Leed L30-0010 SN:21458,21460,20326,21457 Control Efficiency's: 95% Condensate Throughput"[bbl/year] Requested's: 162,060 Maximum for PTE calculation19: 162,060 Actual2s: 135,050 While Controls Operational2' 135,050 Other equipment at facility22: Heater treaters,produced water tanks,natural gas-fired engines,pneumatic pump,flare Comments: 2-year SSEF update required Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit ❑Check if the Division is to calculate emissions. ®Check if site-specific emission factors provided to calculate emissions23. Emission Factor Battery Requested Emissions" Actual Emissions20 Pollutant24 [lb/bbl] PTE2 Uncontrolled26 Controlled2' Uncontrolled26 Controlled2' VOC[tons/year] 1.29 104.89 104.89 5.24 87.41 4.37 NOx[tons/year] 0.23 0.23 0.20 0.20 CO[tons/year] 1.26 1.26 1.06 1.06 Benzene[lbs/year] 0.008 1,279.2 1,279.2 64.0 1,066.0 53.3 n-Hexane[lbs/year] 0.052 8,457.6 8,457.6 422.9 7,048.0 352.4 Wells serviced by this tank or tank battery28 Apt#: 05-123-37732 Name: North Platte Federal P-T-22HNB ®Newly Reported Well Apt#: 05-123-37700 Name: North Platte Federa K-O-22HNB ®Newly Reported Well API#: Name: O Newly Reported Well API#: Name: O Newly Reported Well API#: Name ❑Newly Reported Well API#: Name: ❑Newly Reported Well API#: Name: O Newly Reported Well The signature below indicates that I have knowledge of the facts herein set forth and that the same are true,accurate,and complete to the best of my knowledge and belief. If this is a registration for coverage under general permit GPOI,I further certify that this source is and will be operated in full riliance with each/ioge]trjpryof general permit GPOI. Signature of Legal] Authorized Person(not a vendor or consultant) Date David J.Lillo Vice President,Rocky Mt.Asset Management Type or Print Name of Person Signing Above Official Title Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-BI (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South Q registration to: Denver,CO 80246-1530 FORM APCD-205 J Page 1 of 2 FormAPCD-205-E&PCondensateTankAPEN.docx y « O O r g = ° ; a < g y 0 T o u a . yo a. � �o om ^ z, 0 ❑ 4V V ` s � � r eno � w Ti,o o e wm;, Zow i i wagE N L h n o o c m q w U i es u Y� u- �,/q—� o o ,- y --' V u c .0 y L `�'°' 9 c C `°' y G �.�oj ?rc� I r o g a T p`0 C7 .E 'c E ° C E G e'i o °° W `"o' .. d aC m fi m °' ° a m E O °�' S •n •m m e�"n n `'C [Z o. v al M 0 Y u 0 V 0 • u 0 '0 ❑ CL' 0 c e m Q o �." s., 6 v r g "pop, �y a d c a 3 E y x = y Y .c y a ` S re C ` ° T O 6 f �' L 0 m 0 o �y 70 L �' O F "Wf y m •% o U v "o : e e e ° a N a '° 3 i9> Q 3 E Imi W re v, o C, 0 0 0 0 C € y 3 o a, v' E C. 'oO 3'a a p+ a •E Z Z. 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