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Home My WebLink About20152880.tiff CDPHE COLORADO ✓ Co el 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 11500 St PO Box 758 RECEIVED Greeley, CO 80632 August 24, 2015 AUG7 2 ` 5 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On August 26, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Noble Energy, Inc. - Shable K08-67HN, 68-1HN, 69-1HN, 69HN. 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, / ) F vi Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure Rwit, ReAmi ) 7 2015-2880 S-31_,5 -aRtz; 14t, g/�, a 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe ri John W. Hickenlooper, Governor I Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer „. x'1376*,:,, A CDPHE Air Pollution Control Division CO s Notice of a Proposed Project or Activity Warranting Public M` Comment Website Title: Noble Energy, Inc. - Shable K08-67HN, 68-1HN, 69-1HN, 69HN - Weld County Notice Period Begins: August 26, 2015 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: Noble Energy, Inc. Facility: Shable K08-67HN, 68-1HN, 69-1HN, 69HN Oil and Gas Production Facility NENE, Section 7, T4N, R66W Weld County The proposed project or activity is as follows: Applicant proposes to operate tow pressure separators and Vapor Recovery Towers (VRTs) with emissions during vapor recovery unit downtime, four (4) liquid manifold storage vessels with a total capacity of 3,228 bbl used to store produced water, eleven (11) liquid manifold storage vessels with a total capacity of 5,918 bbl used to store condensate, and loadout of condensate from the site via tanker trucks. Emissions from each of these operations will be controlled by enclosed flares. 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 15WE0341 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: Bradley Eades Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us Az,* COLORADO 1 ,, ,«.. STATE OF COLORADO •LOR D RT F P C HEALTH AND ENVIRONMENT �oF cow AIR POLLUTION CONTROL DIVISION Iy TELEPHONE: (303)692-3150 *1976 CONSTRUCTION PERMIT PERMIT NO: 1 55WE0341 Issuance 1 DATE ISSUED: ISSUED TO: Noble Energy, Inc. THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the Shable K08-67HN, 68-1HN, 69-1 HN, 69HN production facility, located in the NENE Section 7, Township 4N, Range 66W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Truck Hydrocarbon Loadout to Tanker Trucks. Emissions from the Loadout 005 loadout are controlled by an enclosed flare. Tank One (1) above ground 5,918 bbl atmospheric condensate storage Battery 006 tank. Tank consists of eleven (11) liquid manifold storage vessels. Emissions are controlled by an enclosed flare Produced One (1) above ground 2,152 bbl produced water storage tank. Water 007 Tank consists of four (4) liquid manifold storage vessels. Emissions are controlled by an enclosed fare VRT VOC Flash emissions from Vapor Recovery Towers (VRTs) during Burners 008 Vapor Recovery Unit (VRU) downtime. Emissions are controlled by an enclosed flare. LP VOC Flash emissions from Low-Pressure Separators during VRU Burners 009 downtime. Emissions are controlled by an enclosed flare 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: AIRS ID: 123/2653 Page 1 of 13 olor A Depa en . •Ii Health and Environment it Pollution Control Division REQUIREMENTS - - I TH e ` ' 'TION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). II 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 4. Point 008, 009: Within one hundred and eighty (180) days after issuance of this permit, the operator shall install and operate a flow meter to monitor and record volumetric flowrate of natural gas vented from the low-pressure separators and vapor recovery towers. The operator shall use the gas flow rate listed in the application for the actual flow rate until the flow meter is installed, not to exceed one hundred and eighty (180) days after issuance of this permit. 5. 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 6. 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 Equipment ID Point NO„ VOC CO Truck Loadout 005 --- 3.1 --- Point Tank Battery 006 1.3 17.5 3.3 Point Produced 007 1.5 --- Point Water VRT VOC 008 --- 1.2 --- Point Burners PIeaLP VOC 009 --- 6.7 1.3 Point Burners AIRS ID: 123/2653 Page 2 of 13 olor Depa en P : li Health and Environment it Pollution Control Division 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. 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 Truck 005 Enclosed Flare VOC, HAPs Loadout Tank 006 Enclosed Flare VOC, HAPs Battery Produced 007 Enclosed Flare VOC, HAPs Water VRT VOC 008 Enclosed Flare VOC, HAPs Burners LP VOC 009 Enclosed Flare VOC, HAPs Burners 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 Truck 005 Hydrocarbon Liquid Loaded 428,000 BBL/yr Loadout Tank 006 Condensate Throughput 425,000 BBL/yr Battery Produced 007 Produced Water Throughput 225,000 BBL/yr Water AIRS ID: 123/2653 Page 3 of 13 olor- Depa en • 'ii Health and Environment it Pollution Control Division Facility Equipment Point Process Parameter Annual Limit ID VRT VOC 008 Gas vented from VRTs during VRU downtime 0.7 MMSCF/yr Burners LP VOC 009 Gas vented from Low-Pressure Separators 5.8 MMSCF/yr Burners during VRU downtime 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 monitor and record throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. 9. Point 008, 009: Upon installation of a flow meter, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from all separators using the flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented to the enclosed flares from all low-pressure separators and VRTs during VRU downtime. The owner or operator shall use monthly throughput records to demonstrate compliance with the limits specified and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 10. Point 006, 007, 008, 009: The permit number and AIRS ID point number (e.g. 123/4567/008) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 11. Point 005 to 009: This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 12. 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) 13. 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 this condition. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. AIRS ID: 123/2653 Page 4 of 13 olor Depa en f P li Health and Environment it Pollution Control Division 14. Point 005: card 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. 15. Point 005: The owner or operator of a loadout to control emissions shall: a. Install and operate the vapor collection and return equipment to collect vapors during loading of tank compartments of outbound transport trucks. b. Include devices to prevent the release of vapor from vapor recovery hoses not in use. c. Use operating procedures to ensure that hydrocarbon liquid cannot be transferred unless the vapor collection equipment is in use. d. Operate all recovery and disposal equipment at a back pressure less than the pressure relief valve setting of transport vehicles. e. Inspect thief hatch seals annually for integrity and replace as necessary. Thief hatch covers shall be weighted and properly seated. f. Inspect pressure relief devices (PRD) annually for proper operation and replace as necessary. PRDs shall be set to release at a pressure that will ensure flashing, working and breathing losses are routed to the control device under normal operating conditions. g. Document annual inspections of thief hatch seals and PRD with an indication of status, a description of any problems found, and their resolution. 16. Point 006: 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. 17. Point 006, 007, 008, 009: The flare covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). If a flare or other combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XVII. The flare must be equipped with an operational auto-igniter according to the following schedule: o If installed on/after May 1, 2014, upon installation of the combustion device; o If installed before May 1, 2014, by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 18. Point 006, 007: The storage tanks covered by this permit are subject to the emission control requirements in Regulation No. 7, Section XVII.C.1.b. The owner/operator must install and operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. The source shall follow the inspection requirements of Regulation No. 7, Section XVII.C.1.d. and maintain records of the inspections for a period of two years, made available to the Division upon request. The control must be achieved according of the following schedule: AIRS ID: 123/2653 Page 5 of 13 olor. A Depa en . •Ii Health and Environment it Pollution Control Division o If stor. _ w-. - s o 1, 2• within 90 days of the date that the storage tank commences operation; o If storage tank was constructed before May 1, 2014, by May 1, 2015. 19. Point 006, 007: The storage tanks covered by this permit are subject to the venting and Storage Tank Emission Management System ("STEM") requirements of Regulation No. 7, Section XVII.C.2. This storage tank shall be operated without venting hydrocarbon emissions from the thief hatch (or other access point to the tank) or pressure relief device during normal operation, unless venting is reasonably required for maintenance, gauging, or safety of personnel and equipment. The owner/operator must develop, certify, and implement a documented STEM plan to identify, evaluate, and employ appropriate control technologies, monitoring practices, operational practices, and/or other strategies designed to meet these requirements. Compliance is required on the following schedule: o A storage tank constructed on/after must comply and implement AIMM within 90 days of the storage tank commencing operation; o A storage tank constructed before May 1, 2014, must comply by May 1, 2015. Approved instrument monitoring method inspections must begin within ninety (90) days of the Phase-In Schedule in Table 1, or within thirty (30) days for storage tanks with uncontrolled actual VOC emissions greater than 50 tons per year. Following the first approved instrument monitoring method inspection, owners or operators must continue conducting approved instrument monitoring method inspections in accordance with the Inspection Frequency in Table 1. Table 1 — Storage Tank Inspections Threshold: Storage Tank Approved Instrument Phase-In Uncontrolled Actual VOC Monitoring Method ("AIMM") Schedule Emissions (tpy) Inspection Frequency >6 and < 12 Annually January 1, 2016 > 12 and < 50 Quarterly July 1, 2015 > 50 Monthly January 1, 2015 The owner/operator shall maintain records in accordance with Regulation No. 7, Section XVII.C.3. and make them available to the Division upon request. The owner or operator shall maintain records of STEM, including the plan, any updates, and the certification, for the life of the storage tank. The owner/operator will maintain records of all required inspections and monitoring for a period of two years. AIRS ID: 123/2653 Page 6 of 13 olor Depa en P` li Health and Environment it Pollution Control Division 20. Point 008, 009: The Separators and VRTs covered by this permit are subject to Regulation 7, Section XVII.G. (State Only). On or after August 1, 2014, gas coming off a separator, produced during normal operation from any newly constructed, hydraulically fractured, or recompleted oil and gas well, must either be routed to a gas gathering line or controlled from the date of first production by air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98% for hydrocarbons. OPERATING & MAINTENANCE REQUIREMENTS 21. Point 005 to 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 II I.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 22. Point 009: The operator shall complete an initial site specific extended gas analysis within one hundred and eighty days (180) after commencement of operation or issuance of this permit, whichever comes later, of the natural gas vented from this emissions unit in order to verify the VOC content (weight fraction) of this emission stream. Results of testing shall be used to calculate site-specific emission factors for the pollutants referenced above (in units of lb/MMSCF gas vented) using Division approved methods. Results of site-specific sampling and emissions factor analysis shall be submitted to the Division as part of the self-certification and demonstrate that the emissions factor established in the permit application for this emissions point is valid. 23. Point 006, 007, 008, 009: The owner or operator shall demonstrate compliance with opacity standards, using EPA Method 22 to determine the presence or absence of visible emissions. "Visible Emissions" means observations of smoke for any period or periods of duration greater than or equal to one (1) minute in any fifteen (15) minute period during normal operation. (Reference: Regulation No. 7, Section XVII.A.II) ADDITIONAL REQUIREMENTS 24. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: For any criteria pollutant: For sources emitting less than 100 tons per year, a change in actual emissions of five (5) tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO,) in ozone nonattainment areas emitting less than 100 tons of VOC or NO, per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or AIRS ID: 123/2653 Page 7 of 13 olor. A Depa en . - 'ii Health and Environment IL A it Pollution Control Division For so itt 06 ' - pe mor- _ ange 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. 25. 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 26. 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. 27. 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. 28. 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. 29. 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. AIRS ID: 123/2653 Page 8 of 13 olor Depa r enz f P li Health and Environment it Pollution Control Division 30. Each and ev io hi it i ial pa eof 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. 31. 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. 32. 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: Bradley Eades Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Noble Energy, Inc. AIRS ID: 123/2653 Page 9 of 13 Is olor. � Depa en . - •li `Health and Environment it Pollution Control Division Notes to Permit Holder me o •e, a -. 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&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# (Ib/yr) reportable? (Ib/yr) Benzene 71432 361 Yes 18 n-Hexane 110543 2339 Yes 117 005 Toluene 108883 643 Yes 32 Ethylbenzene 100414 16 No 1 Xylenes 1330207 188 No 9 Benzene 71432 2040 Yes 102 n-Hexane 110543 13260 Yes 663 006 Toluene 108883 3613 Yes 181 2,2,4-TMP 540841 213 No 11 Xylenes 1330207 1020 Yes 51 Benzene 71432 1575 Yes 79 007 n-Hexane 110543 4950 Yes 248 Benzene 71432 126 No 6 n-Hexane 110543 818 Yes 41 008 Toluene 108883 223 Yes 11 Ethylbenzene 100414 7 No 0 AIRS ID: 123/2653 Page 10 of 13 olor v Depa en f P li Health and Environment ir Pollution Control Division Xyl 0 3 Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# Ib/ r re ortable? Ib/ r Benzene 71432 830 Yes 42 n-Hexane 110543 5441 Yes 272 009 Toluene 108883 1617 Yes 81 Ethylbenzene 100414 58 No 3 Xylenes 1330207 519 Yes 26 5) The emission levels contained in this permit are based on the following emission factors: Point 005: Emission Factors - Uncontrolled Pollutant Ib/BBL loaded Source VOC 0.2897 Benzene 0.0008 n-Hexane 0.0055 AP-42 Toluene 0.0015 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) = 7.88 psia M (vapor molecular weight) = 60 Ib/Ib-mol T(temperature of liquid loaded) =512.45 °R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the pressurized liquid sample by the VOC emission factor. Controlled emissions are based on the combustor control efficiency of 95%. Point 006: Emission Factors Uncontrolled Pollutant Ib/BBL Source Condensate Throu h ut VOC 1.6475 n-Hexane 0.0312 Benzene 0.0048 HYSYS/AP-42 Toluene 0.0085 X lenes 0.0024 AIRS ID: 123/2653 Page 11 of 13 olor Depa en li Health and Environment ir Pollution Control Division Note: The co is ' fo int n the control efficiency of 95%. Point 007: Emission Factors Pollutant Uncontrolled Source Ib/BBL Produced � Water Throu h ut VOC 0.262 n-Hexane 0.022 CDPHE Benzene 0.007 Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 008: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled Ib/MMscf Ib/MMscf NOx --- 272•$2 272.82 CDPHE CO --- 693.12 693.12 VOC 69.59 73736.93 3686.80 Benzene 0.19 205.48 10.27 Aspen HYSYS V8.6 Toluene 0.34 363.43 18.17 n-Hexane 1.26 1335.12 66.76 Note: The uncontrolled VOC and HAP emissions were calculated based on a HYSYS model to estimate the VOC and HAP content of the stream and stream flow assuming 438 hr/yr VRU downtime. The controlled emissions for this point are based on the flare control efficiency of 95%. Point 009: Weight Emission Emission Pollutant Fraction of Factors Factors Source Gas(%) Uncontrolled Controlled Ib/MMscf Ib/MMscf NOx --- 169.28 169.28 CDPHE CO --- 430.05 430.05 VOC 53.79 45750.13 2287.51 Benzene 0.17 144.37 7.22 Toluene 0.33 281.02 14.05 Aspen HYSYS V8.6 X lenes 0.11 90.23 4.51 n-hexane 1.11 946.08 47.30 Note: The uncontrolled VOC and HAP emissions were calculated based on a HYSYS model to estimate the VOC and HAP content of the stream and stream flow assuming 438 hr/yr VRU downtime. The controlled emissions for this point are based on the flare control efficiency of 95%. 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice(APEN)associated with this permit is valid for a term of five years from the date it was received by the Division.A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. AIRS ID: 123/2653 Page 12 of 13 olor Depa en P li Health and Environment ir Pollution Control Division 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC, n-Hexane NANSR Synthetic Minor Source of: VOC 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.q poaccess.qov/ 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 XXXXXX 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.qov/pacific/cdphe/air-qermit-self-certification AIRS ID: 123/2653 Page 13 of 13 Division Information Engineer: Bradley Eades ' Control Engineer: Christopher Laplante Review Date: 04/28/2015 Application Date: 01/30/2015 Facility Identifiers Permit No. 15WE0341 Potentially located in ozone nonattainment area AIRs County# 123 Weld Facility# 2653 Facility Type: exploration and production facility O Located in the 8-hour non-attainment area? �True Minor � SyntheticMinorfor: �VOC � NOx �'v" CO Administrative Information Company Name: Noble Energy, Inc. Source Name: Shable K08-67HN, 68-1 HN, 69-1 HN, 69HN Source Location: NENE Section 7, Township 4N, Range 66W SIC: 1311 Address 1: Noble Energy, Inc. M2iling Address 2: 1625 Broadway,Suite 2200 Address ty,State Zip: Denver, CO, 80202 Name: ischaffner@nobleener�yinc.com Person To Phone: 720-587-2326 Contact Fax: 303-228-4280 Email: jschaffner@nobleener�yinc.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Shable K08-67HN,68-1 HN,69-1 HN,69HN , located in the NENE Section 7,Township 4N, Range 66W,Weld County,Colorado. Point Name T e Control Action Truck Newly 005 Loadout Loadout Flare reported source Newly 006 Tank Battery Condensate Tanks Flare reported source Produced Newly 007 Water Water Tanks Flare reported source VRT VOC Newly 008 Burners Separator Venting Flare reported source LP VOC Newly 009 gurners Separator Venting Flare reported source 005 Hydrocarbon Loadoutto TankerTrucks Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2, Equation 1) L=loading losses in Ib per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 7.88 psia AP-42 calculation M Molecular Weight of 60 Ib/Ib-mole AP-42 calculation T Liquid Temperature 512.45 deg. R Field Data L 6.90 Ib/10^3 gal 2.90E-01 I b/bb I Annual requested Throughput 428,000 BBL/yr 17976000 gal/yr Annual requested VOC emissions 1z3990 Ib/yr 62.00 tpy Control: Flare Efficiency: 95.00% NCRPs Component Mass Fraction Benzene 0.0029 n-hexane 0.0189 Toluene 0.0052 Ethylbenzene 0.0001 Xylenes 0.0015 Source: Flash stream composition from Hysys with 79%VOC Emissions Summary Table Pollutant Emission Factor Uncontrolled Emission Controlled Emissions Source VOC 0.2897 Ib/bbl 62.00 tpy 3.10 tpy AP-42 Benzene 0.00081b/bbl 361.0Ib/yr 18.0Ib/yr Calc n-Hexane 0.00551b/bbl 23391b/yr 1171b/yr Calc Toluene 0.00151b/bbl 6431b/yr 321b/yr Calc Ethylbenzene 0.00004 1b/bbl 16 1b/yr l ib/yr Calc Xylenes 0.00041b/bbl 1881b/yr 91b/yr Calc Regulatory Review �Requfation 3-APEN and Perm[ttinq Repuirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes, review the following two exemptions for applicability: Dces the operator unload less than 10,000 gallons(238 BBLs)per day aT crude oil on an annual average basis7 NO If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 Does this operator unload less than 6,750 bbls per year of condensate via splash fill or 16,308 bbls per year of condensate via submerged fill procedure? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section II.D.1.1 006 One(1)above ground 5,918 bbl condensate storage tank.Tank consists of 11 liquid manifold storage vessels. Emissions are routed to an enclosed flare Requsted Throughput 425000 bbl Control Flare Combustion emission fa CDPHE Inter-Office Communic Efficiency 95.00% 0.0037 Ib NOX/Ib 0.0094 Ib CO/IbVOC Emissions Summary Table Pollutant Emission Factor Uncontroiled Emissions Controlled Emissions Source VOC 1.6475 Ib/bbl 350.1 tpy 17.50 tpy Benzene 0.0048 Ib/bbl 2040 Ib/yr 102 Ib/yr Toluene 0.00851b/bbl 3612.51b/yr 180.6251b/yr HYSYS/AP-42 Xylenes 0.00241b/bbl 10201b/yr 51 Ib/yr n-Hexane 0.03121b/bbl 132601b/yr 6631b/yr 2,2,4-TMP 0.0005 Ib/bbl 212.5 Ib/yr 10.625 Ib/yr NOx 0.0061 Ib/bbl 1.29534688 tpy 0.064767 tpy CDPHE - CO 0.0155 Ib/bbl 3.29088125 tpy 0.164544 tpy 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. Requlation 6-New Source Performance'Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. The source is not subject because the tanks are all prior to custody transfer and have a capacity less than 10,000 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. Regulation 7=Volatile Orqanic'Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is subject to the emission control requirements for condensate fanks since it is located in a non- attainment area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is currently subject to this since actual uncontrolled emissions are greater than 20 tpy of VOC.) Miscellaneous Notes J.Schaffner confirmed that all flares at this site are enclosed.Updated Hysys calculations were submitted on 05/22/2015.Emission factors changed and throughput was modified. 007 One(1)above ground 2152 bbl Produced Water storage tank. Tank consists of four (4) liquid manifold storage vessels. Emissions are routed to an enclosed fare Emissions Calculations Requsted Throughput 225000 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 29.475 tpy 1.47375 tpy CDPHE Benzene 0.007 lb/bbl 1575 lb/yr 78.75 lb/yr CDPHE n-Hexane 0.022 lb/bbl 4950 lb/yr 247.5 lb/yr CDPHE 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. Two(2)Vapor Recovery Towers(VRT)controlled by one enclosed flare during VRU downtime.Flare has a 005 minimum control efficiency of 95%. 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. Note:During normal operation,gas captured from VRT is routed to vapor recovery units(VRU)and recompressed into the sales line.During periods of VRU downtime,emissions are routed to an enclosed flare. This permit addresses emissions during VRU downtime.Requested gas volume is based on HYSYS modeled vent rates and assumed downtime of 438 hr/yr(5%). 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 scf/lb-mol)gasat 60F and 1 atm (379 Throughput(Q) 0.6133 MMscf/yr 70.01141553 scf/hr MW 40.16 lb/lb-mol 0.001680274 MMscf/d mass fraction lb/hr lb/yr tpy CO2 0.027 0.20 1780.63 0.89 N2 0.001 0.00 32.49 0.02 methane 0.071 0.52 4588.06 2.29 ethane 0.206 1.53 13400.25 6.70 propane 0.307 2.28 19944.96 9.97 isobutane 0.077 0.57 5029.97 2.51 n-butane 0.164 1.22 10664.31 5.33 isopentane 0.051 0.38 3294.82 1.65 n-pentane 0.047 0.35 3073.87 1.54 3-Mpentane 0.017 0.12 1091.78 0.55 n-Heptane 0.010 0.07 617.37 0.31 n-Octane 0.003 0.02 175.46 0.09 n-Nonane 0.000 0.00 25.99 0.01 n-Decane 0.001 0.00 32.49 0.02 Benzene 0.002 0.01 126.02 0.06 Toluene 0.003 0.03 222.89 0.11 E-Benzene 0.000 0.00 7.25 0.00 Xylenes 0.001 0.01 63.73 0.03 n-Hexane 0.013 0.09 818.83 0.41 224-TMP 0.001 0.00 32.49 0.02 VOC mass fraction: 0.6959 Total VOC(Uncontrolled) 22.61 45222.24 Notes MW and mass fractions from Hysys Version 8.6 results submitted with application.Model was carried out using pressurized liquid samples collected from 4 wells at the Shable K08 Facility.("Material Stream:Vapors to VRTVRU/Comb.") Emissions are based on 8760 hours of operation per year. 15WE0341.CP1.xlsm Two(2)Vapor Recovery Towers(VRT)controlled by one enclosed flare during VRU downtime.Flare has a 005 minimum control efficiency of 95%. Flaring Information Equipment Description Enclosed Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Cimarron Model TBD Serial Number TBD Gas Heating Value 2229.17 Btu/scf Throughput 1367.149961 MMBtu/yr Overall Control 95.00% Combustion emission factor source: CDPHE Inter-Office Communication 0.0037 I lb NOX/IbVOC 0.0094 I lb CO/IbVOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 73734.00 lb/MMscf 3686.70 lb/MMscf 22.611 tpy 1.13 tpy Aspen HYSYS V8. Nox 272.82 lb/MMscf 272.82 lb/MMscf 0.084 tpy 0.08 tpy CDPHE CO 693.10 lb/MMscf 693.10 lb/MMscf 0.213 tpy 0.21 tpy CDPHE Benzene 205.48 lb/MMscf 10.27 lb/MMscf 126.02 lb/yr 6.30 lb/yr Aspen HYSYS V8. n-Hexane 1335.12 lb/MMscf 66.7562 lb/MMscf 818.83 lb/yr 40.94 lb/yr Aspen HYSYS V8. Toluene 363.43 lb/MMscf 18.1714 lb/MMscf 222.89 lb/yr 11.14 lb/yr Aspen HYSYS V8. Xylenes 103.913 lb/MMscf 5.1957 lb/MMscf 63.73 lb/yr 3.19 lb/yr Aspen HYSYS V8. Ethylbenzene 11.821 lb/MMscf 0.5911 lb/MMscf 7.25 lb/yr 0.36 lb/yr Aspen HYSYS V8. 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 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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes *November 2014 was date of first production indicated on APEN for point 006(Condensate Tanks). This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 Miscellaneous Notes Met with Jackie Schaffner on 06/16/2015 regarding the structure of this permit and site-design considerations.After continued discussion with Noble following the meeting a flow meter was installed on the LP Separator line to the combustors.Noble will also install flow meter on the VRT vapor line to combustors within 180 days of issuance of this permit. After discussion with J.Schaffner,combustion emission factors for NOx and CO used are derived from CDPHE inter-office communication Re:Condensate Flare Emission Factors.Although the emissions factors were derived for use with storage tanks,their use is approved here since the gas routed to the ECDs is produced from low pressure flash. Emission estimates in this analysis are based on 438 hrs/yr emissions are routed to combustors. Per J.Schaffner,vendors are contractually obligated to provide at least 95%uptime for the VRU units so 5%downtime is a conservative estimate. Per J.Schaffner,the pressurized liquid samples were taken at the HP separator at conditions of HP separator.The liquid stream continues to the LP separator @ 30psig 90F and subsequently to the VRT @ 4psig ambient T.Emissions of gas evolved at each step(LP and VRT)are modeled using Hysys with input compositions based on pressurized liquid composition prior to the LP separator. After discusion with Noble,it was determined that the facility will use the modeled VRT vent rate(from the application)with an assumed 5%"VRU downtime" to the combustors as the actual vent rate until the flow meter is installed.This is not to exceed 180 days. 15WE0341.CP1.xlsm Four(4)low-pressure separators controlled by an enclosed flare during VRU downtime.Flare has a 006 minimum control efficiency of 95%. 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. Note:Under normal operation emissions from this source are routed to VRUs and recompressed into the sales line.During period of VRU downtime,emissions are routed to enclosed combustors.This permit addresses emissions during VRU downtime.Requested gas volume is based on HYSYS modeled vent rates and assumed downtime of 438 hr/yr(5%). 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(Q) 5.751 MMscf/yr 656.5068493 scf/hr MW 32.21 Ib/Ib-mol 0.015756164 MMscf/d mass fraction lb/hr lb/yr tpy CO2 0.040 2.24 19648.12 9.82 N2 0.004 0.22 1955.04 0.98 methane 0.210 11.72 102679.71 51.34 ethane 0.208 11.60 101613.02 50.81 propane 0.234 13.06 114427.53 57.21 isobutane 0.057 3.20 28054.77 14.03 n-butane 0.123 6.88 60256.41 30.13 isopentane 0.040 2.22 19452.61 9.73 n-pentane 0.038 2.13 18670.60 9.34 3-Mpentane 0.015 0.81 7087.01 3.54 n-Heptane 0.009 0.51 4496.58 2.25 n-Octane 0.003 0.16 1368.53 0.68 n-Nonane 0.001 0.03 244.38 0.12 n-Decane 0.001 0.04 342.13 0.17 Benzene 0.002 0.09 830.28 0.42 Toluene 0.003 0.18 1616.15 0.81 E-Benzene 0.000 0.01 57.78 0.03 Xylenes 0.001 0.06 518.93 0.26 n-Hexane 0.011 0.62 5440.93 2.72 224-TMP 0.001 0.03 244.38 0.12 VOC mass fraction: 0.538 Total VOC(Uncontrolled) 131.55 Notes MW and mass fractions from Hysys Version 8.6 results submitted with application.Model was carried out using pressurized liquid samples collected from 4 wells at the Shable K08 facilty.("Material Stream:Vapor to VRU/Comb") Emissions are based on 8760 hours of operation per year. 15WE0341.CP1.xlsm Four(4)low-pressure separators controlled by an enclosed flare during VRU downtime.Flare has a 006 minimum control efficiency of 95%. Flaring Information Equipment Description Enclosed Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Cimarron Model TBD Serial Number TBD Gas Heating Value 1786.99 Btu/scf Throughput 10276.97949 MMBtu/yr Overall Control 95.00% Combustion emission factor source: CDPHE Inter-Office Communication 0.0037 alb NOX/IbVOC 0.0094 Ilb CO/IbVOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 45752.00 lb/MMscf 2287.60 lb/MMscf 131.56 tpy 6.58 tpy Aspen HYSYS V8. Nox 169.28 lb/MMscf 169.28 lb/MMscf 0.49 tpy 0.49 tpy CDPHE CO 430.07 lb/MMscf 430.07 Ib/MMscf 1.24 tpy 1.24 tpy CDPHE Benzene 144.37 lb/MMscf 7.22 lb/MMscf 830.28 lb/yr 41.51 lb/yr Aspen HYSYS V8. n-Hexane 946.08 lb/MMscf 47.3042 lb/MMscf 5440.93 lb/yr 272.05 lb/yr Aspen HYSYS V8. Toluene 281.02 lb/MMscf 14.0510 lb/MMscf 1616.15 lb/yr 80.81 lb/yr Aspen HYSYS V8. Xylenes 90.23 lb/MMscf 4.5117 lb/MMscf 518.93 lb/yr 25.95 lb/yr Aspen HYSYS V8. Ethylbenzene 10.05 lb/MMscf 0.5023 lb/MMscf 57.78 lb/yr 2.89 lb/yr Aspen HYSYS V8. 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 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." AQCC Regulation 7 Was the well newly constructed,hydraulically fractured,or recompleted on or after August 1,2014? yes *November 2014 was date of first production indicated on APEN for point 006(Condensate Tanks). This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 Miscellaneous Notes Met with Jackie Schaffner on 06/16/2015 regarding the structure of this permit and site-design considerations.After continued discussion with Noble following the meeting a flow meter was installed on the LP Separator line to the combustors.Noble will also install flow meter on the VRT vapor line to combustors within 180 days of issuance of this permit.Until the flow meter is installed,the gas flow rate used in the applicaiton(assuming 438 hr/yr VRU downtime)shall be used. After discussion with J.Schaffner,combustion emission factors for NOx and CO used are derived from CDPHE inter-office communication Re:Condensate Flare Emission Factors.Although the emissions factors were derived for use with storage tanks,their use is approved here since the gas routed to the ECDs is produced from low pressure flash. Per J.Schaffner,vendors are contractually obligated to provide at least 95%uptime for the VRU units so 5%downtime is a conservative estimate. Per J.Schaffner,the pressurized liquid samples were taken at the HP separator at conditions of HP separator.The liquid stream continues to the LP separator @ 30psig 90F and subsequently to the VRT @ 4psig ambient T.Emissions of gas evolved at each step(LP and VRT)are modeled using Hysys with input compositions based on pressurized liquid composition prior to the LP separator.An initial testing requirment to confirm VOC content of this emissions stream is required in the permit. 15WE0341.CP1.xlsm AIRS(County/Plant) 123/2653 Permit No. 15WE0341 Date 4/28/2015 Controlled Controlled Actual Requested NCRP= Uncontrolled Emission Emisison Emissions Emissions PTE Ctrl. reportable Point# SCC Pollutant or CAS Factor Factor Source (tpy)* (tpy)* (tpy)* Eff% ? 005 40600132 VOC 6.898 lb/1000 ga AP-42 3.1 62.0 95% Yes 005 40600132 Benzene 0.020 lb/1000 ga Calc 18.0 361.0 95% Yes 005 40600132 n-Hexane _ 0.130 lb/1000 ga Calc 116.9 2338.6 95% Yes 005 40600132 Toluene 0.036 lb/1000 ga Calc 32.2 643.5 95% Yes 005 40600132 Ethylbenzene 0.001 lb/1000 ga Calc 0.8 15.7 95% No 005 40600132 Xylenes 0.011 lb/1000 ga Calc 9.4 188.3 95% No 006 40400311 VOC 39.226 lb/1000 ga HYSYS/AP-42 17.5 350.1 95% Yes 006 40400311 NOx 0.145 lb/1000 ga CDPHE 0.1 1.3 92% Yes 006 40400311 CO 0.369 lb/1000 ga 0.2 3.3 94% Yes 006 40400311 Benzene 0.115 lb/1000 ga 102.0 2040.0 95% Yes 006 40400311 n-Hexane 0.743 lb/1000 ga 663.0 13260.0 95% Yes 006 40400311 Toluene 0.203 lb/1000 ga 180.6 3612.5 95% Yes 006 40400311 Xylenes 0.057 lb/1000 ga 51.0 1020.0 95% Yes 007 40400315 VOC 6.238 lb/1000 ga CDPHE 1.5 29.5 95% Yes 007 40400315 Benzene 0.167 lb/1000 ga CDPHE 78.8 1575.0 95% Yes 007 40400315 n-Hexane 0.524 lb/1000 ga CDPHE 247.5 4950.0 95% Yes Aspen HYSYS 008 31000205 VOC 73734.000lb/MMscf V8.6 1.1 22.6 95% Yes 008 31000205 NOx 272.816 lb/MMscf CDPHE 0.1 0.1 0% No 008 31000205 CO 693.100 lb/MMscf CDPHE 0.2 0.2 0% No Aspen HYSYS 008 31000205 Benzene 205.479 lb/MMscf V8.6 6.3 126.0 95% No Aspen HYSYS 008 31000205 n-Hexane 1335.125 lb/MMscf V8.6 40.9 818.8 95% Yes Aspen HYSYS 008 31000205 Toluene 363.427 lb/MMscf V8.6 11.1 222.9 95% No Aspen HYSYS 008 31000205 Ethylbenzene 11.821 lb/MMscf V8.6 0.4 7.3 95% No Aspen HYSYS 008 31000205 Xylenes 103.913 lb/MMscf V8.6 3.2 63.7 95% No Aspen HYSYS 009 31000205 VOC 45750.130Ib/MMscf V8.6 6.6 131.6 95% Yes 009 31000205 NOx 169.275 Ib/MMscf CDPHE 0.5 0.5 0% No 009 31000205 CO 430.051 Ib/MMscf CDPHE 1.2 1.2 0% Yes Aspen HYSYS 009 31000205 Benzene 144.371 lb/MMscf V8.6 41.5 830.3 95% Yes Aspen HYSYS 009 31000205 n-Hexane 946.084 Ib/MMscf V8.6 272.0 5440.9 95% Yes Aspen HYSYS 009 31000205 Toluene 281.021 Ib/MMscf V8.6 80.8 1616.2 95% Yes Aspen HYSYS 009 31000205 Ethylbenzene 10.047 Ib/MMscf V8.6 2.9 57.8 95% No Aspen HYSYS 009 31000205 Xylenes 90.233Ib/MMscf V8.6 25.9 518.9 95% Yes L , ,- O �O O o 0 4, aa) Z Z Z L G o ° E o vN i C ++ 4, O OO ,!1 3 J, L L co c L G. 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