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Home My WebLink About20153561.tiff A CDPH6 COLORADO da Co Department of Public I Health Fr Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 1150 O St PO Box 758 RECEIVED Greeley, co 80632 OCT 3 0 1015 October 26, 2015 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On October 28, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Noble Energy, Inc. - Burton K25-67-1HN, 68-1HNL, 69-1HNL. 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 Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure �� /% 2015-3561 )/ i 020/. CG �- 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickenlooper, Governor Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer CDPHE Air Pollution Control Division co " Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Noble Energy, Inc. - Burton K25-67-1HN, 68-1HNL, 69-1HNL - Weld County Notice Period Begins: October 28, 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: Burton K25-67-1HN, 68-1HNL, 69-1HNL Exploration and Production Site SWNW Sec 25 T4 R66W Weld County The proposed project or activity is as follows: New oil and gas exploration and production site. Facility aahigh pressure (HP) separator, lowpressure (LP) separator, vapor recovery tower (VRT), g P � P � P { ), condensate tanks, produced water tanks, and truck loadout. Gas from HP separator is routed to sates line, gas from LP separator and VRT is routed to vapor recovery unit (VRU) and compressed to sales line with compressor engines, or routed to enclosed flares. All tanks and loadout emissions are controlled by enclosed combustors. 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): • 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 15WE0704 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: Betsy Gillard Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us cttu u 1 71 k STATE OF COLORADO COLOR D PARTIEN F P C HEALTH AND ENVIRONMENT s AIR POLLUTION CONTROL DIVISION TELEPHONE: (303) 692-3150 ' '"` • '_1876 CONSTRUCTION PERMIT PERMIT NO: 15WE0704 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 Burton K25-67-1HN, 68- 1 HNL, 69-1 HNL, located in the SWNW Sec 25 TWP4 R66W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Tank Nine (9) above ground 538 bbl atmospheric condensate storage Battery 002 tanks Produced 003 Three (3) above ground 500 bbl produced water storage tanks Water Truck 004 Hydrocarbon Loadout to Tanker Trucks Loadout VRU & Bank of two (2) enclosed flares to control vapors from LP separator VRT VOC 005 and VRT Burners THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after commencement of operation or issuance of this permit, whichever comes later, 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 commencement of operation or issuance of this permit, whichever comes later, compliance with the conditions contained in this AIRS ID: 123/8488 Page 1 of 15 olor-w Depa en . P .li Health and Environment it Pollution Control Division permit shall « tr-_=, o _ "' isi.. _ own-.I operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 4. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 5. Point 005: The following information shall be provided to the Division within fifteen (15) days after issuance of permit. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 6. Point 005: Within one hundred and eighty (180) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from the low pressure separator and vapor recovery tower. 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. 7. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 8. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO VOC CO Emission Type X Tank Battery 002 0.7 9.6 1.8 Point Produced 003 0.1 1.3 0.2 Point Water AIRS ID: 123/8488 Page 2 of 15 3 a.... olora Depa end P •li Health and Environment it Pollution Control Division Truck Loado f' 04 ftwis 1.5 Point VRU &VRT 005 0.6 7.3 1.4 Point VOC Burners 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 an nual limits shall be determined by recording the facility's an nual p Y criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 9. 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 Tank 002 Enclosed Flare(s) VOC Battery Produced 003 Enclosed Flare(s) VOC Water Truck 004 Enclosed Flare(s) VOC Loadout VRU &VRT VOC 005 Enclosed Flare(s) VOC Burners PROCESS LIMITATIONS AND RECORDS 10. 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 Tank 002 Condensate Throughput 350,000 BBL Battery AIRS ID: 123/8488 Page 3 of 15 Ill olor. Depa en . P''".Ii Health and Environment A it Pollution Control Division Produced ., r'.•_. W hput 200,000 BBL Water Truck 004 Oil Loaded 350,000 BBL Loadout VRU& VRT VOC 005 Gas Vented from LP Separator/VRT 5.29 MMSCF Burners 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. 11. Point 005: Upon installation of a flow meter, the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from the low-pressure separator and VRT using a 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. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 13. 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.2.b shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 4.) 14. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 15. Point 002: 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. 16. Point 002: 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 002: The condensate storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: XVII.C.1.a. Beginning May 1, 2008, owners or operators of all atmospheric condensate storage tanks with uncontrolled actual emissions of volatile organic compounds equal to or greater than 20 tons per year based on a rolling twelve-month total AIRS ID: 123/8488 Page 4 of 15 ToloraiDep1en, PxPJc Health and Environment Air Pollution Control Division shall o ntro • ent to has an average control efficiency of at least 95% for VOCs on such tanks. 18. Point 002 and 003: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must 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. XVII.C.1.b.(i)(a) Control requirements of Section XVII.C.1.b. must be achieved within ninety (90) days of the date that the storage tank commences operation. XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section XVII.C.1.b.(i), whichever comes later, owners or operators of storage tanks subject to Section XVII.C.1. must conduct audio, visual, olfactory ("AVO") and additional visual inspections of the storage tank and any associated equipment (e.g. separator, air pollution control equipment, or other pressure reducing equipment) at the same frequency as liquids are loaded out from the storage tank. These inspections are not required more frequently than every seven (7) days but must be conducted at least every thirty one (31) days. Monitoring is not required for storage tanks or associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i) Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; XVII.C.1.d.(ii) Visual inspection or monitoring of the air pollution control equipment to ensure that it is operating, including that the pilot light is lit on combustion devices used as air pollution control equipment; XVII.C.1.d.(iii) If a combustion device is used, visual inspection of the auto-igniter and valves for piping of gas to the pilot light to ensure they are functioning properly; XVII.C.1.d.(iv) Visual inspection of the air pollution control equipment to ensure that the valves for the piping from the storage tank to the air pollution control equipment are open; and XVII.C.1.d.(v) If a combustion device is used, inspection of the device for the presence or absence of smoke. If smoke is observed, either the equipment must be immediately shut-in to investigate the potential cause for smoke and perform repairs, as necessary, or EPA Method 22 must be conducted to determine whether visible emissions are present for a period of at least one (1) minute in fifteen (15) minutes. XVII.C.1.e. If storage tanks or associated equipment is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor such equipment until it becomes feasible to do so. AIRS ID: 123/8488 Page 5 of 15 �z olor. - Depa en P°'.h `Health and Environment it Pollution Control Division XVII.C.2. Ca. d ,•: •"t• -q for ge tanks that are fitted with air pollution control equipment as required by Sections XII.D. or XVII.C.1. XVII.C.2.a. Owners or operators of storage tanks must route all hydrocarbon emissions to air pollution control equipment, and must operate 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. Compliance must be achieved in accordance with the schedule in Section XVII.C.2.b.(ii). XVII.C.2.b. Owners or operators of storage tanks subject to the control requirements of Sections XII.D.2., XVII.C.1.a, or XVII.C.1.b. must develop, certify, and implement a documented Storage Tank Emission Management System ("STEM") plan to identify, evaluate, and employ appropriate control technologies, monitoring practices, operational practices, and/or other strategies designed to meet the requirements set forth in Section XVII.C.2.a. Owners or operators must update the STEM plan as necessary to achieve or maintain compliance. Owners or operators are not required to develop and implement STEM for storage tanks containing only stabilized liquids. The minimum elements of STEM are listed below. XVII.C.2.b.(i) STEM must include selected control technologies, monitoring practices, operational practices, and/or other strategies; procedures for evaluating ongoing storage tank emission capture performance; and monitoring in accordance with approved instrument monitoring methods following the applicable schedule in Section XVII.C.2.b.(ii) and Inspection Frequency in Table 1. XVII.C.2.b.(ii) Owners or operators must achieve the requirements of Sections XVII.C.2.a. and XVII.C.2.b. and begin implementing the required approved instrument monitoring method in accordance with the following schedule: XVII.C.2.b.(ii)(a) A storage tank constructed on or after May 1, 2014, must comply with the requirements of Section XVII.C.2.a. by the date the storage tank commences operation. The storage tank must comply with Section XVII.C.2.b. and implement the approved instrument monitoring method inspections within ninety (90) days of the date that the storage tank commences operation. XVII.C.2.b.(ii)(d) 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. AIRS ID: 123/8488 Page 6 of 15 olor Depa en P` li Health and Environment it Pollution Control Division rabfi= - St ta"e rik Insp c ons Threshold: Storage Tank Approved Instrument Phase-In Schedule Uncontrolled Actual VOC Monitoring Method Emissions (tpy) Inspection Frequency > 6 and < 12 Annually January 1, 2016 > 12 and < 50 Quarterly July 1, 2015 > 50 Monthly January 1, 2015 XVII.C.2.b.(iii) Owners or operators are not required to monitor storage tanks and associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. XVII.C.2.b.(iv) STEM must include a certification by the owner or operator that the selected STEM strategy(ies) are designed to minimize emissions from storage tanks and associated equipment at the facility(ies), including thief hatches and pressure relief devices. XVII.C.3. Recordkeeping XVII.C.3. The owner or operator of each storage tank subject to Sections XII.D. or XVII.C. must maintain records of STEM, if applicable, including the plan, any updates, and the certification, and make them available to the Division upon request. In addition, for a period of two (2) years, the owner or operator must maintain records of any required monitoring and make them available to the Division upon request, including: XVII.C.3.a. The AIRS ID for the storage tank. XVII.C.3.b. The date and duration of any period where the thief hatch, pressure relief device, or other access point are found to be venting hydrocarbon emissions, except for venting that is reasonably required for maintenance, gauging, or safety of personnel and equipment. XVII.C.3.c. The date and duration of any period where the air pollution control equipment is not operating. XVII.C.3.d. Where a combustion device is being used, the date and result of any EPA Method 22 test or investigation pursuant to Section XVII.C.1.d.(v). XVII.C.3.e. The timing of and efforts made to eliminate venting, restore operation of air pollution control equipment, and mitigate visible emissions. XVII.C.3.f. A list of equipment associated with the storage tank that is designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.C.1.e., an explanation stating why the equipment is so designated, and the plan for monitoring such equipment. AIRS ID: 123/8488 Page 7 of 15 olorl Depa en P •liHealth and Environment it Pollution Control Division 19. Points 002, 0 ' • .) _ - this -Alit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: XVII.B.2.b If a 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 combustion device, or by other means approved by the Division, determine whether it is operating properly. XVII.B.2.d.(i) All combustion devices installed on or after May 1, 2014, must be equipped with an operational auto-igniter upon installation of the combustion device. 20. Point 004: 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) 21. Point 004: 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 the conditions (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. 22. Point 004: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 23. Point 005: The separator covered by this permit is 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. AIRS ID: 123/8488 Page 8 of 15 3^ y t twx5 oloraR Depa en P li Health and Environment it Pollution Control Division OPERATING & MAiI N 24. Point 002, 003, 004, and 005: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements. 25. Point 002, 003, 004, and 005: 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) 26. Point 005: 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 a site-specific emission factor for the pollutant (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 factors established in the permit application for this emissions point are valid. ADDITIONAL REQUIREMENTS 27. 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 NO, per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or AIRS ID: 123/8488 Page 9 of 15 ro olor_. Depa I en P .li Health and Environment it Pollution Control Division c. When:-- -i_ � ' cr --en • - ed, o -never 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. 28. 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 29. 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. 30. 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. 31. 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. 32. 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. 33. 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. AIRS ID: 123/8488 Page 10 of 15 olora Depa en f P JHealth and Environment it Pollution Control Division • 34. Section 25-7- 2O1 a), S. des ,burces,cequired 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. 35. 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: Betsy Gillard Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Noble Energy, Inc. AIRS ID: 123/8488 Page 11 of 15 olor. 1 Depa en . P .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.qov/cs/Satellite?c=Document C&ch lid pagename=CDPHE- Main%2FDocument C°/02FCBONAddLinkView&cid=1251599389641&paciename-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 Are the Controlled AIRS Emission Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) Benzene 71432 1435 Yes 72 n-Hexane 110543 9170 Yes 459 Toluene 108883 1750 Yes 88 002 Ethylbenzene 100414 35 No 2 Xylenes 1330207 140 No 7 2,2,4-TMP 540841 210 No 11 Benzene 71432 1400 Yes 70 003 n-Hexane 110543 4400 Yes 220 Benzene 71432 654 Yes 33 n-Hexane 110543 4132 Yes 207 Toluene 108883 2873 Yes 144 004 Ethylbenzene 100414 38 No 2 Xylenes 1330207 1005 Yes 50 2,2,4-TMP 540841 325 Yes 16 AIRS ID: 123/8488 Page 12 of 15 f. `1, olor ,' Depar= enl f P-I-- Ii&Health and Environment it Pollution Control Division Y ; ncotOpMia Aire Controlled AIRS Emission Rate emissions Emission Rate Point Pollutant CAS # (lb/yr) reportable? (Ib/yr) Benzene 71432 1404 Yes 70 n-Hexane 110543 9395 Yes 470 005 Toluene 108883 2019 Yes 101 Ethylbenzene 100414 17 No 1 Xylenes 1330207 148 No 7 2,2,4-TMP 540841 309 Yes 15 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Emission Factors Pollutant Uncontrolled Source lb/BBL Condensate Throughput VOC 1.0991 HYSYS n-Hexane 0.0262 HYSYS Benzene 0.0041 HYSYS Toluene 0.0050 HYSYS Ethylbenzene 0.0001 HYSYS Xylenes 0.0004 HYSYS 2,2,4-TMP 0.0006 HYSYS Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 003: Emission Factors Pollutant Uncontrolled Source lb/BBL Produced Water Throughput VOC 0.262 CDPHE n-Hexane 0.022 CDPHE Benzene 0.007 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 004: Emission Factors-Uncontrolled Pollutant lb/BBL loaded Source VOC 0.285 AP-42 Benzene 0.0019 AP-42 n-Hexane 0.0118 AP-42 Toluene 0.0082 AP-42 Ethylbenzene 0.0001 AP-42 Xylenes 0.0029 AP-42 2,2,4-TMP 0.0001 AP-42 AIRS ID: 123/8488 Page 13 of 15 olorl Depa en . P Health and Environment A it Pollution Control Division The uncontroll=" % 4 -mi -S .e... ff _�;" using •_ „2, 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 lb/lb-mol T(temperature of liquid loaded) = 520 °R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each NCRP in the vapors from the HYSYS results by the VOC emission factor. Point 005: Weight Emission Factors Pollutant Fraction of Uncontrolled Source Gas(%) lb/MMscf NOx(lb/lb-VOC) --- 0.0037 AP-42 CO (lb/lb-VOC) --- 0.0094 AP-42 VOC 60.14 55475.81 Gas Analysis/HYSYS Benzene 0.296 272.76 Gas Analysis/HYSYS Toluene 0.426 393.02 Gas Analysis/HYSYS Ethylbenzene 0.002 1.76 Gas Analysis/HYSYS Xylenes 0.043 39.45 Gas Analysis/HYSYS n-hexane 1.927 1777.38 Gas Analysis/HYSYS 2,2,4-TMP 0.054 49.72 Gas Analysis/HYSYS 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, HAPs, n-Hexane NANSR Synthetic Minor Source of: VOC MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable AIRS ID: 123/8488 Page 14 of 15 �oloraDepa Y en PI1IlJHealth and Environment it Pollution Control Division 8) Fullof the TiI ";, , F Regulations can u text t e� � o'':ec ' f �rfl me >�,ectronic Co �„;. € ederal be found at the website listed below: http://ecfr.gpoaccess.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 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.gov/pacific/cdphe/air-permit-self-certification AIRS ID: 123/8488 Page 15 of 15 Division Information Engineer: Betsy Gillard Control Engineer: Stefanie Rucker Review Date: 10/07/2015 Application Date: 04/01/2015 Facility Identifiers Permit No. 15WE0704 Potentially located in ozone nonattainment area AIRs County# 123 (Weld Facility# 8488 Facility Type: exploration and production facility ❑ Located in the 8-hour non-attainment area? O True Minor ® Synthetic Minor for: t✓ VOC t NOx f.7 CO Administrative Information Company Name: Noble Energy, Inc. Source Name: Burton K25-67-1HN, 68-1HNL, 69-1HNL Source Location: SWNW Sec 25 TWP4 R66W SIC: 1311 Address 1: Noble Energy, Inc. Mailing Address 2: 1625 Broadway, Suite 2200 Address ty,State Zip: Denver,CO 80202 Name: Mike Putney Person To Phone: 303-228-4385 Contact Fax: Email: mike.putney@nblenergy.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Burton K25-67-1 HN, 68-1 HNL, 69-1 HNL, located in the SWNW Sec 25 TWP4 R66W,Weld County,Colorado. Point Name Type Control Action Newly 002 Tank Battery Condensate Tanks Flare reported source Produced Newly 003 Water Tanks Flare reported Water source Truck Newly 004 Loadout Loadout Flare reported source VRU &VRT Newly 005 VOC Separator Venting Flare reported Burners source 002 Nine (9)above ground 538 bbl atmospheric condensate storage tanks Requsted Throughput 350000 bbl Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 1.0991 lb/bbl 192.3 tpy 9.6 tpy HYSYS Nox 0.0037 Ib/Ib-VOC -- tpy 0.7 tpy CDPHE CO 0.0094 Ib/Ib-VOC -- tpy 1.8 tpy CDPHE Benzene 0.0041 lb/bbl 1435 lb/yr 71.75 lb/yr HYSYS n-Hexane 0.0262 lb/bbl 9170 lb/yr 458.5 lb/yr HYSYS Toluene 0.005 lb/bbl 1750.0 lb/yr 87.5 lb/yr HYSYS 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 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 Organic Compounds XII. VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS Applicant is subject to the emission control requirements for condensate tanks since it is located in a nonattainment area XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... Applicant is subject since actual uncontrolled emissions are>20 tpy of VOC. 003 Three(3)above ground 500 bbl produced water storage tanks Emissions Calculations Requsted Throughput 200000 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 26.2 tpy 1.31 tpy CDPHE Nox 0.0037 Ib/Ib-VOC -- tpy 0.10 tpy CDPHE CO 0.0094 Ib/Ib-VOC -- tpy 0.25 tpy CDPHE Benzene 0.007 lb/bbl 1400 lb/yr 70 lb/yr CDPHE n-Hexane 0.022 lb/bbl 4400 lb/yr 220 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. 004 Hydrocarbon Loadout to Tanker Trucks Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2,Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 7.88 psia AP-42 M Molecular Weight of Vaty 60 lb/lb-mole AP-42 T Liquid Temperature 520 deg. R Field Data L 6.80 lb/10^3 gal 2.85E-01 lb/bbl Annual requested Throughput 350000 BBL/yr 14700000 gal/yr Annual requested VOC emissions 99922 lb/yr 49.96 tpy Control: Flare Efficiency: 95.00% NCRPs Component Mass Fraction Benzene 0.0065 n-hexane 0.0414 Toluene 0.0288 Xylenes 0.0101 2,2,4-TMP 0.0033 Source: Pressurized oil sample Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2850 lb/bbl 49.9 tpy 2.5 tpy AP-42 Nox 0.0037 Ib/Ib-VOC -- tpy 0.18 tpy CDPHE CO 0.0094 Ib/Ib-VOC -- tpy 0.47 tpy CDPHE Benzene 0.0019 lb/bbl 652.4 lb/yr 32.6 lb/yr AP-42 n-Hexane 0.0118 lb/bbl 4125 lb/yr 206 lb/yr AP-42 Toluene 0.0082 Ib/bbl 2868 lb/yr 143 lb/yr AP-42 Xylenes 0.0029 lb/bbl 1003 lb/yr 50 lb/yr AP-42 2,2,4-TMP 0.0009 lb/bbl 324.2 lb/yr * 16.2 lb/yr AP-42 Regulatory Review 'Regulation 3-APEN and Permitting Requirements Is this site considered an exploration and production location(e.g.well pad)? Yes If yes, review the following two exemptions for applicability: Does the operator unload less than 10,000 gallons(238 BBLs)per day of crude oil on an annual average basis? No If yes,this emissions point is categorically exempt from permit requirements per Regulation 3,Part B,Section 11.0.1.1 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 11.0.1.1 • Paint 005-LP and VRT Venting Calculations LP calculations Actual Throughput(H0565) 8279 Sct/hr 0.1987 MM5cf/day 49674 MMScf/yr Total mass flow 760.1942 lb/hr H25 0 Annual runtime 600 hrs Oxygen 0 C02 27.8227 Actual Nitrogen 1.0279 lb/hr Ib/scf Ib/Mscf lb/yr tpy Methane 135.6919 VOC 455.4527 0.05501301 5501 273272 136.64 Ethane 140.199 Benzene 2.2817 0.0002756 0.28 1369 0.68 VOC mass flow 455.4527 lb/hr Totals Toluene 3.3151 0.00040042 0.40 1989 0.99 E-Benzene 0.0149 1.7997E-06 0.00 9 0.00 Throughput 5.287 MMScf/yr Xylenes 0.3355 4.0524E-05 0.04 201 0.10 2,2,4-TMP 0.4191 5.0622E-OS 0.05 251 0.13 Uncontrolled Controlled(95%) n-Hexane 14.8847 0.00179789 1.80 8931 4.47 lb/yr lb/Mscf tpc lb/yr Ib/Mscf tpy VRT Calculations VOC 293281 55476 146,64 14664 2.774 7.33 Not -- — — 1085 0.54 Actual Throughput(00505) 532 Scf/hr CO -- — — 2757 1.38 0.01277 MMScf/day Benzene 1442 0.273 0.72 72 0014 004 0.31925 MMScf/yr Toluene 2078 0393 1.04 104 0.020 0.05 Total mass flow 52.6179 lb/hr E-Benzene 9 0.002 0.00 0 0.000 0.00 ' H25 0 xylenes 209 0.039 0.10 10 0.002 0.01 Annual runtime 600 hrs Oxygen 0 2,2,4-TMP 263 0050 0.13 13 0002 0.01 C02 1.8536 n-Hexane 9396 1777 4,70 470 0.089 023 Actual Requested Nitrogen 0.0183 lb/hr Ib/scf Ib/Mscf lb/yr tpy Methane 5.8646 VOC 33.3493 00627 62677 20010 1000 Ethane 11.5321 Benzene 0.1216 00002 0.229 73 004 VOC mass flow 33.3493 lb/hr Toluene 0.1478 0.0003 0.278 89 0.04 E.Benzene 0.0006 0.0000 0.001 0 0.00 xylenes 0.0121 0.0000 0.023 7 0.00 2,2,4-TMP 0.019 0.0000 0.036 11 001 n-Hexane 0.7759 0.0015 1.458 466 0.23 n1 0 °' °°' ad Z Z Z id o EO n. 3 T C ° a,o u y Lp, ais ❑ . 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