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Home My WebLink About20153631.tiff ,, CDPHE= ! COLORADO Co Department of Public Health&Environment Dedicated to protecting and improving the health and environment of the people of Colorado Weld County - Clerk to the Board 11500 St PO Box 758 Greeley, CO 80632 RECEIVED November 3, 2015 NOV 1 6 2015 WELD COUNTY Dear Sir or Madam: COMMISSIONERS On November 4, 2015, the Air Pollution Control Division will begin a 30-day public notice period for Noble Energy, Inc. - Five Rivers K07, K08, K09 Econode. 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 E. Environment APCD-SS-B1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure u Do (7 tA.), At "fit, 2015-3631 i --18 --/5- 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe John W. Hickenlooper, Governor I Larry Wolk,MD,MSPH, Executive Director and Chief Medical Officer r x' cDpHE Air Pollution Control Division CO s Notice of a Proposed Project or Activity Warranting Public r„ Comment Website Title: Noble Energy, Inc. - Five Rivers K07, K08, K09 Econode - Weld County Notice Period Begins: November 4, 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: Five Rivers K07, K08, K09 Econode Oil and gas exploration and production facility NESE Sec8 T4N R66W Weld County The proposed project or activity is as follows: The applicant proposes to operate a new oil and gas production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section 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 15WE0366 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: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-B1 Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us WV COLORADO o STATE OF COLORADO ; .s �. of coed LORADO Li cT ENT OF PI BLIC HEALTH AND ENVIRONMENT 4w=` AIR POLLUTION CONTROL DIVISION TELEPHONE: (303)692-3150 , . *1876' CONSTRUCTION PERMIT PERMIT NO: 1 5WE0366 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 Five Rivers K07, K08, K09 Econode, located in the NESE Section 8, 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. The loadout is controlled Loadout 006 by routing vapors directly to an enclosed flare. Each flare has a minimum control efficiency of 95%. Produced Six (6) 538 bbl above ground atmospheric fixed roof produced Water 007 water storage vessels controlled by an enclosed flare. The flare has a minimum control efficiency of 95%. Tank Eighteen (18) 538 bbl above ground atmospheric fixed roof Battery 008 condensate storage vessels controlled by enclosed flare(s). Each flare has a minimum control efficiency of 95%. LP and Venting of gas produced from thirteen low-pressure (LP) VRT VOC 009 separators and two vapor recovery towers (VRTs)controlled by eight enclosed flares. Each flare has a minimum control Burners efficiency of 95%. 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 issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at AIRS ID: 123/9D9F Page 1 of 15 olor. Depa en . P .Ii ealth and Environment ' 'it Pollution Control Division www.cdohe.st- /a,.t n - . _m ` --I -ilure -tify 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). 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. AIRS Point 009:Within one hundred and eighty (180) days after issuance of this permit, the operator shall install flow meters to monitor and record total volumetric flowrate of gas vented from the low pressure separators to an enclosed flare and to monitor and record total volumetric flowrate of gas vented from the vapor recovery towers to an enclosed flare. The operator shall use the gas flow rates listed in the application for actual flow rate until the flow meters are installed, not to exceed one hundred and eighty (180)days after issuance of this permit 5. 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.) 6. 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 7. 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 No. Truck Loadout 006 --- 5.6 -- Point Produced 007 3.0 Point Water Tank Battery 008 3.6 47.4 9.0 Point LP and VRT 009 1.6 20.2 3.9 Point VOC Burners See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. AIRS ID: 123/9D9F Page 2 of 15 .₹ r iiF,olora,A4Depa ens P li ealth and Environment it Pollution Control Division 6 y .031 ittl Facility-wide enlissiont ofA h ittgatteitial,idzardous air pgi!utant 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. 8. 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 006 Enclosed Flare VOC Loadout Produced 007 Enclosed Flare VOC Water Tank 008 Enclosed Flare VOC Battery LP and VRT VOC 009 Enclosed Flare VOC Burners PROCESS LIMITATIONS AND RECORDS 9. 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 006 Condensate Loaded 775,000 BBL Loadout Produced 007 Produced Water Throughput 465,000 BBL Water Tank 008 Condensate Throughput 775,000 BBL Battery LP and Total Gas Vented from all Low-Pressure VRT VOC 009 Separators and Vapor Recovery Towers 15.6 MMSCF Burners (VRTs)to enclosed flare AIRS ID: 123/9D9F Page 3 of 15 olor. ' Depa en ► P .l Ill li ealth and Environment 'ill-Pollution Control Division Compliance n - -ro - -- Ii ie det- ed 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. 10. AIRS Point 009: Upon installation of the flow meter required under Condition 4, the owner or operator shall continuously monitor and record the volumetric flowrate, using flow meters, of gas vented from the low pressure separators to the enclosed flare and gas vented from the VRTs to the enclosed flare. Flow meters shall continuously measure flowrate and record total volumetric flow vented to the enclosed flare(s) from the low- pressure separators and from the VRTs. The owner or operator shall use the sum of monthly throughput records for the low pressure separator gas routed to flare and VRT gas routed to flare to demonstrate compliance with the limits specified in Condition 9 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 11. 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) 12. 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.) 13. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 14. AIRS Point 006: 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) 15. AIRS Point 006: 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. 16. AIRS Point 006: 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. AIRS ID: 123/9D9F Page 4 of 15 ql `0,,oloraj Depar en of PpoliccHealth and Environment 9 solAir Pollution Control Division omo �,.. 17. AIRS Point 0laelThet'0wrieflor oilterator of4alleactdut which, being controlled shall: a. Install and operate the vapor collection equipment to collect vapors during loading of tank compartments of outbound transport trucks and route these vapors to the enclosed flare. 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. 18. AIRS Points 007, 008, and 009: The flare(s) covered by this permit 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 Auto-igniters: All combustion devices used to control emissions of hydrocarbons must be equipped with and operate an auto-igniter as follows: 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. XVll.B.2.d.(ii) All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 19. AIRS Points 007 and 008: 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. AIRS ID: 123/9D9F Page 5 of 15 olor.1 Depa en P ..li ealth and Environment it Pollution Control Division XVII.C . >I =-m — -ction .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. XVII.C.2. Capture and monitoring requirements for storage 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 AIRS ID: 123/9D9F Page 6 of 15 f y olora° Depa ern P lie-Health and Environment Qn, it Pollution Control Division r-el 4774 o a documente f Storage TAni ,Emi agernefi 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. Table 1 —Storage Tank Inspections 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 AIRS ID: 123/9D9F Page 7 of 15 olor- ' Depa en • P •Ii ealth and Environment it Pollution Control Division to; - _-nr' .. , iat ::a-• _,• ent - 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. 20. AIRS Point 008: 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. 21. AIRS Point 008: 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. 22. AIRS Point 008: 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 shall operate air pollution control equipment that has an average control efficiency of at least 95%for VOCs on such tanks. 23. AIR Point 009: The separation equipment, including low pressure separators and vapor recovery towers, covered by this permit is subject to Regulation 7, Section XVII.G. (State AIRS ID: 123/9D9F Page 8 of 15 00, 41 4 olora Depar err:6f- P lic Health and Environment @, ? it Pollution Control Division 41 _If Only). On or after, ,L-gasc , -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 24. AIRS Points 006—009: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record keeping format approved by the Division, in order to demonstrate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 25. AIRS Points 007 - 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) 26. AIRS Point 009: The operator shall complete initial site specific extended gas analyses of the gas vented from the low pressure separator and of gas vented from the VRT in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4- trimethylpentane content (weight fraction) of these emission streams. Results of testing shall be used to calculate site-specific emission factors for the pollutants referenced above (in units of Ib/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 the emissions factors established through this initial testing are less than or equal to, the emissions factors established in the permit application and "Notes to Permit Holder" for this emissions point. If any site specific emissions factor developed through this sampling and analysis is greater than the emissions factors established in the permit application and "Notes to Permit Holder" the operator shall submit to the Division within 60 days, a request for permit modification to update emissions factors and emissions limits specified in this permit. 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 AIRS ID: 123/9D9F Page 9 of 15 Depa en • P •Ii '' ealth and Environment 11 it Pollution Control Division year, - - in a e t•'• . f one in per year or more or five percent,whichever is greater, above the level reported on the last APEN;or For sources emitting 100 tons per year or more, a change in actual emissions of five percent or 50 tons per year or more, whichever is less, above the level reported on the last APEN submitted; or For any non-criteria reportable pollutant: If the emissions increase by 50% or five (5) tons per year, whichever is less, above the level reported on the last APEN submitted to the Division. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 28. Federal regulatory program requirements (i.e. PSD, NANSR)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. AIRS ID: 123/9D9F Page 10 of 15 <yh .,.. '" -✓erN v,I4z1741}vim rom n V.70 c olor. kaDepaGteen 6-f P Iic Health and Environment R \ir Pollution Control Division 32. Unless specifi�JLy stated oth"erWise 11 a getie6aliatid 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. 34. 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. 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: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Noble Energy Inc. AIRS ID: 123/9D9F Page 11 of 15 olor-A Depa en . P .li ealth 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&childpaqename=CDPHE- Main%2FDOcument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapoer 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s)operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (lb/yr) reportable? (Ib/yr) Benzene 71432 609 Yes 30 n-Hexane 110543 4,081 Yes 204 Toluene 108883 1,192 Yes 60 006 Ethylbenzene 100414 26 No 1 Xylenes 1330207 132 No 7 2,2,4- 540841 132 No 7 trimethylpentane Benzene 71432 3,255 Yes 163 007 - n-Hexane 110543 10,230 Yes 512 Benzene 71432 5,158 Yes 258 n-Hexane 110543 34,365 Yes 1,718 Toluene 108883 10,045 Yes 502 008 Ethylbenzene 100414 159 No 8 Xylenes 1330207 1,130 Yes 57 2,2,4- 540841 1,214 Yes 61 trimethylpentane Benzene 71432 2,101 Yes 105 009 n-Hexane 110543 14,146 Yes 707 AIRS ID: 123/9D9F Page 12 of 15 . olora.' ',Depa ens c�f P olio°: ealth and Environment fir Pollution Control Division 1"4 NA Touter '' ; fl88 4,413tajA v,Y0V 221 Ethylbenzene 100414 35 No 2 Xylenes 1330207 313 Yes 16 2,2,4- 540841 521 Yes 26 trimethylpentane 5) The emission levels contained in this permit are based on the following emission factors: Point 006: Uncontrolled Controlled lb/BBL lb/BBL Pollutant loaded loaded Source VOC 0.2899 0.0145 AP-42 Benzene 0.0008 0.00004 _ AP-42 n-Hexane 0.0053 0.00026 AP-42 Toluene 0.0015 0.00008 AP-42 Ethylbenzene 0.00003 0.000002 AP-42 Xylenes 0.0002 0.00001 AP-42 2,2,4- 0.0002 0.00001 AP-42 trimethylpentane 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)=7.8808 psia M (vapor molecular weight)=60 Ib/Ib-mol T (temperature of liquid loaded)=512 R The uncontrolled non-criteria reportable air pollutant (NCRP) emission factors were calculated by multiplying the mass fraction of each in the stable condensate by the VOC emission factor. Point 007: Uncontrolled Controlled lb/BBL Produced Ib/BBL Produced Pollutant Water Throughput Water Throughput Source VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 008: Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput VOC 2.4484 0.1224 HYSYS Model n-Hexane 0.0444 0.0022 HYSYS Model AIRS ID: 123/9D9F Page 13 of 15 olor. _ Depa en`. P .li ealth and Environment •it Pollution Control Division Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput Benzene 0.0067 0.0003 HYSYS Model Toluene 0.013 0.0006 HYSYS Model Ethylbenzene 0.0002 0.00001 HYSYS Model Xylenes 0.0015 0.00007 HYSYS Model 2,2,4- 0.0016 0.00008 HYSYS Model trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. Point 009: Emissions from the separation equipment result from venting of LP separator gas to enclosed flare(s) as well as from venting of VRT gas to enclosed flare(s). Emission factors are detailed below for each emission scenario in two tables. Actual emissions are calculated using the emission factor and corresponding actual process rate for each emission scenario. Total actual emissions for this point are based on the sum of emissions calculated for both emission scenarios. Table 1: LP Separator Emission Factors Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx(lb NOx/lb ___ 0.0037 0.0037 CDPHE Memo VOC) CO(lb CO/lb ___ 0.0094 0.0094 CDPHE Memo VOC) VOC 55.8 47,811 2,390.5 HYSYS Model Benzene 0.14 123.67 6.1836 HYSYS Model Toluene 0.31 267.45 13.373 HYSYS Model Ethylbenzene 0.003 2.5212 0.1261 HYSYS Model Xylenes 0.02 15.687 0.7844 HYSYS Model n-hexane 0.98 841.34 42.067 HYSYS Model 2,2,4- 0.04 30.140 1.5070 HYSYS Model trimethylpentane Table 2:VRT Emission Factors Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas(%) Uncontrolled Controlled lb/MMscf lb/MMscf NOx(lb NOx/Ib ___ 0.0037 0.0037 CDPHE Memo VOC) CO(lb CO/lb ___ 0.0094 0.0094 CDPHE Memo VOC) VOC 85,475 4,273.7 HYSYS Model Benzene 226.73 11.337 HYSYS Model Toluene 413.34 20.667 HYSYS Model Xylenes 56.026 2.8013 HYSYS Model n-hexane 1,455.3 72.764 HYSYS Model AIRS ID: 123/9D9F Page 14 of 15 ,olora,'i Depar rien rJf P lic`Health and Environment ., it Pollution Control Division 414 1Neight._.. .a Euis ion ,... .., Emission Pollutant Fraction Factors Factors Source of Gas (%) Uncontrolled Controlled lb/MMscf lb/MMscf 2,2,4- 60.280 3.0140 HYSYS Model trimethylpentane Note: The uncontrolled VOC and HAP emissions were calculated based on a HYSYS model to estimate the VOC and HAP content of each stream and stream flows. The controlled emissions for this point are based on a 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. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC, Total HAPs, n-hexane NANSR Synthetic Minor Source of: VOC 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.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: 123/9D9F Page 15 of 15 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 06/02/2015 Application Date: 02/06/2015 Facility Identifiers Permit No. 15WE0366 Potentially located in ozone nonattainment area AIRS County# 123 Weld Facility# 9D9F Facility Type: exploration and production facility Located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: 1 VOC r NOx r CO Administrative Information Company Name: Noble Energy Inc. Source Name: Five Rivers K07, K08, K09 Econode Source Location: NESE Section 8,Township 4N, Range 66W SIC: 1311 Address 1: Noble Energy Inc. Mailing Address 2: 1625 Broadway,Suite 2200 Address ity,State Zip: Denver,CO 80202 Name: Jaclyn Schaffner Person To Phone: 720-587-2326 Contact Fax: 303-228-4362 Email: jchaffner@nobleenergyinc.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Five Rivers K07,K08,K09 Econode,located in the NESE Section 8,Township 4N,Range 66W,Weld County,Colorado. Point Name Type Control Action 004 Fugitive Fugitives None Source requested to cancel on 10/28/2015 Emissions 006 Truck Loadout Newly reported source Loadout 007 Produced Water Tanks Flare Newly reported source Water 008 Tank Battery Condensate Tanks Flare Newly reported source LP and VRT 009 VOC Separator Venting Flare Newly reported source Burners VRT VOC Separator Venting Flare Source requested on 10/28/2015 to combine 010 Burners Pt 009 and 010 as one point *Pts 001 -003 are engines covered by GP02 *Source requested Pt 005 to be canceled 8/5/2015 and split into Points 009 and 010 instead 004 Fugitive VOC equipment leaks SOURCE REQUESTED TO CANCEL ON 10/28/2015 SINCE EMISSIONS ARE LESS THAN APEN THRESHOLDS Regulation 7 Information Operating Hours: 8760 hours/year Emission Factor Source Screening EFs-EPA-453/R-95-017 Table 2-8 Control Efficiency Source: None Calculations Emission Factor(kg/hr- Emissions Service Component Type Count source) Control(%)Pollutant Mass Fraction (tpy) Table 2-4 Table 2-8 Reg.3 Connectors 4748 2.00E-04 1.00E-05 0.0% VOC 0.19138 0.3275177 Flanges 484 3.90E-04 5.70E-06 0.0% Benzene 0.00101 0.0017285 Open-Ended Lines 44 2.00E-03 1.50E-05 0 0% Toluene 0.00085 0.0014546 Gas Pump Seals 0 2.40E-03 3.50E-04 0.0% Elhylbenzene 0.00003 5.134E-05 Valves 1410 4.50E-03 2.50E-05 0.0% Xylenes 0.00013 0.0002225 Other 759 8.80E-03 1.20E-04 0.0% n-Hexane 0.00355 0.0060753 Connectors 0 7.50E-06 7.50E-06 0.0% VOC 1 0 Flanges 0 3.90E-07 3.90E-07 0.0% Benzene 0.0053 0 Open-Ended Lines 0 1.40E-04 7.20E-06 0.0% Toluene 0.0044 Heavy Oil 0 Pump Seals 0 0.OOEiO0 0.00E+00 0.0% Elhylbenzene 0.0002 0 Valves 0 8.40E-06 8.40E-06 0.0% Xylenes 0.0007 0 Other 0 3.20E-05 3.20E-05 0.0% n-Hexane 0.0568 0 Connectors 1133 2.10E-04 9.70E-06 0.0% VOC 1 0406183 Flanges 179 1.10E-04 2.40E-06 0.0% Benzene 0.0053 0.0021528 Open-Ended Lines 0 1.40E-03 1.40E-05 0.0% Toluene 0.0044 0.0017872 Light Oil Pump Seals 0 1.30E-02 5.10E-04 0.0% Ethylbenzene 0.0002 8.124E-05 Valves 1115 2.50E-03 1.90E-05 0.0% Xylenes 0.0007 0.0002843 Other 86 7.50E-03 1.10E-04 0.0% n-Hexane 0.0568 0.0230712 Connectors 666 1.10E-04 1.00E-05 0.0% VOC 1 0.1424996 Flanges 38 2.90E-06 2.90E-06 0.0% Benzene 0.0053 0.0007552 Open-Ended Lines 0 2.50E-04 3.50E-06 0.0% Toluene 0.0044 0.000627 Water/Oil Pump Seals 0 2.40E-05 2.40E-05 0.0% Ethylbenzene 0.0002 2.85E-05 Valves 276 9.80E-05 9.70E-06 0.0% Xylenes 0.0007 9.975E-05 Other 90 1.40E-02 5.90E-05 0.0% n-Hexane 0.0568 0.008094 'Gas stream composition is based on sales gas sample collected 12/22/2014 from Five Rivers K07 K08&K09 Econode Emissions Summary Table Pollutant Uncontrolled Emissions Controlled Emissions Source VOC 0.88 Ipy 0.88 tpy Screening EFs-EPA-453/R-95-017 Table 2-8 Benzene 9 lb/yr 9 lb/yr Screening EFs-EPA-453/R-95-017 Table 2-8 Toluene 8 lb/yr 8 lb/yr Screening EFs-EPA-453/R-95-017 Table 2-8 Ethylbenzene U lb/yr 0 lb/yr Screening EFs-EPA453/R-95-017 Table 2-8 Xylenes 1 lb/yr 1 Ib/yr Screening EFs-EPA-453/R-95-017 Table 2-8 n-Hexane 74 lb/yr 74 lb/yr Screening EFs-EPA-4531R-95-017 Table 2-8 Regulatory Applicability Reg.3 Review Regulation 3,Part B,Section III.D.2 to determine is RACT is required? Yes-Reg 7 satisfies RACT Review 40 CFR,Part 60,Subpart KKK to determine if applicable to this source? No Reg.6 Review 40 CFR,Part 60,Subpart 0000 to determine if 60.5380 and/or 60.5385 is applicable? No Reg.7 Review Section XVII.F to determine is LDAR is applicable? Yes 15WE0366.CP1 123/9D9F 006 Hydrocarbon Loadout to Tanker Trucks.The loadout is controlled by an enclosed flare. 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 for submerged loading, dedicated normal P True Vapor Pressure 7.8807589 psia Based on EPA Tanks output M Molecular Weight of Vaf 60 lb/lb-mole Based on EPA Tanks output for Gasoline RVP 1 T Liquid Temperature 512.12 deg. R EPA Tanks Data for liquid bulk temp for Denver, L 6.90 lb/10^3 gal 2.90E-01 lb/bbl Annual requested Throughput 775000 BBL/yr 2123 bbl/day 32550000 gal/yr Annual requested VOC emissions 224682 lb/yr 112.34 tpy Control: Flare Efficiency: 95.00% NCRPs Component Mass Fraction Benzene 0.0023 n-hexane 0.0154 Toluene 0.0045 Ethylbenzen 0.0001 Xylenes 0.0005 224-TMP 0.0005 Source: HAP mass fraction based on flash emission speciation from condensate tank in Promax run Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2899 lb/bbl 112.3 tpy 5.6 tpy AP-42 Benzene 0.0008 lb/bbl 609 lb/yr 30 lb/yr AP-42 n-Hexane 0.0053 lb/bbl 4081 lb/yr 204 lb/yr AP-42 Toluene 0.0015 lb/bbl 1192 lb/yr 60 lb/yr AP-42 Ethylbenzen 0.00003 lb/bbl 26 lb/yr 1 lb/yr AP-42 Xylenes 0.0002 lb/bbl 132 lb/yr 7 lb/yr AP-42 224-TMP 0.0002 lb/bbl 132 lb/yr 7 lb/yr AP-42 15WE0366.CP1 123/9D9F 006 Hydrocarbon loadout to Tanker Trucks.The loadout is controlled by an enclosed flare. 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 11.1.1.1 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 15WE0366.CP1 123/9D9F Six(6)above ground fixed roof 538 bbl produced water storage tanks controlled by 007 an enclosed flare.The flare has a minimum control efficiency of 95%. Emissions Calculations Requsted Throughput 465000 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 0.262 lb/bbl 60.9 tpy 3.0 tpy CDPHE Benzene 0.007 lb/bbl 3,255 lb/yr 163 lb/yr CDPHE n-Hexane 0.022 Ib/bbl 10,230 lb/yr 512 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. 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 7—Volatile Organic Compounds XVII.C.1.b Applicant is subject since actual uncontrolled emissions are greater than 6 tpy. The storage tank was constructed after 5/1/2014. 15WE0366.CP1 123/9D9F Eighteen(18)538 bbl above ground atmospheric fixed roof condensate storage tanks 008 controlled by enclosed flare.The flare has a minimum control efficiency of 95%. Requsted Throughput 775000 bbl Control Flare 1 Efficiency 95.00%] Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 2.4484 lb/bbl 948.7 tpy 47.4 tpy HYSYS Benzene 0.0067 lb/bbl 5,158 lb/yr 258 lb/yr HYSYS n-Hexane 0.0443 lb/bbl 34,365 lb/yr 1,718 lb/yr HYSYS Toluene 0.0130 lb/bbl 10,045 lb/yr 502 lb/yr HYSYS Ethylbenze 0.0002 lb/bbl 159 lb/yr 8 lb/yr HYSYS Xylenes 0.0015 lb/bbl 1,130 lb/yr 57 lb/yr HYSYS 224-TMP 0.0016 lb/bbl 1,214 lb/yr 61 lb/yr HYSYS Nox 0.0037 lb/lb V0C 3.6 tpy 3.6 tpy CDPHE Memo CO 0.0094 lb/lb V0C 9.0 tpy 9.0 tpy CDPHE Memo Regulatory Review Section II.A1 -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. Regulation 2—Odor Section I.A-No person,wherever located,shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven(7)or more volumes of odor free air. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 420,000 gallons and is located prior to custody transfer. 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 the facility is located in the nonattainment area. XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS Applicant is currently subject to this requirement since actual uncontrolled emissions are greater than 20 tpy of VOC and actual uncontrolled emissions are greater than 6 tpy.The tank battery is considered a new tank since it was constructed after 5/1/2014. 15WE0366.CP1 123/9D9F Thirteen low-pressure(LP)separators controlled by eight enclosed flares during VRU downtime.Each 009 flare has a minimum control efficiency of 95%. • Equipment Description This source vents natural gas from: a low pressure separator during VRU downtime Emissions from this source are: routed to a flare 'Natural gas venting from a low pressure separator during VRU downtime.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q'MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow rate/volume of gas processed MW=Molecular weight of gas=SG of gas'MW of air Xx=mass fraction of x in gas C=molar volume of ideal gas(379 scf/lb-mol)at 60F and 1 atm • Throughput(0) 13.85905 MMscf/yr 1582.083333 scf/hr MW 32.4622 Ibllb-mol 0.03797 MMscf/d mole% MW lbx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.02 44.01 0.889 0.027 3.71 32508.50 16.25 N2 020 28.013 0.056 0.002 0.23 2048.73 1.02 methane 41.48 16.041 6.654 0.205 27.78 243312.51 121.66 ethane 22.43 30.063 6.743 0.208 28.15 246578.86 123.29 propane 17.96 44.092 7.919 0.244 33.06 289574.55 144.79 isobutane 372 58.118 2.162 0.067 9.02 79058.37 _ 39.53 n-butane 7.25 58.118 4.214 0.130 17.59 154078.81 77.04 isopentane 1.90 72.114 1.370 0.042 5.72 50103.43 25.05 n-pentane 1.67 72.114 1.204 0.037 5.03 44038.28 22.02 cyclopentane 0.51 70.13 0.358 0.011 1.49 13078.81 6.54 n-Hexane 0.37 86.18 0.319 0.0098 1.33 11660.11 _ _ 5.83 cyclohexane 84.16 0.000 0.000 0.00 0.00 0.00 Other hexanes 86.18 0.000 0.000 0.00 0.00 0.00 heptanes 0.23 100.21 0.230 0.007 0.96 8428.17 4.21 methylcyclohexane 98.19 0.000 0.000 0.00 0.00 0.00 224-TMP 0.01 114.23 0.011 0.0004 0.05 417.71 0.21 Benzene 0.06 78.12 0.047 0.0014 0.20 1713.99 0.86 Toluene 0.11 92.15 0.101 0.0031 0.42 3706.66 1.85 Ethylbenzene 0.00 106.17 0.001 0.00003 0.00 34.94 0.02 Xylenes 0.01 106.17 0.006 0.0002 0.02 217.41 0.11 C8+Heavies 0.07 253.8909286 0.178 0.005 0.74 6498.89 3.25 VOC mass frac 0.558 Total VOC(Uncontrolled) 331.31 Notes Mole%and MW of gas are based on stream values predicted in HYSYS model Emissions are based on assuming 5%downtime for the VRU I calculated the average MW of C8+based on the average MW on the analysis for the gas. 15WF0366.CP1 123/9D9F Thirteen low-pressure(LP)separators controlled by eight enclosed flares during VRU downtime.Each 009 flare has a minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust low-pressure separator gas during VRU downtime. Manufacturer Cimarron Model Serial Number Gas Heating Value 1827.92 Btu/scf Throughput 25333.23468 MMBtu/yr VRU Information-NOT APPLICABLE.VRU IS PART OF THE PROCESS Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup J Flare 'Overall Control 95.00%' Combustion emission factor source: CDPHE Memo 0.00 jIb NOX/lb VOC 0.01 Ilb CO/lb VOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 47811 lb/MMscf 2390.5 lb/MMscf 331.3 tpy 16.6 tpy HYSYS Model Nox 0.0037 lb Nox/lb VOC 0.0037 lb Nox/Ib VOC 1.3 tpy 1.3 tpy CDPHE Memo CO 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC 3.2 tpy 3.2 tpy CDPHE Memo Benzene 123.67 lb/MMscf 6.1836 lb/MMscf 1714 lb/yr 86 lb/yr HYSYS Model n-Hexane 841.34 lb/MMscf 42.067 lb/MMscf 11660 lb/yr 583 lb/yr HYSYS Model Toluene 267.45 lb/MMscf 13.373 lb/MMscf 3707 lb/yr 185 lb/yr HYSYS Model Ethylbenzene 2.5212 lb/MMscf 0.1261 lb/MMscf 35 lb/yr 2 lb/yr HYSYS Model Xylenes 15.687 lb/MMscf 0.7844 lb/MMscf 217 lb/yr 11 lb/yr HYSYS Model 224-TMP 30.140 lb/MMscf 1.5070 lb/MMscf 418 lb/yr 21 lb/yr HYSYS Model 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 This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVIl.B.2 15WE0366.CP1 E0366.CP 1 123/9D9F Two(2)vapor recovery towers(VRTs)controlled by eight enclosed flares during VRU downtime.Each 009 flare has a minimum control efficiency of 95%. Equipment Description This source vents natural gas from: vapor recovery towers(VRTS)during VRU downtime Emissions from this source are: routed to a flare 'Natural gas venting from vapor recovery towers(VRTS)during VRU downtime.Emissions from this source are routed to a flare. Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=O*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-mot)at 60F and 1 atm Throughput(O) 1.7082 MMscf/yr 195 scf/hr MW 42.7014 Ib/lb-mol 0.00468 MMscf/d mole% MW lbx/lbmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 1.42 44.01 0.625 0.015 0.32 2816.69 1.41 N2 0.02 28.013 0.006 0.000 0.00 25.25, 0.01 methane 13.11 16.041 2.103 0.049 1.08 9478.37 4.74 ethane 25.19 30.063 7.573 0.177 3.90 34131.86 17.07 propane 30.72 44.092 13.545 0.317 6.97 61049.28 30.52 isobutane 6.96 58.118 4.045 0.095 2.08 18231.37 9.12 n-butane 13.66 58.118 7.939 0.186 4.08 35781.69_ 17.89 isopentane 3.54 72.114 2.553 0.060 1.31 11505.95 5.75 n-pentane 3.05 72.114 2.199 0.052 1.13 9913.32 4.96 cyclopentane 0.90 70.13 0.631 0.015 0.32 2844.76 1.42 n-Hexane 0.64 86.18 0.552 0.0129 0.28 2485.91 1.24 cyclohexane 84.16 0.000 0.000 0.00 0.00 0.00 Other hexanes 86.18 0.000 0.000 0.00 0.00_ 0.00 heptanes 0.38 100.21 0.381 0.009 0.20 1716.30_ 0.86 methylcyclohexane 98.19 0.000 0.000 0.00 0.00 0.00 224-TMP 0.02 114.23 0.023 0.001 0.01 102.97 0.05 Benzene 0.11 78.12 0.086 0.0020 0.04 387.31 0.19 Toluene 0.17 92.15 0.157 0.0037 0.08 706.06 0.35 Ethylbenzene 0.00 106.17 0.000 0.0000 0.00 0.00 0.00 Xylenes 0.02 106.17 0.021 0.0005 0.01 95.70 0.05 C8+Heavies 010 263.517 0.264 0.006 0.14 1187.70 0.59 VOC mass frac 0.759 Total VOC(Uncontrolled) 73.00 Notes Mole%and MW of gas are based on stream values predicted in HYSYS model Emissions are based on assuming 5%downtime for the VRU I calculated the average MW of C8+based on the average MW on the analysis for the gas. 15WE0366.CP1 123/9D9F Two(2)vapor recovery towers(VRTs)controlled by eight enclosed flares during VRU downtime.Each 009 flare has a minimum control efficiency of 95%. Flaring Information Equipment Description Flare to combust VRT separator gas during VRU downtime. Manufacturer Cimarron Model Serial Number Gas Heating Value 2392.22 Btu/scf Throughput 4086.390204 MMBtu/yr VRU Information-NOT APPLICABLE.VRU IS PART OF THE PROCESS Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup I Flare Overall Control 95.00 Combustion emission factor source: CDPHE memo 0.0037 jIb NOX/Ib VOC 0.0094 IIb CO/lb VOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 85475 lb/MMscf 4273.7 lb/MMscf 73.0 tpy 3.7 tpy HYSYS Model Nox 0.0037 lb Nox/Ib VOC 0.0037 lb Nox/Ib VOC 0.3 tpy 0.3 tpy CDPHE Memo CO 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC 0.7 tpy 0.7 tpy CDPHE Memo Benzene 226.73 lb/MMscf 11.337 lb/MMscf 387 lb/yr 19 lb/yr HYSYS Model n-Hexane 1455.3 lb/MMscf 72.764 lb/MMscf 2486 lb/yr 124 lb/yr HYSYS Model Toluene 413.34 lb/MMscf 20.667 lb/MMscf 706 lb/yr 35 lb/yr HYSYS Model Ethylbenzene 0.000 lb/MMscf 0.0000 lb/MMscf 0 lb/yr 0 lb/yr HYSYS Model Xylenes 56.026 lb/MMscf 2.8013 lb/MMscf 96 lb/yr 5 lb/yr HYSYS Model 224-TMP 60.280 lb/MMscf 3.0140 lb/MMscf 103 lb/yr 5 lb/yr HYSYS Model 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 This separator is subject to Reg 7,Section XVII.G.and control requirements of Reg 7,Section XVII.B.2 15 W E0366.CP 1 123/909F Thirteen low-pressure(LP)separators and two(2)vapor recovery towers(VRTs)controlled by eight 009 enclosed flares.Each flare has a minimum control efficiency of 95%. Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 133286 lb/MMscf 6664 lb/MMscf 404.3 tpy 20.2 tpy HYSYS Model Nox 0.0037 lb Nox/Ib VOC 0.0037 lb Nox/lb VOC 1.6 tpy 1.6 tpy CDPHE Memo CO 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC 3.9 tpy 3.9 tpy CDPHE Memo Benzene 350.41 lb/MMscf 17.520 lb/MMscf 2,101 lb/yr 105 lb/yr HYSYS Model n-Hexane 2296.6 lb/MMscf 114.83 lb/MMscf 14,146 lb/yr 707 lb/yr HYSYS Model Toluene 680.79 lb/MMscf 34.040 lb/MMscf 4,413 lb/yr 221 lb/yr HYSYS Model Ethylbenzene 2.5212 lb/MMscf 0.1261 lb/MMscf 35 lb/yr 2 lb/yr HYSYS Model Xylenes 71.714 lb/MMscf 3.5857 lb/MMscf 313 lb/yr 16 lb/yr HYSYS Model 224-TMP 90.420 lb/MMscf 4.5210 lb/MMscf 521 lb/yr 26 lb/yr HYSYS Model 15WE0366.CP1 123/9D9F AIRS(County/Plant)123/9D9F Permit No.15W E0366 Date 6/2/2015 Controlled Controlled Actual Requested NCRP= Emissions Emissions CM. reportable Point# SCC Pollutant or CAS Uncontrolled Emission Factor Emisison Factor Source (tpy)* (tpy)' PTE(tpy)' Eff% 7 VOC 6.9027 lb/1000 gallons AP-42 5.6 112.3 95% Yes Benzene 0.0187 lb/1000 gallons AP-42 30 609 95% Yes n-Hexane 0.1254 lb/1000 gallons AP-42 204 4,081 95% Yes 006 40600132 Toluene 0.0366 lb/1000 gallons AP-42 60 1,192 95% Yes Ethylbenzene 0.0008 lb/1000 gallons AP-42 1 26 95% No Xylenes I 0.0041 lb/1000 gallons AP-42 7 132 95% No 224-Trimethylpentane 0.0041 lb/1000 gallons AP-42 7 132 95% No VOC 6.238 lb/1000 gallons CDPHE 3 60.9 95% Yes 007 40400315 Benzene 0.167 lb/1000 gallons CDPHE 163 3255 95% Yes n-Hexane 0.524 lb/1000 gallons CDPHE 512 10,230 95% Yes VOC 58.295 lb/1000 gallons HYSYS 47.4 948.7 95% Yes NOx 0.0037 lb/lb VOC CDPHE Memo 3.6 3.6 0% Yes CO 0.0094 lb/lb VOC CDPHE Memo 9.0 9.0 0% Yes Benzene 0.1585 lb/1000 gallons HYSYS 258 5,158 95% Yes 008 40400311 n-Hexane 1.0558 lb/1000 gallons HYSYS 1,718 34,365 95% Yes Toluene 0.3086 lb/1000 gallons HYSYS 502 10,045 95% Yes Ethylbenzene 0.0049 lb/1000 gallons HYSYS 8 159 95% No Xylenes I 0.0347 lb/1000 gallons HYSYS 57 1,130 95% Yes 224-Trimethylpentane 0.0373 lb/1000 gallons HYSYS 61 1,214 95% Yes VOC 133286 lb/MMscf HYSYS Model 20.2 404.3 95% Yes NOx 0.0037 lb Nox/Ib VOC CDPHE Memo 1.6 1.6 0% Yes CO 0.0094 lb CO/lb VOC CDPHE Memo 3.9 3.9 0% Yes Benzene 350.41 lb/MMscf HYSYS Model 105 2101 95% Yes 009 31000205 n-Hexane 2296.6 lb/MMscf HYSYS Model 707 14146 95% Yes Toluene 680.79 lb/MMscf HYSYS Model 221 4413 95% Yes Ethylbenzene 2.5212 lb/MMscf HYSYS Model 2 35 95% No Xylenes I 71.714 lb/MMscf HYSYS Model 16 313 95% Yes 224-Tnmethylpentane 90.420 lb/MMscf HYSYS Model 26 521 95% Yes o -"I0) L.d 0 0 0 0 0 w •cu = 8 c co ,n S - CD - O - .� - .� - y a v - O ar — O Z M M M _ d T E U U R a ^C a C ^C C W b4 N N N N • n R ❑ C Q Q 0 0 Q o < 7 ai a% SC .7 w .- > > b � � o a ❑ ❑ ❑ ❑ ❑ W U ° = c 0 0 0 v U- _O C. > co c O L > O. ,C�. 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Source Name: Five Rivers K07,K08,K09 Econode Emissions Source AIRS ID2: N/A/ / Wells Services by this Storage Tank or Tank Battery (E&P Sites Only) API Number Name of Well Newly Reported Well 05-123-39463 FIVE RIVERS K09-62-1HN 05-123-39464 FIVE RIVERS K09-63-1HN 05-123-39465 FIVE RIVERS K09-63HN 05-123-39483 FIVE RIVERS K09-64-1HN 05- 123-39476 FIVE RIVERS K09-65-1HN 05-123-39479 FIVE RIVERS K09-66-1AHN 05-123-39482 FIVE RIVERS K09-66-1HN 05-123-39480 FIVE RIVERS K09-67-1HN - ❑ - ❑ Footnotes: 1 Attach this addendum to associated APEN foul'when needed to report additional wells. 2 If this is a newly report source that has not been assigned an AIRS ID by the APCD, enter N/A Form APCD-212 APEN-Addendum Condensate Tanks 2.6.15 co O r^ 04 U N Z Z 4 W L G o ° °O c ° 0) 0 00 k 0 a O v 3 > y csd o a.) 0 Lo a G. � � � 0 ca y 0 ca N C ^p IZZ N U L y, N N N y a: c ad in E roc -o W �° c '5 arnaz ^ h Q+ O y =y.] 'V V N W O N N 7 - O O C. Q a DD E f ' M c0 aE. 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