The URL can be used to link to this page

Browse Search

Home My WebLink About20161413.tiff A CDPHE COLORADO II Co '✓ Department of Public ...° Health Er Environment Dedicated to protecting and improving the health and environment of the people of Colorado RECEIVED Weld County - Clerk to the Board APR 2 5 2016 1150 O St PO Box 758 WELD COUNTY Greeley, CO 80632 COMMISSIONERS April 20, 2016 Dear Sir or Madam: On April 27, 2016, the Air Pollution Control Division will begin a 30-day public notice period for Noble Energy, Inc. - Klingenberg C20-780. 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, E fg Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure 2016-1413 4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe ( k r , o' John W. Hickenlooper, Governor I Larry Wolk, ,MSPH Executive Director and Chief Medical Officer f1( .. . ?Ltitl ?t14/62-{A) e--e--- ckd ) VL-' 174.-o 7- 7A O21- A CDPHE Air Pollution Control Division CO c` Notice of a Proposed Project or Activity Warranting Public Comment Website Title: Noble Energy, Inc. - Klingenberg C20-780 - Weld County Notice Period Begins: April 27, 2016 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: Klingenberg C20-780 Oil and gas exploration and production facility SESW Sec 20 T4 R64W Weld County The proposed project or activity is as follows: Source proposes to operate an oil and gas exploration and 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): • 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 16WE0087 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 COLORADO 1 r . �caie�,a cm�naaaoi "' Construction Permit C Air Pollution Control Division Permit number: 16WE0087 Issuance: 1 Date issued: Issued to: Noble Energy, Inc. Facility Name: Klingenberg C20-780 Plant AIRS ID: 123/9E46 Physical Location: SESW Section 20,Township 4, Range 64W County: Weld County General Description: Oil and gas exploration and production facility Equipment or activity subject to this permit: Facility AIRS Equipment Point Equipment Description ID Three (3) 300 bbl above ground atmospheric fixed roof condensate Tank Battery 001 storage tanks controlled by enclosed flares. Each flare has a minimum control efficiency of 95%. Produced One (1) 300 bbl above ground fixed roof produced water storage tank Water 002 controlled by enclosed flares. Each flare has a minimum control efficiency of 95%. LP &r VRT Up to one low-pressure (LP) separator and up to one (1) vapor recovery VOC Burners 004 tower (VRT) controlled by enclosed flares. Each flare has a minimum control 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 the specific 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 of the latter of commencement of operation or issuance of this permit, by submitting a Notice of Startup form to the Division for the equipment covered by this permit. The Notice of Startup form may be downloaded online at www.colorado.gov/pacific/cdphe/other-air-permittin-- notices. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation Number 3, Part B, Section III.G.1. and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) of the latter of commencement of operation or issuance of this permit, compliance with the conditions contained in this permit shall be Storage Tank version Syn Minor N13-' Page 1 of 12 dffioRi ion. Itg. the owner or operator's responsibility to self-certify cop he ."' •ns. F.1 e to demonstrate compliance within 180 days may result in revocation of the permit. A self certification form and guidance on how to self-certify compliance as required by this permit may be obtained online at www.colorado.Qov/pacific/cdphe/air-permit-self-certification. (Regulation Number 3, Part B, Section 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. (Regulation Number 3, Part B, Section III.F.4.) 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. (Regulation Number 3, Part B, Section III.E.) 5. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 6. Emissions of air pollutants shall not exceed the following limitations. (Regulation Number 3, Part B, Section II.A.4.) Annual Limits: Facility AIRS Tons per Year Emission Equipment ID Point PM2.5 NO), VOC CO Type Tank Battery 001 --- 1.0 Point Produced Water 002 --- --- 0.1 --- Point LP a VRT VOC 004 3.4 Point Burners Note: See "Notes to Permit Holder" for information on emission factors and methods used to calculate limits. Compliance with the annual limits, for both criteria and hazardous air pollutants, 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 actual emissions each month and keep a compliance record on site or at a local field office with site responsibility for Division review. 7. The emission points in the table below shall be operated and maintained with the emissions control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit. (Regulation Number 3, Part B, Section III.E.) Facility AIRS Control Device Pollutants Equipment ID Point Controlled Tank Battery 001 Enclosed Flare VOC COP COLORADO Co Air Pollution Control Division ^a m ,bt :n b Hr rn-ment Page 2 of 12 0 A Jr.! ' Water Enclosed Flare VOC LP a VRT VOC 004 Enclosed Flare VOC Burners PROCESS LIMITATIONS AND RECORDS 8. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Regulation Number 3, Part B, II.A.4.) Process Limits Facility AIRS Process Parameter Annual Limit Equipment ID Point Tank Battery 001 Condensate Throughput 16,000 BBL Produced 002 Produced Water Throughput 20,000 BBL Water LP a VRT VOC 004 Condensate Throughput 16,000 BBL Burners The owner or operator shall monitor monthly process rates based on the calendar month. Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 9. The permit number and ten digit AIRS ID number assigned by the Division (e.g. 123/4567/001) shall be marked on the subject equipment for ease of identification. (Regulation Number 3, Part B, Section II I.E.) (State only enforceable) 10. 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. a 4.) 11. This source is subject to the odor requirements of Regulation Number 2. (State only enforceable) 12. AIRS ID 001: This source is subject to Regulation Number 7, Section XII. The operator shall comply with all applicable requirements of Section XII and, specifically, shall: • Comply with the recordkeeping, monitoring, reporting and emission control requirements for condensate storage tanks; and . • Ensure that the combustion device controlling emissions from this storage tank 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. (Regulation Number 7, Section XII.C.) (State only enforceable) * CDPHE COLORADO CO Air Pollution Control Division P-,men;ef-Abtr-,-PaIirt BFmironmPnt Page 3 of 12 13. p . I 0 a 0 • T - flare( ; covered by this permit is subject to Regulation No. 7, ectio II. er iv'"ions e 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. 14. AIRS ID 001: 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 * CDFHE COLORADO O Air Pollution Control Division , :r-mF._„ ,ni._ ., n E^shorn-anr Page 4 of 12 het= r v ble emiions are present for a period of at least one (1) minute in ,. te-ma inut-. . 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 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. 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 CDPHE COLORADO CO s Air Pollution Control Division „onar-men..,; ,-,,vc?ment Page 5 of 12 A •- �� 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. 15. AIRS ID 004: The separation equipment, including low pressure separators and vapor recovery towers, 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. OPERATING £t MAINTENANCE REQUIREMENTS 16. 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 the O&M plan are subject to Division approval prior to implementation. (Regulation Number 3, Part B, Section III.G.7.) 4 CDPHE COLORADO tirc + + Air Pollution Control Division ^.vrorment Page 6 of 12 Fp IIII A A COMA SG , D PG Initial Testing Requirements 17. AIRS ID 001: The owner or operator shall demonstrate compliance with opacity standards, using EPA Reference Method 22, 40 C.F.R. Part 60, Appendix A, 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 minute in any fifteen minute period during normal operation. (Regulation Number 7, Sections XVII.B.2. and XVII.A.16) 18. AIRS ID 004: The operator shall complete initial site specific extended gas analyses of the gas vented from the low pressure separators and of gas vented from the VRTs 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 lb/bbl condensate) 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 19. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Regulation Number 3, Part A, II.C.) • 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 (NOr) 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. • Whenever there is a change in the owner or operator of any facility, process, or activity; or • Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or • Whenever a permit limitation must be modified; or • No later than 30 days before the existing APEN expires. 20. 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 COPHE COLORADO Co Air Pollution Control Division DP;:a,me Phr e nfr r.,,i✓onment Page 7 of 12 + +iti . y lax 'on hat inc ses the potential to emit above the applicable Federal progr hr d re a 1 eview 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 Number 3, Parts C and D). GENERAL TERMS AND CONDITIONS 21. 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 Number 3, Part B, Section II.B. upon a request for transfer of ownership and the submittal of a revised APEN and the required fee. 22. 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 Number 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. 23. 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. 24. 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. 25. 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. 26. 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. 27. 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 4, CDPtiE COLORADO Air Pollution Control Division -eparme .:fri h onrn=nt Page 8 of 12 i110 A r t E }•inen Permit History Issuance Date Description Issuance 1 This Issuance Issued to Noble Energy, Inc. 4 CDPHE COLORADO CO 11 Air Pollution Control Division 1 ;e,1.men:nr P.ihl-.-22ii I a 21 E^sronment Page 9 of 12 q No -a:I--r th • this • it issuance: 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. (Regulation Number 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: https://www.colorado.gov/pacific/cdphe/aqcc-regs 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? (lb/yr) Benzene 71432 74 No 4 n-Hexane 110543 714 Yes 36 001 Toluene 108883 123 No 6 Ethylbenzene 100414 4 No 0.2 Xylenes 1330207 47 No 2 Benzene 71432 140 No 7 002 n-Hexane 110543 440 Yes 22 Benzene 71432 271 Yes 14 004 n-Hexane 110543 2,560 Yes 128 Toluene 108883 465 Yes 23 Note: All non-criteria reportable pollutants in the table above with uncontrolled emission rates above 250 pounds per year (lb/yr) are reportable and may result in annual emission fees based on the most recent Air Pollution Emission Notice. 5) The emission levels contained in this permit are based on the following emission factors: Point 001: Uncontrolled Controlled Emission Factors Emission Factors CAS# Pollutant lb/bbl lb/bbl Source N0x 0.0090 0.0090 CDPHE CO 0.0229 0.0229 CDPHE CDPHE. [ COLORADO O +1.. Air Pollution Control Division epzrm `r,M n h zr nenent Page 10 of 12 iik controlled Controlled mission Factors Emission Factors CAS# Pollutant lb/bbl lb/bbl Source _ VOC 2.4402 0.1220 HYSYS n-Hexane 0.0446 2.2 x 10-3 HYSYS 71432 Benzene 0.0046 2.3 x 10-4 HYSYS 108883 Toluene 0.0077 3.8 x 10-4 HYSYS 100414 Ethylbenzene 0.0002 1.1 x 10-5 HYSYS 1330207 Xytenes 0.0030 1.5 x 10-4 HYSYS 2,2,4- 540841 Trimethylpentane 0.0016 7.9 x 10"5 HYSYS Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%. Point 002: Uncontrolled Controlled lb/BBL Produced lb/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 004: Weight Emission Emission Fraction Weight Factors Factors of LP Fraction Uncontrolled Controlled Separator of VRT lb/bbl lb/bbl Pollutant Gas (%) Gas (%) condensate condensate Source NOx (lb NOx/lb VOC) --- --- 0.0037 0.0037 CDPHE Memo CO (lb CO/lb VOC) --- --- 0.0094 0.0094 CDPHE Memo VOC 54.2 74.0 8.4435 0.4222 HYSYS Model Benzene 0.11 0.14 0.0170 0.0008 HYSYS Model Toluene 0.19 0.25 0.0290 0.0015 HYSYS Model n-hexane 1.03 1.40 0.1600 0.0080 HYSYS Model 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 flow. 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 1 CDPHE COLORADO co f Air Pollution Control Division Ceparme,:.ofn1bli-1-'.eai,,&r.vIrortment Page 11 of 12 JeRA . Operating Permit Synthetic Minor Source of: VOC 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 cLHE COLORADO co ' Air Pollution Control Division m h e^or,n-pnr Page 12 of 12 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 02/23/2016 Application Date: 12/07/2015 Facility Identifiers Permit No. 16WE0087 Potentially located in ozone nonattainment area AIRS County# 123 'Weld Facility# 9E46 Facility Type: exploration and production facility 2 Located in the 8-hour non-attainment area? O True Minor Synthetic Minor for: r4•1'. VOC r NOx r CO Administrative Information Company Name: Noble Energy Inc. Source Name: Klingenberg C20-780 Source Location: SESW Section 20, Township 4, Range 64W SIC: 1311 Address 1: Noble Energy Inc. Mailing Address 2: 1625 Broadway, Suite 2200 Address ty,State Zip: Denver, CO 80202 Name: Jaclyn Schaffner Person To Phone: 720-587-2326 Contact Fax: 303-228-4280 Email: iaclyn.schaffnerPnblenergy.com Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the Klingenberg C20-780, located in the SESW Section 20, Township 4, Range 64W,Weld County, Colorado. Point Name Type Control Action 001 Tank Battery Condensate Tanks Flare Newly reported source 002 Produced Water Tanks Flare Newly reported source Water LP &VRT 004 VOC Separator Venting Flare Newly reported source Burners *Point 003 is the condensate loadout which is categorically permit exempt since the throughput is less than 16,308 bbl/yr. *Points 005 and 006 are each 24 hp engines that are permit exempt Three (3) 300 bbl above ground atmospheric fixed roof condensate storage tanks controlled 001 by enclosed flares. Each flare has a minimum control efficiency of 95%. Requsted Throughput 16000 bbl Control Flare Efficiency 95.00%I 0.8969 0.49105275 Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 2.4402 lb/bbl 19.5 tpy 1.0 tpy HYSYS Benzene 0.0046 lb/bbl 74 lb/yr 4 lb/yr HYSYS n-Hexane 0.0446 lb/bbl 714 lb/yr 36 lb/yr HYSYS Toluene 0.0077 lb/bbl 123 lb/yr 6 lb/yr HYSYS Ethylbenze 0.0002 lb/bbl 4 lb/yr 0 lb/yr HYSYS Xylenes 0.0030 lb/bbl 47 lb/yr 2 lb/yr HYSYS 224-TMP 0.0016 Ib/bbl 25 lb/yr 1 lb/yr HYSYS Nox 0.0037 lb/lb VOC 0.1 tpy 0.1 tpy CDPHE Memc CO 0.0094 lb/lb VOC 0.2 tpy 0.2 tpy CDPHE Memc 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 6- New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons (471 bbl) NSPS 0000: 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 16WE0087.CP1.xlsm 123/9E46 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. 16WE0087.CP1.xlsm 123/9E46 One (1) 300 bbl above ground fixed roof produced water storage tank controlled by 002 enclosed flares. Each flare has a minimum control efficiency of 95%. Emissions Calculations Requsted Throughput 20000 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 2.6 tpy 0.1 tpy CDPHE Benzene 0.007 lb/bbl 140 lb/yr 7 lb/yr CDPHE n-Hexane 0.022 lb/bbl 440 lb/yr 22 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 The tanks are not subject since actual uncontrolled emissions are less than 6 tpy. 16WE0087.CP1.xlsm 123/9E46 One low-pressure separator and one vapor recovery tower controlled by two enclosed flares during VRU 004 downtime.Each 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(Q) 1.282245 MMscf/yr 146.375 scf/hr MW 34.36 Ib/Ib-mol 0.003513 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0.00 CO2 2.80 44.01 1.232 0.036 0.48 4169.09 2.08 N2 0.00 28.013 0.000 0.000 0.00 0.00 0.00 methane 31.17 16.041 5.000 0.146 1.93 16916.09 8.46 ethane 31.61 30.063 9.503 0.277 3.67 32150.57 16.08 propane 18.05 44.092 7.959 0.232 3.07 26925.81 13.46 isobutane 4.63 58.118 2.691 0.078 1.04 9103.82 4.55 n-butane 6.10 58.118 3.545 0.103 1.37 11994.23 6.00 isopentane 2.42 72.114 1.745 0.051 0.67 5904.28 2.95 n-pentane 1.36 72.114 0.981 0.029 0.38 3318.11 1.66 cyclopentane 0.83 70.13 0.582 0.017 0.22 1969.31 0.98 n-Hexane 0.41 86.18 0.353 0.0103 0.14 1195.42 0.60 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 0.34 100.21 0.341 0.010 0.13 1152.71 0.58 methylcyclohexane 98.19 0.000 0.000 0.00 0.00 0.00 224-TMP 0.01 114.23 0.011 0.0003 0.00 38.65 0.02 Benzene 0.05 78.12 0.039 0.0011 0.02 132.15 0.07 Toluene 0.07 92.15 0.065 0.0019 0.02 218.24 0.11 Ethylbenzene 0.00 106.17 0.000 0.0000 0.00 0.00 0.00 Xylenes 0.03 106.17 0.032 0.0009 0.01 107.76 0.05 C8+Heavies 0.13 216.3687692 0.281 0.008 0.11 951.63 0.48 VOC mass fract 0.542 Total VOC(Uncontrolled) 31.51 • Notes Mole%and MW of gas are based on stream values for stream labeled"Vapors to VRU/Comb"predicted in HYSYS model Emissions are based on assuming 100%of the stream is routed to flare even though the site is equipped with a VRU. I calculated the average MW of C8+based on the average MW on the analysis for the gas. 16 W E0087.CP1.xlsm 123/9546 One low-pressure separator and one vapor recovery tower controlled by two enclosed flares during VRU 004 downtime. Each 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 2122.94 Btu/scf Throughput 2722.1292 MMBtu/yr VRU Information -NOT APPLICABLE. NOT CLAIMING ANY VRU UPTIME EVEN THOUGH SITE IS EQUIPPED WITH A VI 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 Ilb CO/lb VOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Er VOC 49142 lb/MMscf 2457.10 Ib/MMscf 31.5 tpy Nox 0.0037 lb Nox/lb VOC 0.0037 lb Nox/lb VOC 0.1 tpy CO 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC 0.3 tpy Benzene 103.06 lb/MMscf 5.1530 lb/MMscf 132 lb/yr n-Hexane 932.29 lb/MMscf 46.615 lb/MMscf 1195 lb/yr Toluene 170.20 lb/MMscf 8.5099 Ib/MMscf 218 lb/yr Ethylbenzene 0.000 lb/MMscf 0.0000 lb/MMscf 0 lb/yr Xylenes 84.040 lb/MMscf 4.2020 lb/MMscf 108 lb/yr 224-TMP 30.140 lb/MMscf 1.5070 Ib/MMscf 39 lb/yr 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 oth( 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 One vapor recovery tower controlled by two enclosed flares during VRU downtime. Each flare has a 004 minimum control efficiency of 95%. Equipment Description This source vents natural gas from: a VRT during VRU downtime Emissions from this source are: routed to a flare Natural gas venting from a VRT 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(Q) 0.844975 MMscf/yr 96.45833333 scf/hr MW 43.69 Ib/Ib-mol 0.002315 MMscf/d mole% MW Ibx/Ibmol mass fraction lb/hr lb/yr tpy Helium 0.00 4.0026 0.000 0.000 0.00 0.00 0. CO2 1.65 44.01 0.726 0.017 0.18 1618.97 0. N2 0.00 28.013 0.000 0.000 0.00 0.00 0. methane 8.18 16.041 1.312 0.030 0.33 2925.43 1. ethane 31.00 30.063 9.320 0.213 2.37 20777.76 10. propane 29.12 44.092 12.840 0.294 3.27 28625.68 14. isobutane 8.50 58.118 4.940 0.113 1.26 11013.73 5. n-butane 11.36 58.118 6.602 0.151 1.68 14719.52 7. isopentane 4.52 72.114 3.260 0.075 0.83 7267.13 3. n-pentane 2.49 72.114 1.796 0.041 0.46 4003.35 2. cyclopentane 1.46 70.13 1.024 0.023 0.26 2282.77 1. n-Hexane 0.71 86.18 0.612 0.0140 0.16 1364.17 0. cyclohexane 84.16 0.000 0.000 0.00 0.00 0. Other hexanes 86.18 0.000 0.000 0.00 0.00 0. heptanes 0.55 100.21 0.551 0.013 0.14 1228.79 0. methylcyclohexane 98.19 0.000 0.000 0.00 0.00 0. 224-TM P 0.02 114.23 0.023 0.0005 0.01 50.93 0. Benzene 0.08 78.12 0.062 0.0014 0.02 139.33 0. Toluene 0.12 92.15 0.111 0.0025 0.03 246.54 0. Ethylbenzene 0.00 106.17 0.000 0.0000 0.00 0.00 0. Xylenes 0.04 106.17 0.042 0.0010 0.01 94.68 0. C8+Heavies 0.19. 247.2703158 0.470 0.011 0.12 1047.44 0. VOC mass fraci 0.740 Total VOC(Uncontrolled) 36. Notes Mole % and MW of gas are based on stream values for stream labeled "Vapors toVRTVRU/Comb" predicted in HYSYS model Emissions are based on assuming 100% of the stream is routed to flare even though the site is equipped with a VRU. I calculated the average MW of C8+ based on the average MW on the analysis for the gas. One vapor recovery tower controlled by two enclosed flares during VRU downtime. Each flare has a 004 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 2122.94 Btu/scf Throughput 1793.831227 MMBtu/yr VRU Information -NOT APPLICABLE. NOT CLAIMING ANY VRU UPTIME EVEN THOUGH SITE IS EQUIPPED WITH A VI Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup J Flare Overall Control 95.00% Combustion emission factor source: CDPHE Memo 0.0037 Ilb NOX/Ib VOC 0.0094 [lb CO/lb VOC Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Er VOC 85309 lb/MMscf 4265.5 lb/MMscf 36.0 tpy Nox 0.0037 lb Nox/lb VOC 0.0037 lb Nox/lb VOC 0.1 tpy CO 0.0094 lb CO/lb VOC 0.0094 lb CO/lb VOC 0.3 tpy Benzene 164.90 lb/MMscf 8.2449 lb/MMscf 139 lb/yr n-Hexane 1614.5 lb/MMscf 80.723 lb/MMscf 1364 lb/yr Toluene 291.77 lb/MMscf 14.588 lb/MMscf 247 lb/yr Ethylbenzene 0.000 lb/MMscf 0.0000 lb/MMscf 0 lb/yr Xylenes 112.05 lb/MMscf 5.6026 lb/MMscf 95 lb/yr 224-TMP 60.280 lb/MMscf 3.0140 lb/MMscf 51 lb/yr 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 othe 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 LA 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 One(1)low-pressure(LP)separator and one(1)vapor recovery tower(VRT)controlled by two 004 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 8.4435 lb/bbl condensate 0.4222 lb/bbl condens 67.5 tpy 3.4 tpy HYSYS Model Nox 0.0037 lb Nox/lb VOC 0.0037 lb Nox/lb 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 0.0170 lb/bbl condensate 0.0008 lb/bbl condens 271 lb/yr 14 lb/yr HYSYS Model n-Hexane 0.1600 lb/bbl condensate 0.0080 lb/bbl condens 2560 lb/yr 128 lb/yr HYSYS Model Toluene 0.0290 lb/bbl condensate 0.0015 lb/bbl condens 465 lb/yr 23 lb/yr HYSYS Model Ethylbenzene 0.0000 lb/bbl condensate 0.0000 lb/bbl condens 0 lb/yr 0 lb/yr HYSYS Model Xylenes 0.0127 lb/bbl condensate 0.0006 lb/bbl condens 202 lb/yr 10 lb/yr HYSYS Model 224-TMP 0.0056 lb/bbl condensate 0.0003 lb/bbl condens 90 lb/yr 4 lb/yr HYSYS Model Total throughput 16000.0 bbl condensate/yr Technical Notes: In the draft permit,I required a flow meter to determine actual process flow and for calculating emissions.Noble provided comments back requesting to remove the flow metering requirement due to the lower PTE for this site.Typically,for a LP separator and VRT,the Division would require a flow meter for on- going compliance.Since this site is being permitted assuming all emissions are routed to flare(the site is equipped with a VRU but process limits and emissions limits are based on 100%of the streams going to flare)and since,at 100%,the uncontrolled emissions from the LP separator and VRT are less than 100 tpy, the Division agrees to using a less stringent compliance demonstration which is to correlate to condensate throughput.I removed the flow metering requirements and instead tied emissions to the condensate throughput for the site. 16WE0087.CP1.xlsm 123/9D9F o ° �°�' 0) et 0 Z Z > o o h o �, O a 3 >-, a c Lac � � � t .I , c se V \ ❑•.U+ ®® 40 TO .° _ of MM K1 = k ❑ R N C. .b > U Z O y N N Ncn H s° s E 7°> w o Wo COa � � � EI °' c c) a) C. x y' ,' 0.' 6, U sa C Q N t �'! `� co, co co C ,0 y o 0.. Fa •T aJ m aJ H ! .Mi mi x c� a 3 v 3 - c o s y a sF a, > �;s — Cj A x ° c w e •F•� c c c,_f �co E ° ZI „ _ O C C U O -= . X .. N `n 4. LTa v , _^S . _ CO04 o L. W I® o❑❑ o ff o 0 I l i N W -I c O w U 0y ^C y4. vs To U .C' E an 'O N m ;," F' oo o o m �� ad a. s E 4. o x .O y O A ca = s s u' s o W a) a ea v s 0 ip ; �, o. E g = C7 d 5 5 a) w c .O W v G o Ca ^I ^A o a y E a o o m E e = 'a .,5., o o c E o o •N Z vi a, s p O U N .0 4 �? a, °' k E u E c o et Cj E `� c j el c o ¢ of s..i c v o E W o s a> m ° :=1- s E Q.' Z ., a.� Oo o U U .� V .`� . 0. i CL C1 Q u O O o v L W d W > o C U v p b A ,L, Z 'E O •v - U A = cn c w V A, = A ,-, 0 c o E vC c v1 o E C° c.)i O 0. o 7 3 a : :° •+„ 0 Cn a.) U CO a o •0 ...r = o ..4z C 0 u, 'o aL' c. a a `c° . ¢ o if: o w E L U aii o w o C. 0 o Z _ O G b0 Q m ,--, L L CO Vj 0 ^.O C O a T �, •'^r1'.; v O A O >L„ �'- CO w R. y V y CC •U aJ . yp W 4 • O T O O L O" O > .� O a M d p i E G. E". L •• U o .. LT Ud �°� u � W t� LUdvA Lz. dCn d d • w o V W e a a w = ° E � 'o ei z U O - a°o EE c 0 w ti o U GJ W 0 C / C0 C0O .0 C OU - vs C co O _ _ 0 o A I 04 v aU v U U Z ZC a. >,w U 3 • .`4 0 0 0 0 O _ u c p a�'i api v O.W FW, ? Z ¢ r`, u; o et 0 O V] p : ai g ❑ g ❑ ❑ Q d G U N a }`U� L. U O O 4. O N ❑ �'i O v' 0 N ti.., # ® ❑ ❑ ❑ ❑ ' .=! . c o0 0 . CZ c v, .. 0 O as c� ,o ° o y ZZono c O CO o ..v.• - •E w 3 ❑❑ U i a� u cd p o oq C7 _> A-w 'O N o Q •.U.0 CD C O O P. ≥> ti U O •CO y CO >, Q .•. .O O O N 7 OCip 7 O > E _ .. •O .. ,-i d sO N N oo E a" O A I a;-, �. U V = c cz C'? a? G .M-i ct 7 0o 04 v'°i N a EEn En a 0 W is w 1 a y W ❑ as n CO P O M E 0 U y bD cn • ' 0 U O U hi N OM En '7 0 N up a) E ° L Y' O -0 O W .23 W [� O O O •Z}, O a U Ltl U U C 0 [0 U •• i U c . 0 U „may T O pQy U U N P. O a cC cd a7 C p s. a7 ,�' .� Z V] W N E E N ❑ ®® ro U A .y p �. O rW� C L4 -ci to O ? O A H O O N a) CO C V E~ 0 ,moo 0 Lt, ... 0 O - p C bD (.. �.'. U O ca P J '•C T V1 0 .... CO L. O W J r� a' �ctl c�0O ca 6 �+�, COy O 0 a> Z '1 O• a O0 a�0J CO L .0 -0 '0 0 Y n Al_ , ° LL e E ,, o •Y . o c...) p M@ �~••� O bT0 a 0 .C O .0 co N C E CO _ o [;] 00 0 O d °� O 0 0 C e _ F". N 0 y 0O U E O �; .. .. O H = O '=' O U O _ O a) _ .0 O` y N 7 _, c6 a'O U E .OL CC p Z a�"i ci U ° o r O e O ti E ¢ CO c w c C7 v' L c u,a3 Z .C:n^> o .. m ® _C CID L. E- as C . R; , C 0 ...� O K w >,^ a s.. p , V7 h g v tO z w ^el cz � OU 0 ,.- a CO o °" b > o v = 3 ac s a U F7 a, = o o ® V o a; n I 0 x = x Pi «t 0 ,n > T >, 4-4 •� Ft •u e"e a C� ca y o tr. c p...) arCO - - CO o o E. G. •x y H N (2 .� Z .. , A ti ti a o d w m • it L." .. .. 0eij C 4) U O Yr bD C 0 C. ay 0 a) a) C U us <0.) U .`1 U > U "" O O CO L VI P. C ¢ d co ca •E °> -' s° •-, C7 5 c°C c °' O p, V > w O V] Z� Q A O I Z Z a -0 o ti I ° E'"' a' o T'�. I Q ° '.' 00 i17'W oct 00 0 ._ •o f a) dCO - © a © a ¢ • p (1.) c H ti O o d cn - .. CO s o d 7 o E cn E c E o '≥t c y o 0 o a) °o° Q x N �. y • v 0 r° CO w u as . - ♦ ♦ C V c o . . ca A ., —. 4. o cn P. W v1 a cn L° H -.. C7 v) UH H v) �" _ y. o a0 N NNNNNN vi N V I- 1- r d• 1- r V N o r (0 W [z. x ¢ T, d Q Q Q Q Q4. a c ~ H bA 5 m C v] P'-• is.--) c. U? UJ U1 U? Vl 0 o s. vP 5 C.) vi) C.) up v) vD vD vz up a) Q.C - H = o Q U V W x x x x x x x p Ct o o �a O ❑ -O U O 0 9 a -O..V7 a) 'i7 CC r O ro L tj U L, d] • f; 4. Ct R. o - Ui. ca cu d E - vI °�° c i G a s w cc cz y •• yO„ v t. H g O O O O O O N O . •^, (a) .d •b c. ti ^y II a) O O\ N O O O O O O ) C ,� w CC a D o 0 0 0 0 0 0 0 0 0 1, W F, O O .O. C a) b0 N U .C 4" A 'in •— f., OT. OT. yam, c o D ., j c.) o cn O p i O O Q C .r C R O V v1 O o Q E z N , F W o h V c � o c 3 ti U : �•� a v - a) O O Cr cu >col~ u O 3 .� c a y\ - ° MI a o b Fp^.7 ',F o 0 O Cr' v, O y >' C4 cn .s; V) N U O O y V) cn 2 cn a es a ... 0 y vi ° U U I y ° Ocr, c c c V) O H o 0 0 o M o , = . 0 ®® �' W pCq O I a) °� �. ai ti O O O O O O et y o rn it C/1 u .a a> O� Q R d O .O. 3 N -p N a O 0 U O 0.) O C O 'O a U -O W.n a) a U L i a) CD 6� y' oA O r- - E •�. N c C H o 0 1 y N 0 o °o y o `.. N v c >, y ai R 9 O s. Q 0 8 r~U- to - •� u NN O `o •4 >� o �" . ca w ct 5 O rn O.=v 4 cA cs 0 c•, w v c v E E ao p ❑ 2 U .� v1 Q ❑ a) s.. W N ® o -°a o U -O ca — b4 zr E 1 q <v . m w co ° N a[i • vj °c 3 °° ^a a C7 " n o c = Q '� o ^d a� o a°)i 3 N C O o� 3 a'a' o 0 on 7,1) 0) o d u c N - , = U d ^_ O „ , o CC x 2 p C w .o_ c ` W O R -, ti Z o o > > o N sca. _p W Q ... Q, .. U y w �, C. = v a) c, x ° °� a' c .- .4 $o cc O . ',- 0 v R ° o° R. cc E aU ❑ �U o " a o r, 5 C ❑ �, pp O y, O O Q) 7 O C c^`a Q o ea o w c U H > U Q .^. c a? d Ca 9 C o A o •U ,• o h U �-' o C ., ca O .o i�j".�' 'p L". �' h a7 C O s"' .. 0- a.) ti F-1 y ® ❑ O - E .E W o L U R Ti, W 0 c v F." °c. in T o ,o . Li '' cp bD HOi eLc -^ O aC N O ^ y cn a1 o 3 a, gyy E r — 9 0 L N N(".., c0 N o `••J y0 X O ...1.' C .d+ L NI /-� C R '.. U > R N Lra iO 'y W - L r F�1 a) Ca a o O �v ,p ❑ F) m c- a.) es 0 O V V 7 O R N O .7.1 m r: c N CGSC+ as a V. Z . Lc o ^ a o Z O C� k. ❑ ca _ G 6) y C ct .� ,^ .^ ¢rim-, . h 3 U `o O ` U U V ." z '-' d O ._. L?. ¢ U1 .. �, .O • ' u • .�`�, ^.� O .O '� O '� '� Wes' cC w Fri.' a3 �_ > •E > 0 > O O 0 .° 0 O O1 5 ° O .2 C!1 U Y i' as ° �' .� Q Q _N ._ Z/] cC •U o •.. a°i U A o o v u cid 9, E R ❑ o p Uca . da00 c N s. nhiH O v4. aC a U 3 O an CC) G" I 0' W� o i, m c cea. .. o s 2 ao `'" s •- -O r .. 7 v, N N a V° V) I a <. d ¢ 0 m > 'b y O +O-' .O Iy a? M O CT 7 l� O N !. O C� „N,, N O U U W 'O •� O R W O 7 O O O O 0 7 0 O 's.., v, Ey �. ai Q G O 5 r c�3 O © a O O O O O O O y p a1 R r-� y Q = y C :: c� r-. �N U y,.i o ^ O N O O O O O O O el .r"-, p Ia+ Oy .� ono O H p ap v, p O Q EEC O CC -!V. x CD v •N c.,0 > U Ct 0 CO D ice., ro • . • y • '' w o E c Z . I W aJ -E O O -o eu — V o ca y C F�'I ►� c��a•o �' cO. o sue. Rs -• O 4 q ;d cC a b° ,n p Q x °� 'e-',, 15 o vti > O y y )- co e, as 1 0 ^ •° et C.. VD cn W c0a •C U a i ! ! IU .I rn x UOO9 -' 4. O U o 0 O x li) I o R . _ ar T o 3 o • C O o a V o. c o c.) o y a) o '0 a°, W E y >C -E.," a� o o a ..� o ° —. C° N y m 0 W 4.1 F. o ° _ /gam +. a. Q ,.. ,L 7:+ y ,..c y �+ N 0 7 ar �L 0.4 O w a ❑ ❑ 3 c a ® N ; - ', V_ Vi V) V) V5 va 3 c a.) I- o 0 0 0 0 c o N ° O a 3 >,zZZzz ° c ° o00cn a- 3 aJ y s- 0 ❑ L C. d vi ^ O aJ \ ❑®❑®® W >'•9 2 C ^ M M M ..'i z ........ K ❑ d C •- > U Z O aL' r:r "` N N N VD ...::l r 7. .°o s E > 4" -0 wo aC' ,..,a) p.,`" c, 0, rnZ, - Q w 0 W �. ' ' ' a O' x v//' _ i i i o .- o° a dN � ��c o0o C '' `° y ° 3 -to 3 C o L ai o.yy a' > rn • C O L L E C a a.) Z N H 'O y \ L 0 3 1, w [� I®❑®❑❑ aXi M aJ o z ct En O ' c w OU 0 ^O d y R• C•.) .L. F v -0 T ¢ , _ CL .-' ,- a) d aJ 4ay co C m 7 A aJ a °-'.- CC _I CA — L E: co A on v ae b 0 a w d o x Ti E =I L. y .- a A m ro Cse. `�W on y d d d s a' �° �I s C: > U E- `� y' m .. 0 o aai ad y o a o I C4` A U et a A C C 5 N @ 0* ,b U >,S 3 o 0, F O 0. i �I .O d to v a`°i a) v c o 0 w E 'a „ o A 'Mn ,. Ca CI.) c d a c a 4 a� c o a' -. •C - G W d s 3 o j .I V d o x c W .. o •o @ E G "' ae L E e) �o o z d y ►.] Z •x 0 o >, c1 -0 cz i o : '16 ti:, E w i i N s c Q l Ci U_ O W o U 0.U P a c a m C, U o00 o U .I p w a y, a ¢ v o C 7 Lc' L C..) Z a, ^" > U 0 0 r4 A O o 0 .0 i� V ° = A Z Z 6 E R c0i O° o 3 c a. o o p v U C o a� I M o y — G — p d O. 0 C CZ 0 '° — 4. ^ y E d 0 z s :9 ° 0, w° �, p > v A ° E� 0 ._ A. 0 0 0 v w 0 0 co ° tt L L A U a+ 7 o z .0 0 En ° 0 o _ y C Q Z d N ^ L L 0, T F A p •� O U O c b0 G W .� L V U - a.. 4- y O E O O., C °YJ > •zt y O Ow M a1 p 4, E G. tl. it .E '3 ar 3 a' o r .1 t U d -V O W L U d � A w d v) Q d W > y c. a = y a - E 0 A, tu Z c' A C 'e0 E E 0 ° W O o o w ,- iG 0 0 . . °U — m -CID o 0 _ FD y y a" y s s N w >, U 1 0 0 U U Z Z o o a� on 0 c .0 ,-, c o ac' ai' aci 0w, 0.w. 4,9 3 Z ¢� En rn o aLa ao v >: c4 0 O . p C ❑ �" in c 'u L® ❑ ❑ ❑ ❑ Q + 9 ° .. c, H sr, ea o a o z w L \ O F 8 ®❑ ❑ O ¢at L o L.; w o s, y " Cn a° 00 0 3 C.• '0 3 F 0 :? c� O d z aN�, o Ea z 3 U � z o CU C7 00 A N w 0 ❑ tti O`•' O N au •v 'Di, -0 N ez Q 8 •0 v o c °' w A P-, C2r M 3 o OD N 9 �y- � EAI o X uy E El - 00 In N 0 W O_ E C .!✓ W L O 41V . E N O N G R > j .° 0 co)0 70 0 i", 'CL O dJ .L' ,b [^ M ° y 'O C a N U ° L L O Z W O ,7-° ›-' c, g .9 5 " y 'Oa' U C U y 4 �' U U R. .o _ N j ac s,. �a y 3 4' C o o CA a y 'v Z W N E E El El m m L ro r, a f...._.4 h c U LT 7 7 \ 0 00 cUa i 7 ❑ A O Ot d N z z ° � o U G a' � — Ha � an ^ 0) C7 o y' o R C `0 W in 0 �' U `T7 0 C h' L d O y w c a o 3 o a o y E z �.• �_ C -� >, >, y t� r... w r—! OZ � � � o w r� 4� M c y E T o ° A. o F > L DI C.) p O O ^ O C O i C. G co o U 0 O K Y...i coCA O O N °YJ m '_' N .7. C E- L. y C N dr O a) ,.. a) N •� .. > bA M C W N = � CZd� c, 42U a L. E0 � U ' V] �1 •� F o �ZW �x ak � o o Q ® F ti c.> w >, W N C O CO W CO `m is i �, ? E- [� _ O '"- 0.) Z W = O V R o C •o y o b o p, i""▪i a;..; .o to U .•a a .. W Cn ° i v) y c ® y 3 3 ° x ° 8 M C G p O Al �' a o a Z ur' c >, >, i :° y °Oo •°. m O 0Gc h eCa 1 C Q Q ° W as ¢ U a> U 6 E- 8 x v E� N A. �, Z .•, A ti ►� ea iw °y � •cOOa y w ° w •a .� a oc /^�' H:y .�. .. .. CLi ° �'. °0. ° °0. Ca' ° CC bD L '7 , o L ca m •� „ ,•C52 0 �/ 7 co E 0 0 0 0 a. V] y .. O V1 ,. Z M Q • 6, 0 >, C' O ¢ U Q M N •O 0+� 0 0 U N er �j '� .°° C th Z w p sU aA 0 — 0 •0 cct ' 0 ¢ CaaQ .t 0 .o a 7, 3 0 • v• U Cn0 2 o w ,- 0 •N Y ♦ ♦ ♦ ♦ c 7 0 sC N CLe ° ca p•, w rn a o) u°. E� .- 3 C7 C.1 a H H- z H A 0 O N �+ C O-i W �0. y O r _ H b0 c0 N co 0kr Q Q �.' ci ,Z U U U w W C Uo A WeUn cio O. W a a o 0. G 0. tU. y c a. Q - O Q ro r: _ v] Q Q Q s., 'U m -U X c V V 'Vi R •* U Up 00 t6 o.�v C W ^0 r a. E-, CC'S ,- ° ° C7 5 en" W U o o [-I 6, c �, ipn .> cu p 0 0. , O C 0 10 0 Fo N U LR, O a, .y a' ,0 a-) a, 7-2 a, i R o o o y ., c O. • F m o G i m = a) •' a s o 0 o G. W H a y w 0 0 Yom- aa�i = o a UE� E 0 0 •— 'o= •o a c)a �cc° ro a) °� a >, >, et P. O � J a, O �, '^ 3 E 10' O O _� 1 O. O o n� Co) 4L. . 'fl O O N N N R C 7,M I I .. p 0 y o v, ..- ' O N 'C r -'y.., ,p,7. .. CJ a R a A C ti o a, 0 U O z.-. O, �U, x x at oap a S rt • = '° a' M a Y R ., Clr �n .O. 'O O a ca �cz ^ 'w'' R•'e 0 '3 �� a)bk, G b0 m O U U .�� J a, O� Q .C .a O •� N g O0. D 1.F C rOi, O If') ,� ,� Q. ^O 6, 6? � w. ❑ .0 U O O� z ?'' N 0 S. r., a) G, aa) ❑ i ..RO -, ° .N c c'4 = c o C' ° ❑ ° © c d o ° q, O Y. C .-. "a R c4 0 O O O a ,� .N m ..I O •E-. O O .. O o � N - o a� c u, o. d UH - d 0 $ O o 0 a ,_ `u' - o o a > �0.) O N O L a' c W w ��° aa o v et F r C w •U � T, R Q V E a R W bp a ``" V o W O RZEn 0 y w p R �, L v, 8 ^a d O p ti ti ru B a o o c c 9 ,p C y IS 7" "o O C ° N� a, c o .� s L a, CC c N 4-, O N �] 3 y y O OD w y0 R Q ct V G 'O p O � a!-. r O L' oQ A u c...)0 o _ ° U a) s. c 0 ti Z c - ° cv ,wet.. y w - u O O 4J U C y C 3CZ R o E y U .= c U c d a F.. 6 N 'v c O T 0 O U 1,1 in O .m Q' _V. r p . U C. = °c•^° U H > U CZ i p d i 5 .5 c o ti I I —L" �. N y o• u y i i. O. In C �^.• O 0 _ O i ar O .--1 i^ .y CA N 4y >+ Lyi �' O rr m W U bD .-1 M o e••:. _ �0 o °� C� L ,� y : c A- _ .� ° R ae o U O ._G O �, L /R-� >,_ U > U W 1-r-'' .OR C. 'y, t... ,... �y 0 m U e-ia w u o a = = Z — ni u O .� ❑ O L. 'JLO v, •O y A cc O O Q p �Oi U y ,� L p c.)a. y y .o ^per O Z - a, --- R r-i7.1 — W >, W u O, o f cn a °° a, : u o •.. U V a, °� A O a; — u2-4, c f t cn R d.., t �, > - o •`, 3 ❑ - o CID L. > ❑ ° -a y o a, ,o r3 ¢ .N 3 a y c 0 C R u co U •F co w v a, c, s. d Ra Cl, i--, a) � ^o ° h.-.4 y O cxC U C > 3 O — N N N "O 4� Er L al) > U O R 'a `*a. �-� `� O '"'' O a^ :. C" O N .r N Z . �z O ° a>i _ Tr O W ^v .O R I›. ea O N C.' O C ,N W o 4 " L .. L ;, o C O O O t-+ 7-.--- 0.. ° 7 i. �..i h Q a, au, O O O r`i, O CS R v, 6 0 C y, O .O ._ 0 c v a -F ti v y y o 0 R Q ¢ :: �, a o ao 0 O 74 ..i o o v 2 c w e iP y UCY s wa) 7 U _y •y 'C '7 "� N Ca ."� V U cC CO 3 C OCJ o N.. O �I , rN ti 0^ ro o ?' ro v, ° O C d 6 Fes, CJ ,x °' •m y O '�' j O ,-.6 ti Cl a, u O C .. c.r, o •,.., P. P+ � —' ate'' b=A O U > rn O N � W.I [ U a) a) 0 �' C %j L P. v� m c •C U ar .y o .° U - W a x U aai 'y 0 Z m a, Cl---..,m_, E `-° o Q s� y a O O c . °- aj_ a, I J +. _ In . c r-, c °o. 0 .a^, a 0 v o i o .a) o . Ha X ' c ( a)i-c1-&41I cz 5) liii) W C . a W . r-, ❑ u3 F. t ❑ N v ,.,_ __.QC VI Cn U] V) V) °' O Ii oab � ai = �' T v A. � � � v CO 4.0 ❑ _ ra E W y m cn n o . p C a N N N N y 3 •2 — _ o — 0 0 0 ° ° a ° A 4' E ? R o-o o a 0 0 y O En G L F. S7 G .� 4' G —iL `_ ED L O G' G O G .� a=+ O - b0 a) ,--4 L.] �4-. .. 10. :::,i rCu a 3 • a on °� W a a rn co) s °D w° ° B = o s-. 3 ,,, = x b° o o r� r CL cGc u O v� GL a 0 0) t. P c? 0 O "O O T T �, V CU Ci) r :''' to ❑ ❑ > a) o E o W 3 .. % en 6. o •- o 3 0 0 O C 1• .! Hifi34 A ^" 3 0 .cACd N a) C L ❑ a) O A 5 > l MI L s. N p Q •,P. >a is m v ° ° °) ca ?� w B o > w- -o E a n a o U m ..0 i' _o .0 6, C/ o _ O E C U W 0 " o G V y o a) U N C o a°i cu � o —, c "" 0 a, o d o C o 0 0 cfla s L ° r� E U U A ,, •a = U ° a Q ^o at a) .m- -o '6.▪ a u a ° c..) o a ,✓ ro pWp� p m W ,-. E ¢ :. G 'r' -o W 0 a) A o°n c0p W ° °' °' N cn 5* = L �Or G G W .m m G L A 0 a' a m U U d v i F p � `G° o U Q c el cz aci a�i v v 0 3 a o o oc°n w 4 o p F p CG fx ❑ ❑ G4 ❑ ❑ y c 1.0 Li.* .. U r 3 0a) 0. O .T. 0 y N > 5 cO w ��Q.. co �T y a x N ,--I �, ❑ ❑ W N •a ❑ U 4l 0 t41) G cd ,`,'I \N 00 p O OL y 0 a /1 CI o - A 0 N 7 CV 0 a) F. N'�•+ G Q O _ W ~ O 00 N . O N ° v 0 r4 O F © M b N O .n..� ii .�0., , W O U o O ) T G N l� OM rn T L. O 0 U Q o., -p G O -o O o ® 'a pp W C/) O a o a ' k •n' N 0 t V V ¢ U U a> U0 .o •- o N aai = o _' [-i a w 2 U NE a c r vl i HC e N o .c O ° -S) Z p N o x Cr, zO. IN Z O V) 0 0 s0. ' cc� G 3 N m T"7 �y 1G41 7. 1-1 rA o p o 0 • Q .'' < ti `' W ' >'h. @ ;� O 5 N b0 p O O OD O C .0- M c r,.i = O N eal U zt .0.+ .�.+^ a Y G Z F., i. a r • Q a > ? L ^ o a a F a a 4) O 0 0. T0 4 CZ 0 w ^ 0 a > - O °� '-' v Z U a o s s ce o c° G -, .. x o o 0 Q .,v.,,, Z rY, .fir A 'n ti p c°p �� V 0 E C�. ^p v i '' aCi °' p el i, Q n o ° 0 v m a F ° Q .. y a) - A 6) 0 6 N C in .. C. 04 U G C -Fa O O U cn aa. 0 a' O. c°i I' U E �d E E eu a c.., o Q V ° r 6. ~ C -o U o e o ' > Pi ca 0 'z. ,. G .ti O —. O O a) •— •a s 3 R 6. ca `4' .o I Z Z U o ° o I al o o5 c Or ,-i >+ o 3 d U Q M a "' as •3 o x _. E a. o i 0. o ffl ZW o 9 `- to o — o G - I' a) 3 0 aaa) E o -Cc E- ° p a E o O y L G 41 Co.C a) U a W ris a CD Q ❑ ® ❑ ❑ ❑ ® °" j ® w O u O _ \ O 0 O F. eV 7 U U U U U 0 E ^ �n m 0 s0 V] Cr W L4 CO CS eC CO cC y H p CU co . ;--,• < x = U U U U U s. a w° n m w W m ^° ,:: A G 0 0 ^° 0 0 p U °O° C. Li. W U U U W W W W W 6, 'c) • o O v uu c b o• c a aa) ` . 0 o . is 5.! C7 0 p u aroi CZ V G dp .. M N �O co, O O O O �, cu U F C C M C O O O o O O S. i - •C c m w o o a.- O y " II L U V y a, °23 0 6' y R E .y °) W H c,91F to °� p G Ca O C y to N -° 0 7 rn y E !,� ° :a °' c ° ao ° 0. u Q p" o Q o L ^ `c '� `� Z .. N i., .L A 4' �'"' V O2 >, N � en N O 0 N aJ O _ _ 44• ` 0 y 7 E 0 O O O O O O O O . i O _O a `- O U to 5 _ = _ r:+ -,- et 4:. 4; o ° v F• 'c o -o c FOf ° '� L▪r �v�i C,ru p,, in a en yr ,� N C `�` Pr w U O� ca O --" v i.n N b 0 N U1 N y - -a+ .� o 3 II o c c m ---� 00 c � a° � o Q a v Z .cz cU � O 0 ❑ Q+ o m •• 5 '2 o � Q. at a" Fr c o _ CO O E •1:. • Cr v y y o p i W o i-, - o O .��, --i 0 o o o a) aa: < 0 0 ° 0 r c▪o' 0 0 N m .. v 0 0 U• � �. C U O .7 — O G i U .'i NN O t C ® 0 w CD ' 0 W E ^ 7 O L V CD 4. co o c, 00 x ❑ `� w ? C nv .Sw va : V) I Q v LL W a i > 0 aJ -0 C v) c-, 0 Z ,O o o c.. I^ w w c.. w a, a) . O 0 >~ v cn ❑ d co y o y o c u s s u u u u u .p s •▪`—e O (� u y o s o '� E ,l ,4 E E E E E 'O 4 b z, a) N •v .-, y o E 3 A 0 0 a . a J .s7 .s.7 .s-1 c 0 cc ti Z o �r '^" p w 3 0 0 N = E u xz a W 0 o m Qy Y O N Q •R O p S W.3 R }l. 6 ��yy eci co,U O 7 0 CO m V 0 0 0 ... P. "U 0 _ a U E y F p n L — ^ ^o ,.--. ~° E c 0 , W 0 d p __ Z U G U F-' Q U 0 0 0 N O, 0 0000 V7 U U 0 ea d o II " 0 r o o ., c� o o - Ct 0 ,. o, �'' i ® CC 0 L. V O O O O O O ,, L E dc, a O a p Z -F. ,-. U - m o 3 G d > p w � .N li �- U o 70 i 0 W " - y t... ,N-1 Q ,, p• Q O o 0 W o c e o o e o V 6 .° 7� > V o U 0 ? .—' o a 0,,tn In 01 0, 0 , CC N @ G U L Oo. i o. Y ti U ❑ i_ y 0 c C A °a 3 74 — m t.C4 0 a W C Q▪ > = w ,d, cw — ca v s U u 023 _o OU W � .� � u Q W • 0. i • > o h .. > V� ❑ -a 0 = ° y �O E--'" • >> O O 0 >, . - 1. y-0 0• cl, O p y 1 E W '0 O y m a) v C , cA a E U N • a .. u y, o y •v_ > a a .. . O F�1 U a, .U. O 0 't'1 @ O U N m - E O Q ,- O Y pp O O>a", a) y m U 0 U /� Pi y Z U iu .tg'- " 4 a) U a CIO y y .. W • E E u >. 0 0 >~ E , ki � a, s U 1.0 f0 p @ O N O h '. y U p. yu„ L L L L L v -^�'� 1 7 U U ro UCS A o • co w° J u u c i �' LL L; LL LT. Lz, �. E U I u I ' ... I r.o o a; I v) 0 0 r 0 0 J 5 oo 0 H G u u V U 0 ¢ ol . 0 1 p 0 m CG N a°) o ,2 r, s W 6 O O O O N 5 ° 0 O O c m Z o 0 CD •v] d E� Q O U > Z U <D o a > X 0 al 0 U aJ Q W aJ ❑ ❑ Q ® at V) (/) V) Hello