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Home My WebLink About20141754.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH Fk, g o Executive Director and Chief Medical Officer r Dedicated to protecting and improving the health and environment of the people of Colorado 4300 Cherry Creek Dr.S. Laboratory Services Division i876 Denver,Colorado 80246-1530 8100 Lowry Blvd.Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Weld County -Clerk to the Board 1150 O St P° Box'58 RECEIVED Greeley, CO 80632 June 4, 2014 WELD COUNTY Dear Sir or Madam: On June 8,2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC— State Antelope F-30 Production Facility(COGCC #433300), in the'File Greeley Tribune. A copy of this public notice and the public comment packet are enclosed. Thank you for assisting the Division by posting a copy of this public comment packet in your office. Public copies of these documents are required by Colorado Air Quality Control Commission regulations. The packet must be available for public inspection for a period of thirty (30)days from the date the public notice is published. Please send any comment regarding this public notice to the address below. Colorado Dept. of Public Health &Environment APCD-SS-B 1 4300 Cherry Creek Drive South Denver, Colorado 80246-1530 Attention: Clara Gonzales Regards, 4, f1 Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure To jai) Rithiu) Q PLL M1 N-Lf,PPS')Pt,3 2014 1754 9- l'l STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk, MD,MSPH 7-oF coto� Executive Director and Chief Medical Officer ,\ Dedicated to protecting and improving the health and environment of the people of Colorado 4300 Cherry Creek Dr.S. Laboratory Services Division 8V6 / Denver,Colorado 80246-1530 8100 Lowry Blvd. -- Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located in Glendale,Colorado (303)692-3090 of Public Health www.colorado.gov/cdphe and Environment Website Title: Bonanza Creek Energy Operating Company LLC— State Antelope F-30 Production Facility (COGCC#433300)—Weld County Released To: The Greeley Tribune On: June 4, 2014 Published: June 8, 2014 PUBLIC NOTICE OF A PROPOSED PROJECT OR ACTIVITY WARRANTING PUBLIC COMMENT Notice is hereby given that an application for a proposed project or activity has been submitted to the Colorado Air Pollution Control Division for the following source of air pollution: Applicant: Bonanza Creek Energy Operating Company LLC Facility: State Antelope F-30 Production Facility (COGCC#433300) Exploration and Production Facility NWNW, SEC 30, T5N, R62W Weld County The proposed project or activity is as follows: The source proposes to construct a facility that includes 9 condensate storages tanks,2 produced water storage tanks, truck loadout operation, fugitive equipment leaks, emergency flare, 2 high/low pressure separators, and water transfer pneumatic pump. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section IILC due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section IILC.I.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 14WE0012 have been filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are available on the Division's website at www.colorado.gov/cdphe/AirPublicNotices The Division hereby solicits submission of public comment from any interested person concerning the ability of the proposed project or activity to comply with the applicable standards and regulations of the Commission. The Division will receive and consider written public comments for thirty calendar days after the date of this Notice. Any such comment must be submitted in writing to the following addressee: David Thompson Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South, APCD-SS-Bl Denver, Colorado 80246-1530 cdphe.commentsapcd@state.co.us 4 > STATE OF COLORADO COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT 'IV' \' k AIR POLLUTION CONTROL DIVISION ,---� I TELEPHONE: (303)692-3150 .'a *`, \.r/876{- CONSTRUCTION PERMIT PERMIT NO: 14WE0012 Issuance 1 DATE ISSUED: ISSUED TO: Bonanza Creek Energy Operating Company LLC THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS: Oil and gas exploration and production facility known as the State Antelope F-30 Production Facility (COGCC #432809), located in the NWNW Sec 30 T5N R62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Condensate 003 Nine (9) above ground 500 bbl atmospheric condensate storage Tank tank Two (2) above ground 400 bbl and two (2) 60 bbl concrete vaults PW Tanks 004 used to store produced water. Only the 400 bbl tank is controlled by the combustors TL 005 Truck Condensate Loadout FUG 006 Fugitive VOC leak emissions Sep-1, 007 Separator controlled by a flare. Flare has a minimum combustion Sep-2 efficiency of 95%. The flare is enclosed FL-1 008 Separator controlled by an emergency flare. Flare has a minimum combustion efficiency of 95%. The flare is not enclosed P-1 009 One (1) Sandpiper G1F pneumatic pump used for water transfer Point 009: This pump may be replaced with another pump in accordance with the provisions of the Alternate Operating Scenario (AOS) in this permit. 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 AIRS ID: 123/9BDF Page 1 of 14 4 . olor- tDepa en .f P r•li Health and Environment 'it Pollution Control Division b 1. Points 003, ',c t" , 0. I r' - t i Ye.= ii_1:.T nob "k„ e Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, l submittinq a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Point 008: YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after startup by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ap/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 3. Points 003, 004, 005, 006, 007, 009: Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 4. Point 008: Within one hundred and eighty days (180) after startup, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 5. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (Hi) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.) 6. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 7. Point 008: The following information shall be provided to the Division within fifteen (15) days after start-up. • manufacturer • model number • serial number This information shall be included with the Notice of Startup submitted for the equipment. (Reference: Regulation No. 3, Part B, III.E.) 8. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source AIRS ID: 123/9BDF Page 2 of 14 wier olor. Depa en If P li Health and Environment it Pollution Control Division I. EMISSION LIMITATIONS AND RECORDS 9. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility AIRS Tons per Year Equipment ID Point NO, VOC CO Emission Type Condensate 003 11.5 Point Tank PW Tanks 004 0.6 Point TL 005 39.5 Point FUG 006 19.1 Fugitive Sep-1, Sep-2 007 1.0 20.8 5.2 Point FL-1 008 1.7 14.4 9.2 Point P-1 009 0.1 2 1.3 Point See "Notes to Permit Holder"for information on emission factors and methods used to calculate limits. Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0 tpy. Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy. Compliance with the annual limits shall be determined by recording the facility's annual criteria pollutant emissions, (including all HAPs above the de-minimis reporting level) from each emission unit, on a rolling twelve (12) month total. By the end of each month a new twelve-month total shall be calculated based on the previous twelve months' data. The permit holder shall calculate emissions each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. This rolling twelve-month total shall apply to all permitted emission units, requiring an APEN, at this facility. 10. Point 006: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent gas analysis and liquids analyses, as required in the Compliance Testing and Sampling section of this permit. The operator shall maintain records of the results of component counts and sampling events used to calculate actual emissions and the dates that these counts and events were completed. These records shall be provided to the Division upon request. AIRS ID: 123/9BDF Page 3 of 14 Illolor- Depa f P di Health and Environment a'- en "it Pollution Control Division 11. Theemission - >i. r , th .g e -- a .xsh.=, a-daa-, ated aintained 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 Equipment AIRS Control Device Pollutants Controlled ID Point Condensate Tank 003 Enclosed Flare VOC, HAPs PW Tanks 004 Enclosed Flare VOC, HAPs (400 bbl tanks only) Sep-1, Sep-2 007 Enclosed Flare VOC, HAPs FL-1 008 Open Flare VOC, HAPs P-1 009 Enclosed Flare VOC, HAPs PROCESS LIMITATIONS AND RECORDS 12. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits Facility AIRS Point Process Parameter Annual Limit Equipment ID Condensate Tank 003 Condensate Throughput 237250 BBL PW Tanks 004 Produced Water Throughput 91980 BBL TL 005 Oil Loaded 284700 BBL Sep-1, Sep-2 007 Gas Vented from Separator 21.4 MMSCF FL-1 008 Gas Vented from Separator 38.1 MMSCF P-1 009 Natural Gas 5.3 MMSCF Compliance with the annual throughput limits shall be determined on a rolling twelve (12) month total. By the end of each month a new twelve-month total is calculated based on the previous twelve months' data. The permit holder shall calculate throughput each month and keep a compliance record on site or at a local field office with site responsibility, for Division review. STATE AND FEDERAL REGULATORY REQUIREMENTS 13. The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on all applicable equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 14. Visible emissions shall not exceed twenty percent (20%) opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. & 4.) AIRS ID: 123/9BDF Page 4 of 14 olor , , Depa en & P lic Health and Environment Ail it Pollution Control Division 15. This source ' u ct t the requie of Regulation No. 2. (State only enforceable) 16. Point 003: No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30% opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.) 17. Point 003: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. 18. Point 003: This source is subject to the recordkeeping, monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 19. Point 005: This source is located in an ozone non-attainment or attainment-maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 20. Point 005: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 18 (a) and (b) above. The inspections shall occur at least monthly. Each inspection shall be documented in a log available to the Division on request. 21. Point 005: 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. 22. Point 006: This source is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). All condensate collection, storage, processing and handling operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. The operator shall comply with all applicable requirements of Section XII. AIRS ID: 123/9BDF Page 5 of 14 olor.AL Depa ° en .f P •li 1Health and Environment A it Pollution Control Division 23. Point 006: Mi-. , e Ufa !.• n•.9f a+rr-nt or -*nment/maintenance areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for which the area is nonattainment or attainment/maintenance (Reference: Regulation No. 3, Part B, III.D.2.a). This requirement to apply RACT shall be satisfied by installing/implementing the following emission controls: a. Directed Inspection & Maintenance as described below shall satisfy the requirement to apply RACT. i. Auditory/visual/olfactory inspection (AVO) will be performed on a semi-annual basis. The first AVO inspection shall be completed within 180 days of permit issuance. ii. For each leak found in the AVO inspection, a gas detector may be used to determine the size of the leak. The gas detector shall be regularly calibrated. Component leaks greater than 10,000 ppm shall be managed in accordance with Item (vi) below, unless it is unfeasible to make the repair without shutting down the affected operation of the facility. Component leaks less than 10,000 ppm shall not require repair. For such component leaks that require a shutdown to be repaired, repair shall occur during the first shutdown of the affected operation after the leak is discovered. iii. For repair, valves adjacent to the equipment to be repaired will be closed if practicable, minimizing the volume released. iv. Repaired components shall be re-screened using AVO to determine if the leak is repaired. v. The following records shall be maintained for a period of two years: • The name of the site screened via AVO inspection and the name of the inspector. • Components evaluated with the gas detector. • Repair methods applied. • Dates of the AVO inspections, gas detector calibrations, attempted repairs, successful repairs, repair delays, and post- repair screenings. vi. Leaks shall be repaired as soon as practicable, but no later than 15 calendar days after detection, unless it is technically or operationally infeasible to make the repair within 15 calendar days. Records documenting the rationale shall be maintained if it is technically or operationally infeasible to make the repair within 15 calendar days. OPERATING & MAINTENANCE REQUIREMENTS 24. Points 003, 004, 005, 007, 008, 009: 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 AIRS ID: 123/9BDF Page 6 of 14 keg olor. Depar yen f P li Health and Environment ` 'air Pollution Control Division subject to Division rova rio admplementaton. (Refs ce: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 25. Point 006: Within one hundred and eighty days (180) after issuance of this permit, the owner or operator shall complete the initial extended gas analysis of gas samples that are representative of volatile organic compound (VOC) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. The operator shall submit the results of the gas analysis and emission calculations to the Division as part of the self-certification process to ensure compliance with emissions limits. 26. Point 006: Within one hundred and eighty days (180) after issuance of this permit, the operator shall complete a hard count of components at the source and establish the number of components that are operated in "heavy liquid service", "light liquid service", "water/oil service" and "gas service". The operator shall submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. 27. Point 007: The owner or operator shall demonstrate compliance with opacity requirements, using EPA Method 9 to measure opacity from the flare. (Reference: Regulation No. 1, Section II.A.1 & 4) 28. Point 009: The owner or operator shall complete an initial extended gas analysis and submit the results to the Division as part of the self-certification process to ensure compliance with emissions limits. (Reference: Regulation No. 3, Part B, Section III.E.) Periodic Testing Requirements 29. Point 006: On an annual basis, the owner or operator shall complete an extended gas analysis of gas samples that are representative of volatile organic compounds (VOC) and hazardous air pollutants (HAP) that may be released as fugitive emissions. This extended gas analysis shall be used in the compliance demonstration as required in the Emission Limits and Records section of this permit. ALTERNATE OPERATING SCENARIOS 1. Point 009: This pump may be replaced with a like-kind pump in accordance with the requirements of Regulation 3, Part A, Section IV.A and without applying for a revision to this permit or obtaining a new construction permit. A like-kind replacement pump shall be the same make, model and capacity as authorized in this permit. 2. Point 009: The owner or operator shall maintain a log on-site or at a local field office to contemporaneously record the start and stop dates of any pump replacement, the manufacturer, model number, serial number and capacity of the replacement pump. 3. Point 009: All pump replacements installed and operated per the alternate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. AIRS ID: 123/9BDF Page 7 of 14 olor Depa en P li Health and Environment it Pollution Control Division • ADDITIONAL REQUIREMENTS 30. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30`" 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. b. Whenever there is a change in the owner or operator of any facility, process, or activity; or c. Whenever new control equipment is installed, or whenever a different type of control equipment replaces an existing type of control equipment; or d. Whenever a permit limitation must be modified; or e. No later than 30 days before the existing APEN expires. 31. Federal regulatory program requirements (i.e. PSD, NANSR or Title V Operating Permit) shall apply to this source at any such time that this source becomes major solely by virtue of a relaxation in any permit condition. Any relaxation that increases the potential to emit above the applicable Federal program threshold will require a full review of the source as though construction had not yet commenced on the source. The source shall not exceed the Federal program threshold until a permit is granted. (Regulation No. 3 Part D). GENERAL TERMS AND CONDITIONS 32. 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. 33. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section AIRS ID: 123/9BDF Page 8 of 14 olora Depa enr f P lic Health and Environment it Pollution Control Division 41z, tv III.G. Final authonza onad` ono rant- - IL.he o tion or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. 34. This permit is issued in reliance upon the accuracy and completeness of information supplied by the owner or operator and is conditioned upon conduct of the activity, or construction, installation and operation of the source, in accordance with this information and with representations made by the owner or operator or owner or operator's agents. It is valid only for the equipment and operations or activity specifically identified on the permit. 35. Unless specifically stated otherwise, the general and specific conditions contained in this permit have been determined by the APCD to be necessary to assure compliance with the provisions of Section 25-7-114.5(7)(a), C.R.S. 36. Each and every condition of this permit is a material part hereof and is not severable. Any challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit and upon such occurrence, this permit shall be deemed denied ab initio. This permit may be revoked at any time prior to self-certification and final authorization by the Air Pollution Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and regulations of the Air Quality Control Commission (AQCC), including failure to meet any express term or condition of the permit. If the Division denies a permit, conditions imposed upon a permit are contested by the owner or operator, or the Division revokes a permit, the owner or operator of a source may request a hearing before the AQCC for review of the Division's action. 37. Section 25-7-114.7(2)(a), C.R.S. requires that all sources required to file an Air Pollution Emission Notice (APEN) must pay an annual fee to cover the costs of inspections and administration. If a source or activity is to be discontinued, the owner must notify the Division in writing requesting a cancellation of the permit. Upon notification, annual fee billing will terminate. 38. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122 (civil penalties), -122.1 (criminal penalties), C.R.S. By: David Thompson Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BDF Page 9 of 14 . s r`,'n olor. Depa en f P# ell 'Health and Environment � a it Pollution Control Division Notes to Permit Holder " °' - me o""' ' •e an -:' 1) The permit holder is required to pay fees for the processing time for this permit. An invoice for these fees will be issued after the permit is issued. The permit holder shall pay the invoice within 30 days of receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference: Regulation No. 3, Part A, Section VI.B.) 2) The production or raw material processing limits and emission limits contained in this permit are based on the consumption rates requested in the permit application. These limits may be revised upon request of the owner or operator providing there is no exceedance of any specific emission control regulation or any ambient air quality standard. A revised air pollution emission notice (APEN) and complete application form must be submitted with a request for a permit revision. 3) This source is subject to the Common Provisions Regulation Part II, Subpart E, Affirmative Defense Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division of any malfunction condition which causes a violation of any emission limit or limits stated in this permit as soon as possible, but no later than noon of the next working day, followed by written notice to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions Regulation. See: http://www.colorado.gov/cs/Satellite?c=Document C&childpagename=CDPHE- Main%2FDocument C%2FCBONAddLinkView&cid=1251599389641&pagename=CBONWrapper 4) The following emissions of non-criteria reportable air pollutants are estimated based upon the process limits as indicated in this permit. This information is listed to inform the operator of the Division's analysis of the specific compounds emitted if the source(s) operate at the permitted limitations. Uncontrolled Emission Are the Controlled AIRS Rate emissions Emission Rate Point Pollutant CAS# (Ib/yr) reportable? (Ib/yr) 003 Benzene 71432 3321.5 Yes 166.1 003 n-Hexane 110543 22064.2 Yes 1103.2 004 Benzene 71432 643.9 Yes 32.2 004 n-Hexane 110543 2023.6 Yes 101.2 005 Benzene 71432 970 Yes 970 005 n-Hexane 110543 5560.1 Yes 5560.1 005 Toluene 108883 2251.9 Yes 2251.9 005 Xylenes 1330207 1937.1 Yes 1937.1 006 Benzene 71432 202.5 No 202.5 006 n-Hexane 110543 1084.5 Yes 1084.5 006 Toluene 108883 388.6 Yes 388.6 006 Ethylbenzene 100414 79.4 No 79.4 006 Xylenes 1330207 317.9 Yes 317.9 007 Benzene 71432 1861.4 Yes 93.1 007 n-Hexane 110543 11128.8 Yes 556.4 007 Toluene 108883 1352.8 Yes 67.6 AIRS ID: 123/9BDF Page 10 of 14 olor Depa en P P lip Health and Environment " it Pollution Control Division Xti 007 Ethylb4 zene 04004 3. xNoc 7.2 007 Xylenes 1330207 335.7 Yes 16.8 008 Benzene 71432 1256.5 Yes 62.8 008 n-Hexane 110543 7389.9 Yes 369.5 008 Toluene 108883 1741.6 Yes 87.1 008 Ethylbenzene 100414 149.4 No 7.5 008 Xylenes 1330207 362.9 Yes 18.1 009 Benzene 71432 173.3 No 8.7 009 n-Hexane 110543 1019.5 Yes 51 009 Toluene 108883 240.2 No 12 009 Ethylbenzene 100414 20.6 No 1 009 Xylenes 1330207 50.1 No 2.5 5) The emission levels contained in this permit are based on the following emission factors: Point 003: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput VOC 1.94 0.097 Source n-Hexane 0.093 0.0047 Source Benzene 0.014 0.0007 Source Note: The controlled emissions factors for point 002 are based on the flare control efficiency of 95%. Point 004: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL Produced lb/BBL Source Water Throughput Condensate Throughput VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE Note: The controlled emissions factors for point 003 are based on the flare control efficiency of 95%. Point 005: Emission Factors-Uncontrolled AIRS ID: 123/9BDF Page 11 of 14 olor Depa en ef P,•li "Health and Environment A it Pollution Control Division ° Pollutant VOC 0.277 AP-42 Benzene 0.012 (tpy)(wt%)/100 n-Hexane 0.070 (tpy)(wt%)/100 Toluene 0.029 (tpy)(wt%)/100 Xylenes 0.025 (tpy)(wt%)/100 The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95) using the following values: L= 12.46*S*P*M/T S = 0.6 (Submerged loading: dedicated normal service) P (true vapor pressure) =6.88 psia M (vapor molecular weight) = 67.18 Ib/Ib-mol T(temperature of liquid loaded) =64 °R Point 006: Component Gas Service Heavy Oil Light Oil ervi S Water/Oil Service Connectors 2079 953 702 Flanges 94 26 30 Open-ended Lines 64 9 2 Pump Seals 4 0 1 Valves 309 123 82 Other* 148 16 30 VOC Content(wt. fraction) 25.31 99.58 100 Benzene Content(wt. fraction) 0.06 1.23 0.12 Toluene Content(wt. fraction) 0.05 2.85 0.03 Ethylbenzene(wt. fraction) <0.01 0.58 <0.01 Xylenes Content(wt. fraction) 0.02 2.45 <0.01 n-hexane Content(wt. fraction) 0.33 7.04 <0.01 *Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms, drains, dump arms, hatches, instrument meters, polish rods and vents TOC Emission Factors (kg/hr-component): Component Gas Service Heavy Oil Light Oil Water/Oil Service Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04 Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06 Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04 Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05 Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05 Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02 Source: EPA-453/R95-017 AIRS ID: 123/9BDF Page 12 of 14 6. olor Depa en . P, ilic Health and Environment it Pollution Control Division Compliance with e, -len= im(., t it ernonstrat --by using the TOC emission factors fisted in the table above with representative component counts, multiplied by the VOC content from the most recent gas analysis. Point 007: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (%) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 48.73 38948.25 lb/MMscf 1947.41 lb/MMscf Engineering Calculation Benzene 0.1088 86.9832 lb/MMscf 4.3492 lb/MMscf Engineering Calculation Toluene 0.0791 63.2164 lb/MMscf 3.1608 lb/MMscf Engineering Calculation Ethylbenzene 0.0084 6.7232 lb/MMscf 0.3362 lb/MMscf Engineering Calculation Xylenes 0.0196 15.6874 lb/MMscf 0.7844 lb/MMscf Engineering Calculation n-hexane 0.6503 520.0360 lb/MMscf 26.0018 lb/MMscf Engineering Calculation Note: the gas heat content of the flare gas is 1737 Btu/scf Point 008: Weight Emission Factors Emission Factors Pollutant Fraction of Uncontrolled Controlled Source Gas (°/.) NOx --- 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO --- 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 VOC 25.312 15101.50 lb/MMscf 755.075 lb/MMscf Engineering Calculation Benzene 0.0556 32.9794 lb/MMscf 1.6490 lb/MMscf Engineering Calculation Toluene 0.0484 45.7103 lb/MMscf 2.2855 lb/MMscf Engineering Calculation Ethylbenzene 0.0066 3.9218 lb/MMscf 0.1961 lb/MMscf Engineering Calculation Xylenes 0.0161 9.5245 lb/MMscf 0.4762 lb/MMscf Engineering Calculation n-hexane 0.3272 193.9618 lb/MMscf 9.6981 lb/MMscf Engineering Calculation Note: the gas heat content of the emergency flare gas is 1,304 Btu/scf Point 009: Emission Factors- Emission Factors- Uncontrolled Controlled Pollutant lb/MMscf vented lb/MMscf vented Source: NOx 0.068 lb/MMBtu 0.068 lb/MMBtu AP-42 CO 0.37 lb/MMBtu 0.37 lb/MMBtu AP-42 All emission factors VOC 15,102.84 755.14 are based on the displacement equation and the State Antelope K-O- n-Hexane 193.96 9.70 30HNB October 1, 2013 gas analysis. Note: the gas heat content of the flare gas is 1,304 Btu/scf AIRS ID: 123/9BDF Page 13 of 14 +,.LlY.f4Y?.5 olorl Depa en f Pra.li <Health and Environment ` u it Pollution Control Division 6) In accordance with C.R.S. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with this permit is valid for a term of five years from the date it was received by the Division.A revised APEN shall be submitted no later than 30 days before the five-year term expires. Please refer to the most recent annual fee invoice to determine the APEN expiration date for each emissions point associated with this permit. For any questions regarding a specific expiration date call the Division at (303)-692-3150. 7) This facility is classified as follows: Applicable Status Requirement Operating Permit Synthetic Minor Source of: VOC's, HAPs, n-Hexane NANSR Synthetic Minor Source of: VOC's, HAPs, n-Hexane MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.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) An Oil and Gas Industry Construction Permit Self-Certification Form is included with this permit packet. Please use this form to complete the self-certification requirements as specified in the permit conditions. Further guidance on self-certification can be found on our website at: www.colorado.gov/cdphe/oilgasperm its AIRS ID: 123/9BDF Page 14 of 14 Division Information Engineer: David Thompson Control Engineer: Chris Laplante Review Date: 05/12/2014 Application Date: 11/12/2013 Facility Identifiers Permit No. 14WE0012 AIRS County# 123 Weld Facility# 9BDA Facility Type: exploration and production facility ❑Located in the 8-hour non-attainment area? O True Minor 0 Synthetic Minor for: W VOC r NOx r CO Section 01: Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Antelope F-30 Production Facility (COGCC #42 Source Location: NWNW Sec 30 T5N R62W SIC:)311 Address 1: Bonanza Creek Energy Operating Company LLC Mailing Address 2: 410 17th Street. Suite 1500 Address :ity,State Zip: Denver, CO 80202 Name: Peg Young Person To Phone: 720-440-6133 Contact Fax: 720-279-2331 Email: pyoung@BonanzaCrk.com !Section 02: Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Antelope F-30 Production Facility(COGCC #432809), located in the NWNW Sec 30 T5N R62W, Weld County, Colorado. Point Name Type Control 003 Condensate Condensate Tanks Flare Tank 004 PW Tanks Water Tanks Flare 005 TL Loadout None 006 FUG Fugitives Flare 008 FL-1 Separator Venting Flare 007 Sep-1, Sep-2 Separator Venting Flare 009 P-1 Pump Flare 002 Nine(9)above ground 500 bbl atmospheric condensate storage tank Emissions Calculations Pollutant E.F. Source VOC 1.94 lb/bbl E&P TANK 0.097 Benzene 0.014 lb/bbl E&P TANK 0.0007 n-Hexane 0.093 lb/bbl E&P TANK 0.00465 Requsted Throughput 237,250 bbl Control 0 No Control 0 Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 230.1325 tpy 11.506625 tpy Benzene 3321.5 lb/yr 166.075 lb/yr n-Hexane 22064.25 lb/yr 1103.2125 lb/yr Regulatory Review Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A(July, 1992)) in all subsections of Section II. A and B of this regulation. Section II.A.5- :Smokeless Fla or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the co ibr..,tm ortvse gages shall allow v or cause emissions into the atmosphere of any ar pollutant which is in excess of bellirif opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. Regulation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. Regulation 6-New Source Performance Standards NSPS Kb: for storage vessels greater than 19,800 gallons after 7/23/84. This source is not subject because each tank is less than 19,800 gallons (471 bbl) • NSPS 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 not subject to the emission control requirements for condensate tanks since it is located in an attainment area.) XVILC STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is not currently subject to this since actual uncontrolled emissions are less than 20 tpy of VOC.) 003 Two (2) above ground 400 bbl and two (2) 60 bbl concrete vaults used to store produced water. Emissions Calculations Pollutant E.F. Source VOC 0.262 lb/bbl CDPHE 0.0131 Benzene 0.007 lb/bbl CDPHE 0.00035 n-Hexane 0.022 lb/bbl CDPHE 0.0011 Requsted Throughput 919801bb1 4380 Control O No Control ®Flare Pollutant Uncontrolled Emissions Controlled Emissions VOC 12.04938 tpy 0.602469 tpy 0.57378 1.176249 Benzene 643.86 lb/yr 32.193 lb/yr 30.66 n-Hexane 2023.56 lb/yr 101.178 lb/yr 96.36 Regulatory Review Section II.A.1 - Except as provided in paragraphs 2 through 6 below, no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20% opacity. This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes. The approved reference test method for visible emissions measurement is EPA Method 9 (40 CFR, Part 60, Appendix A (July, 1992)) in all subsections of Section II. A and B of this regulation. Section ILA.5 - Smoke. ss Rare at r-Gres s or ihe Sc ushon :a Waste Cases Noowner or operator of a smokeless flare or other flare for the combustion of waste J .sen shaU ;r3rloy.., cause emissions into the atmosphere of any air pollutant which is in excess of 30% op 3cty for a period or periods anci tins more than six minutes in any sixty consecutive rnmuta_s. Regulation 2—Odor Section I.A- No person, wherever located, shall cause or allow the emission of odorous air contaminants from any single source such as to result in detectable odors which are measured in excess of the following limits: For areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the odorous air has been diluted with seven (7) or more volumes of odor free air. 004 Truck Condensate Loadout Calculations AP-42: Chapter 5.2 Equation 1 L= 12.46*S*P*M/T L= loading losses in lb per 1000 gallons loaded S =Saturation Factor P=true vapor pressure of liquid loaded [psia] M = molecular weight of vapors [lb/lb-mole] T=temperature of bulk liquid loaded [deg. R] 1 degree Fahrenheit=460.67 degree Rankine Source 5 0.6 Submerged loading:ded AP-42 P 6.88 psia Sales Oil Analysis M 67 lb/lb-mole AP-42 T 522 deg. R Field Data L 6.60 lb/10^3 gal 2.77E-01 lb/bbl Annual requested Throughput 284700 BBL/yr 11957400 gal/yr Annual requested VOC emissions 78940 lb/yr 39.47 tpy Regulatory Considerations This facility is not condisdered a terminal (in Reg. 7) because average daily throughput will be below 20,000 gallons at 3,956 gallons per day. This facility is not considered a bulk plant(in Reg. 7) because it does not distribute gasoline. NCRPs Component Mass Frac. lb/yr Emission Factor Benzene 0.012288 970.02 0.00340716 lb/bbl n-hexane 0.070434 5560.08 0.019529615 lb/bbl Touene 0.028527 2251.93 0.007909835 lb/bbl Xylenes 0.024539 1937.12 0.006804061 lb/bbl =_ oc, N ry v ry o 0 0 0 o 0 66666 '8 0 P o U� X C y co n • C. Wbo '^ o ,n o 00000oo ~ o04P632 °8 oeJ w „� P .. ry ,^_, a 000 00 u m n 0, 6 o ui .. o ,g •m m 0 0 0 0 0 0 0 6 0 o a " " NON ta w m x• w 12 .-a O LI .. o . m 6 O 0 0 0 0 0 0 0 0 0 0 " o 3 o a• 6 O ry o o m O „ ry .4 4m P. 0 0 0 0 0 0 0 0 0 o O o n PO ? o P N UOa do . N • Cz, „ owl CO n rv ? O P m P Oo O O oo O O oo N .. O O p d o u. 3 6 ai r c b m P o n▪ m P O O ry '' N ry m ti ti O b 6 N b O 0 0 0 0 0 0 n O O o 6 n 6 co " rii F = m ,- , b O P o o ry O O o N ti O O b O O O O o O O ry O O O 7 o 0 d' > O ,,Z, e co o 00o ry o 2 „ o n P ,+i o 6060 000 „ 600 2� N 01 c u c w m ci, - - ,., o 0 0 " 30 o 6 wi n o ry P �, 0 0 0 0 0 0 0 �, o r 3 0 0 0 0 0 0 2 la pi 0 m .. O O m 0 .. .. O CO 0 0 0 o O o P o 0 3'0 0 0 0 0 o U U 2 x o a o_ a '.' .rv. o ° ° ° ° ° ° " 9094 0 0 $ o ooea S- 999 " 07199 " " 009.9. 0 00 0 - 6 0 6 '' 4 _5 c... 0 0 0 0 .o• c 9 m c — e _ a - t 0 0 0 0 6 o 0 0 o 0 0 o E o c u U G 6 0 6 0 a `u'. w o0 So "' o 'no ^ o '" POOP i 2' 8 t 5 e m o m o 0 0 0 0 0 o E A Cr, 6N6m 66 .. n 66 -- 6 m6m ,. mrv .. .. rvn N : Q _ i Q 0 8.L" 8,- ^ '" ins mLx c a in - 8888 '88888888 . 8838888888 H .E p-L Y o W Q a e a o`,222 ,28 `4 ,222372', 31 _ a0 r m6n .. em ,.P , ry .. P ry m .. .. m rn6 m wi 666 on ' — n r . Q o - o o a o v 3 N Q 0 Q .� a. U �, 0 w 2 0 0 a d d _6_T O - T Li- U a .. a a ‘L) n ;Li . n .. U O L cO. C y O 'O a 9 Q J G J u O _ .>_i m G G `^ •n '" Y N M " y N C v a r C v c ~ h ~ U O O Q o i. a E t 2 '� a 2 E c cc ca > E a U a i E a c 0 L O 6 : .LL o u I- >' . 0 8 " o >" 0 o 0 >' c. s c 0 >' n' 0 8 c o 3 43 in o ° = 3 U T.: 3 U o o v •= v u = ry 3 'w 2 o o co LL co = 2 `o zw z v 5 dz 8 2 5 2=° d 8 `rvc E ca H 3 4 55 i- pL 3 2 w ' L � `N. v z gN 007 Separator controlled by a 40'flare stack.Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: gas from low pressure separator Emissions from this source are: routed to a flare Natural gas venting from gas from low pressure separator Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II, Chapter 10-Displacement Equation(10.4-3) Ex=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) 21 MMscf/yr 2442.9 scf/hr 1.82 MMscf/mo MW 30 300 Ib/Ib-mat 0.059 MMscf/d mole% MW lbx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 0 4.0026 0.000 0.000 Helium 0.0 0 0.00 CO2 2.6 44.01 1.144 0.038 CO2 7.4 64610 32.30 N2 0.12 28.013 0.034 0.001 N2 0.2 1898 0.95 methane 44 5737 16.041 7.150 0.236 methane 46.1 403724 201.86 ethane 23.9852 30.063 7.211 0.238 ethane 46.5 407146 203.57 propane 18.2999 44.092 8.0688 0.266 propane 52.0 455599 227.80 isobutane 1.8484 58.118 1.0743 0.035 isobutane 6.9 60657 30.33 n-butane 5.3735 58.118 3.1230 0.103 n-butane 20.1 176337 88.17 isopentane 0.9088 72.114 0.6554 0.022 isopentane 4.2 37005 18.50 n-pentane 1.1402 72.114 0.8222 0.027 n-pentane 5.3 46427 23.21 cyclopentane 0.082 70.13 0.0575 0.002 cyclopentane 0.4 3247 1.62 n-Hexane 0.2287 86.18 0.1971 0.007 n-Hexane 1.3 11129 5.56 cyclohexane 0.0594 84.16 0.0500 0.002 cyclohexane 0.3 2823 1.41 Other hexanes 0.3787 86.18 0.3264 0.011 Other hexanes 2.1 18428 9.21 heptanes 0.1777 100.21 0.1781 0.006 heptanes 1.1 10055 5.03 methylcyclohexane 00452 98.19 0.0444 0.001 methylcyclohexane 0.3 2506 1.25 224-TMP 0 0001 114.23 0.0001 0.000 224-TMP 0.0 6 0.00 Benzene 00422 78.12 0.0330 0.001 Benzene 0.2 1861 0.93 Toluene 0.026 92.15 0.0240 0.001 Toluene 0.2 1353 0.68 Ethylbenzene 0.0024 106.17 0.0025 0.000 Ethylbenzene 0.0 144 0.07 Xylenes 0.0056 106.17 0.0059 0.000 Xylenes 0.0 336 0.17 CB+Heavies 0.0917 10;'755 0.0988 0.003 08+Heavies 0.6 5579 2.79 VOC mass fraction: 0.4872 Total VOC Emissions(Uncontrolled) 416.7 30.300 Notes Mole'2.MW,and mass fractions from State Antelope sample 10/1113 Emissions are based on 8760 hours of operation per year. I calculated the average MW a'084 based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0010-000 Serial Number 21126.20667,20334,20668,20665,20920,20921,20941 Gas Heating Value 1737 Btu/scf Throughput 37171.8 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare Overall Control 95.00% 416.9 20.845 4.169 Combustion emission factor source. AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 1.26 tpy NOX 6.88 tpy CO Emissions Summary 1.3 tpy NOX Uncontrolled/PTE 6.9 tpy CO 416.7 tpy VOC Controlled 20.8 tpy VOC Uncontrolled Controlled Total Total(lb/yr) Reportable? (lb/yr) Benzene 1861 Yes 93 Toluene 1353 Yes 68 Ethylbenzene 144 No 7 Xylenes 336 Yes 17 n-hexane 11129 Yes 556 224-TMP 6 No 0 Regulatory Applicability AQCC Regulation 1 [This source is subject to the opacity requirements for flares in Section II.A 5-'No owner or operator of a A CC Re ulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the AQCC Regulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled NOX 118.116 b/MMscf CO 642.69 b/MMscf VOC 38948.2494 b/MMscf Benzene 86.9832 b/MMscf Toluene 63.2164 b/MMscf Ethylbenzene 6.7232 b/MMscf Xylenes 15.6874 b/MMscf n-Hexane 520.0360 b/MMscf 224-TMP 0.3014 b/MMscf Controlled NOX 118.116 b/MMscf CO 642.69 b/MMscf VOC 1947.4125 b/MMscf Benzene 4.3492 b/MMscf Toluene 3.1608 b/MMscf Ethylbenzene 0.3362 b/MMscf Xylenes 0.7844 b/MMscf n-Hexane 26.0018 b/MMscf 224-TMP 0.0151 b/MMscf 006 Separator controlled by a 40'flare stack. Flare has a minimum combustion efficiency of 95%. The flare is/is not enclosed. Equipment Description This source vents natural gas from: Sales gas routed to a candle stick flare in case of emergency Emissions from this source are: routed to a flare Natural gas venting from Sales gas routed to a candle stick flare in case of emergency.Emissions from this source are routed to a flare. Emission Calculation Method EPA Emission Inventory Improvement Program Publication'Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=Q*MW'Xx/C Ex=emissions of pollutant x Q=Volumetric flow 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) 38 MMscf/yr 4349.3 scf/hr 3.24 MMscf/mo MW 22.500 Ib/Ib-mol 0.104 MMscf/d mole% MW lbx/Ibmol mass fraction E lb/hr lb/yr tpy Helium 001 4.0026 0.000 0.000 Helium 0.0 40 0.02 CO2 216 44.01 0.951 0.042 CO2 10.9 95563 47.78 N2 0 63 28.013 0.176 0.008 N2 2.0 17741 8.87 methane 72 92603 16.041 11.698 0.520 methane 134.2 1175980 587.99 ethane 13.1423 30.063 3.951 0.176 ethane 45.3 397182 198.59 propane 7.2887 44.092 3.2137 0.143 propane 36.9 323069 161.53 isobutane 0.6814 58.118 0.3960 0.018 isobutane 4.5 39811 19.91 n-butane 1.9526 58.118 1.1348 0.050 n-butane 13.0 114080 57.04 isopentane 0.3282 72.114 0.2367 0.011 isopentane 2.7 23793 11.90 n-pentane 0.4119 72.114 0.2970 0.013 n-pentane 3.4 29861 14.93 cyclopentane 0 0292 70.13 0.0205 0.001 cyclopentane 0.2 2059 1.03 n-Hexane 0.0853 86.18 0.0735 0.003 n-Hexane 0.8 7390 3.69 cyclohexane 0.0227 84.16 0.0191 0.001 cyclohexane 0.2 1921 0.96 Other hexanes 0.1409 86.18 0.1214 0.005 Other hexanes 1.4 12207 6.10 heptanes 0.0711 100.21 0.0712 0.003 heptanes 0.8 7163 3.58 methylcyclohexane 0 0188 98.19 0.0185 0.001 methylcyclohexane 0.2 1856 0.93 224-TMP 0 114.23 0.0000 0.000 224-TMP 0.0 0 0.00 Benzene 0.016 78.12 0.0125 0.001 Benzene 0.1 1257 0.63 Toluene 00188 92.15 0.0173 0.001 Toluene 0.2 1742 0.87 Ethylbenzene 0O014 106.17 0.0015 0.000 Ethylbenzene 0.0 149 0.07 Xylenes 0.0034 106.17 0.0036 0.000 Xylenes 0.0 363 0.18 C8+Heavies 0.0479 C antf 0.0860 0.004 CB+Heavies 1.0 8649 4.32 VOC mass fraction: 0.2544 Total VOC Emissions(Uncontrolled) 287.7 22.500 Notes Mole 66.MW,and mass fractions from State Antelope K-O-30HN8 Sales Gas gas analysis 10/1/13. Emissions are based on 8760 hours of operation per year I calculated the average MW of C8+based on the average MW on the analysis for the gas. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Candle Stick Flare Model TBD Serial Number TBD Gas Heating Value 1304 Btu/scf Throughput 49682.4 MMBtu/yr VRU Information Equipment Description Engine to recompress gas to sales line. Make GasJack Model GJ320 Requested Control Efficiency 100.00% Annual Bypass Time 50.00% Backup Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 lb NOX/MMBtu 0.37 lb CO/MMBtu 1.69 tpy NOX 9.19 tpy CO Emissions Summary 1.7 tpy NOX Uncontrolled/PTE 9.2 tpy CO 287.7 tpy VOC Controlled 14.4 tpy VOC Uncontrolled Controlled Total Total(lb/yr) Reportable? (Ib/yr) Benzene 1257 Yes 63 Toluene 1742 Yes 87 Ethylbenzene 149 No 7 Xylenes 363 Yes 18 n-hexane 7390 Yes 369 224-TMP 0 No 0 Regulatory Applicability A CC Re ulation 1 This source is subject to the opacity requirements for flares in Section II A 5'No owner or operator of a 1 A CC Re ulation 2 Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the A CC Re ulation 3 Is public comment Public Comment Required required? Emission Factors for Permit Uncontrolled NOX 88.672 lb/MMscf CO 482.48 lb/MMscf VOC 15101.4979 lb/MMscf Benzene 32.9794 lb/MMscf Toluene 45.7103 lb/MMscf Ethylbenzene 3.9218 lb/MMscf Xylenes 9.5245 lb/MMscf n-Hexane 193.9618 lb/MMscf 224-TMP 0.0000 .lb/MMscf Controlled NOX 88.672 lb/MMscf CO 482.48 lb/MMscf VOC 755.0749 lb/MMscf Benzene 1.6490 lb/MMscf Toluene 2.2855 lb/MMscf Ethylbenzene 0.1961 lb/MMscf Xylenes 0.4762 lb/MMscf n-Hexane 9.6981 lb/MMscf 224-TMP 0.0000 lb/MMscf 008 One (1) Sandpiper G1 F pneumatic pump used for water transfer Section 04: Pump Information Manufactur Sandpiper Model Number: G1F Serial Pump Number: 2091608 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumptio Control O Uncontrolled 0 Flare Section 05: Emission Calculations Emission Calculation Method EPA Emission Inventory Improvement Program Publication:Volume II, Chapter 10- Displacement Equation (10.4- 3) Ex =Q* MW * Xx/C Ex=emissions of pollutant x • Q=Volumetric flow rate/volume of gas processed MW = Molecular weight of gas =SG of gas * MW of air Xx= mass fraction of x in gas C= molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm Q sot) scf/hr MW 22.5 Ib/Ib-mol Hours of Op. 8760 hours/yr Requested Throughput 5.256 MMscf/yr Component Mole % MW mass fraction Component lb/hr lb/yr tpy CO2 2.16 44 0.0422 CO2 1.505 13180.217 6.590 nitrogen 0.63 28 0.0078 nitrogen 0.279 2446.328 1.223 methane 72.92603 16.04 0.5199 methane 18.518 162219.509 81.110 ethane 13.1423 30.07 0.1756 ethane 6.256 54805.097 27,403 propane 7.2887 44.09 0.1428 propane 5.087 44566.273 22.283 isobutane 0.6814 58.12 0.0176 isobutane 0.627 5492.169 2.746 n-butane 1.9526 58.12 0.0504 n-butane 1.797 15738.199 7.869 isopentane 0.3282 72.15 0.0105 isopentane 0.375 3283.909 1.642 n-pentane 0.4119 72.15 0.0132 n-pentane 0.470 4121.395 2.061 cyclopentane 0.0292 72.15 0.0009 n-pentane 0.033 292.170 0.146 n-hexane 0.0853 86.18 0.0033 n-hexane 0.116 1019.463 0.510 cyclohexane 0.0227 84.18 0.0008 cyclohexane 0.030 265.003 0.133 Other hexanes D.1409 86.18 0.0054 Other hexanet 0.192 1683.967 0.842 heptanes 0.0711 100.21 0.0032 heptanes 0.113 988.091 0.494 methylcyclohexa 0.0188 98.19 0.0008 methylcyclohe 0.029 256.001 0.128 224-TMP 0 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 0.016 78.11 0.0006 Benzene 0.020 173.318 0.087 Toluene 0.0188 92.14 0.0008 Toluene 0.027 240.227 0.120 Ethylbenzene 0.0014 106.17 0.0001 Ethylbenzene 0.002 20.613 0.010 Xylenes 0.0034 106.17 0.0002 Xylenes 0.006 50.061 0.025 C8+ Heavies 0.0479 179.08866 0.0038 C8+ Heavies 0.136 1189.651 0.595 Mass Fraction VOC: 0.2544 Total 39.690 Heating Value I 1304 BTU/scf Combustion emission factor source: AP-42:Chapter 13.5 0.07 1 lb NOX/MMBtu 0.37 I lb CO/MMBtu Notes Mole%, MW,and mass fractions from: Buffalo Ditch 1-32H facility gas analysis,dated 211/2008 Emissions Summary Uncontrolle tpy NOX ncontrolle • d/PTE 1.3 tpy CO 39.7 tpy VOC Controlled 2.0 tpy VOC • Reportable Controlled CAS# Total (Ib/yr) ? Total n-hexane 110543 1019.5 Yes 51 • 224-TMP 540841 0.0 No 0 Benzene 71432 173.3 No 9 Toluene 108883 240.2 No 12 E-Benzene 100414 20.6 No 1 Xylenes 1330207 50.1 No 3 Uncontrolled Emission Factors Controlled Emission Factors VOC 15102.837 lb/MMscf 755.1418441 lb/MMscf Benzene 32.975 lb/MMscf 1.648759894 lb/MMscf n-hexane 193.962 lb/MMscf 9.698092348 lb/MMscf Toluene 45.705 lb/MMscf 2.285266491 lb/MMscf E-Benzene 3.922 lb/MMscf 0.196092348 lb/MMscf Xylenes 9.524 lb/MMscf 0.476224274 lb/MMscf 224-TMP 0.000 lb/MMscf 0 lb/MMscf 0 rn a o re a a LU W C N O Oo 2 t a a = z O Z J J O o m o z J o 0 s K > I- 2 Z rnU c p 0 Z 0 > U a a• `^ ¢ Z a o a a.nn r t. a p U 6Nm mn.co m r0 en N' N a m 0• 0 = - a d U H Z Z w O O I- Z � o a • 2• 0 U Q N K C_ a C n a o a a c" o W yaa O J 2 I a CO .- m'o s J 0 o0 U 0 - O C' J 0 Z g8 00 N t- p _ U Ln co v. m 1 3 0 -oamt- NN 0U > - f 0 I- J >0 a nU 0% o Z E$ 0 U C LL ii O Cr 6 o 0o3 O0 Jy LL f ` p a a a s >> 6 3 2 5 ;10010 n x F w ° `o p Q TA U - y o o R N a a C C o =- 0.0166E 0 N Z 3 0 O 3 LL h o a' '0 N N N N N N N 5 C 0 0 0 0 C O O O O a` 333 co a vveavv - a 0 m Z A 0 0 0 0 0 0 0 O O 00000 0 0 • rN 0000W - nn NO Nnvl000 fr- 00 00 000 or� o 'no o 6 ri n ≥m ,-vonvc0000a; innv0mvm0000 F▪ 0 o It r 0 0 0 0 0 0 n F N r n r Vi r....:o 0 0 0 A Tig, 70 ,- - nv r0N Or N0000 72 n N r 010 m n 000m L '(ti ON 006 0(0 m . 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W W W W W W S 3333333 3333333 o v v a v v v v _ a v a v a v v e ¢ m p — :) m ` o o c .t w co u 0 0 0 0 0 co 0 0 y 0 0 0 0 00 co 0 0 T 0 o o 0 7 0000000 Air Pollutant Emission Notice (APEN)—and—Application for Construction Permit OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY Current Status(Check all that apply) Reason for APEN Submittal(Check all that apply) AIRS ID#': 1 Z.3 - '1 6-PA - o 3 ❑ APEN update only./1 ❑ New or previously unreported battery ❑ Modification to existing sources ❑ Previously grandfathered battery' ❑ Registration for coverage under general permit no.GPOI ❑ Synthetic minor facility &cancellation request for individual permit6: Z Located in the 8-hr Ozone Control Area ® Application for or Modification of an individual permit ❑ Registered under general permit no.G 1 El Administrative permit amendment' ❑ Permitted under individual permit: 19 WE 0 D i 2 ❑ Other: For individual permit applications,check if you wants: ® A copy of the preliminary analysis conducted by the Division ®To review a draft of the permit prior to issuance Company Name9: Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address10: 410 1711 Street.Suite 1500 pyoung@BonarvaCrk.co City: Denver State: CO Zip: 80202 E-mail: m Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name": State Antelope F-30 Production Facility(COGCC#432809) Number of tanks: 9-500 bbl Location12(QQ Sec.Twp.Range.): NW/NW,Sec 30,T5N,R62W County: Weld Total tank capacity[bbl]: 4.500 Calendar year for which "Actual"data applies's: 2013 Year(s)tank(s)were placed in service1°: 2013 Eight(8)Leed L30-0010 SN:21126,20667,20334,20668,20665, Control Description's: 20920,20921,20941 Control Efficiency16: 95% Condensate Throughput1?[bbl/year] Requested1t: N/A Maximum for PTE calculation's: 284,700 Actual'-°: 237,250 While Controls Operational2' 237,250 Other equipment at facility-22: Heater treaters,produced water tanks,natural gas-fired engines,pneumatic pump,flare Comments: 2-yr APEN update required(emissions>80tpy) Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit ❑ Check if the Division is to calculate emissions. ®Check if site-specific emission factors provided to calculate emissions. Emission Factor Battery Requested Emissions's Actual Emissions'-° Pollutant24 [lb/bbl] PTE'-' Uncontrolled26 Controlled'' Uncontrolled26 Controlled' VOC[tons/year] 1.94 299.8 229.8 11.49 191.53 9.58 NOx [tons/year] N/A N/A 0.43 0.43 CO[tons/year] N/A N/A 2.35 2.35 Benzene[lbs/year] 0.014 3,439.2 3,439.2 172.0 2,866.0 143.3 n-Hexane[lbs/year] 0.093 22,058.4 22,058.4 1,102.9 18,382.0 919.1 Wells serviced by this tank or tank battery28 API#: 05-123-37291 Name: State Antelope K-O-30HNB , ----. ®Newly Reported Well API#: 05-123-37289 Name: State Antelope 21-24-3OHNC /. A®Newly Reported Well 05-123-37288 API#: Name: State Antelope F-J-3OHNB / Newly Reported Well API#: Name: , L. L 2&I' iii) Newly Reported Well API#: Name '\ `\ /❑Newly Reported Well API#: Name: ❑Newly Reported Well API#: Name: ❑Newly Reported Well The signature below indicates that I have knowledge of the facts herein set forth and that the same are true,accurate,and complete to the best of my knowledge and belief If this is a registration for coverage under general permit GPOI,1 further certify that this source is and will be operated in full co liance with ach condition eral permit GPOI. a -ei// Q_ // Signature of Legally Aiiorized Person(not a vendor or consultant) • Date David J.Lillo Vice President,Roc .Mt.Asset Mana ement Type or Print Name of Person Signing Above • Official Title Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-BI (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South O registration to: Denver,CO 80246-1530 300896 FORM APCD-205 Page I of 2 Form.APCD-205-E&PCondensateTankAPEN.docx r o ° .c a `• Ef / :6iu __ _ O t. O O a E Lou I 201o�ao ❑ d m a \ O C °' c °25 a; Wa. T C C Q, °, °, t Q P. C °. O C V .>`. L.Q .V.' S' C�` /+i^1 M .I y m ^ C q G C ; O 9 } Y v• q J Y� L C O „I _I el GI v ° x e , a. c .c a "e n Q .0 o a ° o a v -_ 1 ° n T -' y .V C '° q r L C r °M ° N 'Si L. ; v ^^I n 1 L0. E =a 2 3 c o. '2 " E , .= E n c - h A y a ni C v e d c ° E c " g : ≥ > N .2 `L y = a Q Ell = L L G L F Es. c4 ` lu ^°' '4J = tC• . 3 N a 4 4 S -^. E _ i y _ '' O. - c E E " 1 i .E 'c.. — E a a. a O F R' s o a v c a U •T• ° E. A 0 , , e y ° oo a _ o 3 E .T4 x y y o 0 0 ° c E 3 a y VD a C Z. Z = 'E _ v w Z Z Z Z E > > P? u 3 e Y E L ePo 6 'n c°� > c°i 1 U I� C A .. 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W ? ° 5 E o o in o °..° o :� e a c c ° v _og .3 v c o e e e e c u -0 y c N _ L V 0 'N L ` o W L �� 7,d O L ... E O c U C 2, a o e o c C Q �/i`. T.) �_ O r GIII _ L. ..a T s'Y •:`wy •� V J c F C v3 � `' o M ,�„� oa a 'eo A C4 o.2- c v, > ❑C. ° a O o °•\• si sri'eg C�'124.'--)4)4.-' r' e c -' >, e. O 9 U s O °' q a a O F`� C 33 c v czgx O4 o s O cra C cn V L ❑ O V 1 .v E E :�. G r . y : t y c a0i a O E O o y e 5 m W 0 r o N Z c G ¢c ° C s C ^ c o. 5 ._0 G ?•l :es'' n n L' u O d ass gssc� , N Q > i _ ° E _ >C > Q ^ e 4 G C+ C. u° `, a - a y C ? d C To. S a E u m �:. ro ° e 5 '° L U Y SU)T C o a. u c U Y >r V C i C o T '� U - F O c m y y' e➢ e u > .il C E V� m co c.J V E ^ Q W o p Q d _ CC � v Q a I a ! L = — v a = I 9 m m O 2 I - O C y la x S C 5 V m C E m C U O N v ; K O L e '.°5 s o c e > 'm c3 Q > E 0 c GC a U c ' .. �, T X •- o v D U d ❑ ❑ so ki ® 21 o CO (/J CI) CI) J VI CA m >. a ,° c * i �-- 91,1,tom ? E c d e .o u E _ so ,. j ri " _ m u m y e %vote c> = _ m L` 'y Q O O o m C J x ` Q 'O u Y \E \_... -:n., 1r11 m M _ .= G. Cs! N C w a". C' m �/ _ _ H -2 � ca ea a E G L4 N O L A u GL) U a 0 O O W en � _ F•' _ > m e. a .� A L 7 a w y L v ---E _C:=,, O ]0 W c a v c c .E 7 7 ' .a m E T c P �� - o d �' L - a0. G O L m = aw. r c' 'Y w Cl W .. .' O ca \ ; P a G o a n .. - e a m , c n 00 v, dJ Z a. - E E 01 04 t"1 = e Y 'a E .. C E E c = �' 3 u > > m vv L (LIc. m _' = o G �+ N v - uu v tit.). u t c e w q `n v �« i ¢ .n i u m `. C !- w L c C v .� � w e 'C I a L n L C s r S ` C ^ R - r `I O L O PO L e c q t0. F' O >` C 6 L e "13t .. _ T O a. p L .. - u w y w o g v 7 Et f' o e -- E c c 0. cn 22 G 3 ' °• ' E A i. _ c ❑ ❑ �, L E . u G 8 i o 7 V u w c a a en c u � c E 'o ❑ I 3 0 C. w > o i W at ^ e w a_ i z_ q c v o E = " v i en o o c .... v V G Y T a L Y T 3 OL 1 C .-' c O '.: T C C c — 3 .. c c > y t c 3 .% ti ww cc E c F 'e o. s- m 0; a v ,0 E w a o - '"' _ — .°'. ` E L' w _ C. L = L e r e w a. Q ' > V R L Lei .'. N _ O C O .ms p c 9 a = � z ' e < 0 '� E c.,,, L m o U . = 10 K x o C Z � o u „L., y u e v 7 - 0 0 �cc q t'G 8 E c c r L w. o C v _ g O — L ca b E c0 a ., o m L 'm w o o a. u c 4 n - G w o .. s q L u 7 U c e q ca G V `t 'E o — z = = no > ,Cr". v d a _ r .2 G Cc. t C � v .a 0 0. G t0 ' m y ',' L L y W v v Z G a y' E GZ] .o v 7 3 ea e y "! [=' v v d e 0 a°- Q Q a 0 Gen a 0, v c 7 9 m G aE c o. E e o g C ' a ` y cC " .v. c Pe 2 y " d U U c c `o Y o t c t, i c e C C ❑ ❑ C C ❑ ❑ - 3 o c c c ° e n e ^> C C e Y Y c M O o at d v ® ❑ ❑ ❑ ., 3. 7 z v L IN E ❑ C I. E ii 3 v T t e c u _ '... 73 C 3 a. v c 7 ❑ ® ® k ; > N w a R 'n 43 y .. O ^ 7 T e 'ni wl VI A C 'n v c ry e IQ u c u �" T 3 d m = e, 2 L v v v d t rya v �. 31• N Y .0.1 � �" , r Ne x .j O `L L E O (a. C .2 90 N r w m T 3 ° >v a 2 ® ❑ ❑ >V O z ❑ L . a. 4 = C •L" O F+ 6 �` Q V O G _ = - LE u Q " E E ry N rn el u _ w z z e � c0 w x _ = o x O m O W O t ti H 7 J > N O C C.J a = T c e ^ F _ a 0. E V Q v c. a c.. 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E C s 73 U m F O O N O bO Q ? '�N=' o `c ' U o p o c 3 � e a G R nay R 7 c] ...._ y _ .^ V o ?. - 3. C 3 <m I e "E m I 'w v w �D Z W v y E N o — C'� = C v C v y o v O o co 19�.m o d E $ 3. -0-1 - o ° = V v y e c m 0 C o v C - r a y y W h - .. m = O o c s u T E G ad G N Q O — ,e G m C O. E y 3 O , > y O . >' C o O 0 u `o Z u C C G. `c° G. c m C 3.i u a W F = X ¢ Y 'u (( re s c �� = v C 9 c li� t ° 12 c o fon ° 0. °c°v \ )/// rt N N m0 .n 0 77= v o a L] U w E o c o u o` c - m L FL' c u ° _ 'c G J i rn .nnE .y.� w P. - c n �, y Dy ^ _ _ C Q' 1, `O — .i . ,A La me o c o _ 3 � " eo r _ ..li: nL23CG .n .E E E n C V'� aY G G0G G ¢1Cr) M ° sv _ v v2 c v u r.Lc.. w ¢ m > ^cJ' = u O. zz 77 • C rrni '� q ?^ E —.. j .cam. N� ? L C LC4 % N ... C.J F p ^ m ic l.: T ° .E S' L ? n E A G U _E n n c ^- E ve ° a. a vOn mcd v E = ^ Eu .E oV z .cli > _ 3 na vZ i, v ° = E = '� v M ° n c 3 _ CI Q s T n = i. 3 °4. L ca c! Qa 3 .0 la E = .c c E _n 3 = _ ^� I u N o 3 .L ... 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