The URL can be used to link to this page

Browse Search

Home My WebLink About20141847.tiff STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH wp4•c°io Executive Director and Chief Medical Officer ,e ' oDedicated to protecting and improving the health and environment of the people of Colorado r<> ~ 4300 Cherry Creek Dr.S. Laboratory Services Division 1816 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 PO Box 758 Greeley,CO 80632 RECEIVED June 11,2014 JUN 17 2014 WELD COUNTY COMMISSIONERS Dear Sir or Madam: On June 15,2014,the Air Pollution Control Division will publish a public notice for Bonanza Creek Energy Operating Company LLC—State Antelope F-32, in the The 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, 7; Clara Gonzales Public Notice Coordinator Stationary Sources Program Air Pollution Control Division Enclosure UJf LCmrn1FW CAI-Am th 96) - 11- aoIM 2014-1847 STATE OF COLORADO John W.Hickenlooper,Governor Larry Wolk,MD,MSPH -10C cot 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 \ � Denver,Colorado 80246-1530 8100 Lowry Blvd. 18 76 Phone(303)692-2000 Denver,Colorado 80230-6928 Colorado Department Located n 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-32—Weld County Released To: The Greeley Tribune On: June 11,2014 Published: June 15, 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-32 Oil and gas production facility NENW Section 32 T5N, R62W Weld County The proposed project or activity is as follows: The applicant proposes to operate a new oil and gas production facility. The Division has determined that this permitting action is subject to public comment per Colorado Regulation No. 3, Part B, Section III.C due to the following reason(s): • permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section ll1.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area) • the source is requesting a federally enforceable limit on the potential to emit in order to avoid other requirements The Division has made a preliminary determination of approval of the application. A copy of the application,the Division's analysis,and a draft of Construction Permit 14WE0156 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: Carissa Money Colorado Department of Public Health and Environment 4300 Cherry Creek Drive South,APCD-SS-BI . Denver,Colorado 80246-1530 cdphe.commentsapcd@state.co.us STATE OF COLORADO LOR D T F PU1rC HEALTH AND ENVIRONMENT �oFcoto AIR POLLUTION CONTROL DIVISION �R TELEPHONE: (303)692-3150 .1 .1876. CONSTRUCTION�ACG PERMIT PERMIT NO: 14 E01 56 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-32 Production Facility, located in the NENW Section 32, Township 5N, Range 62W, Weld County, Colorado. THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING: Facility AIRS Equipment Point Description ID Six(6)500 bbl above ground atmospheric condensate storage Condensate 002 tanks. The condensate storage tanks are controlled by enclosed Tanks flares. Each flare has a minimum combustion efficiency of 95%. Two(2)400 bbl above ground atmospheric produced water storage tanks and two (2)60 bbl concrete vaults for produced PW Tanks 003 water storage. The 400 bbl produced water storage tanks are controlled by enclosed flares. Each flare has a minimum combustion efficiency of 95%. Truck 004 Truck Condensate Loadout Loadout FUG 005 Fugitive VOC equipment leaks Sep-1, Sep- Two low-pressure separators controlled by enclosed flares. Each 2 006 flare has a minimum combustion efficiency of 95%. One (1) pneumatic water transfer pump, rated at 600 scf/hr P-1 007 (Sandpiper, Model G1 F, Serial number 2040603)controlled by enclosed flares. Each flare has a minimum combustion efficiency of 95%. Point 007: 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 AIRS ID: 123/9BDE Page 1 of 20 olor Depa en P Ii ealth and Environment it Pollution Control Division CONTROL ACT C.R. 0 NE ERMS AND CONDITIONS INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS: REQUIREMENTS TO SELF-CERTIFY FOR FINAL AUTHORIZATION 1. YOU MUST notify the Air Pollution Control Division (the Division) no later than fifteen days after issuance of this permit, by submitting a Notice of Startup form to the Division. The Notice of Startup form may be downloaded online at www.cdphe.state.co.us/ao/downloadforms.html. Failure to notify the Division of startup of the permitted source is a violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section III.G.1 and can result in the revocation of the permit. 2. Within one hundred and eighty days (180) after issuance of this permit, compliance with the conditions contained in this permit shall be demonstrated to the Division. It is the owner or operator's responsibility to self-certify compliance with the conditions. Failure to demonstrate compliance within 180 days may result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2). 3. This permit shall expire if the owner or operator of the source for which this permit was issued: (i) does not commence construction/modification or operation of this source within 18 months after either, the date of issuance of this construction permit or the date on which such construction or activity was scheduled to commence as set forth in the permit application associated with this permit; (ii) discontinues construction for a period of eighteen months or more; (iii) does not complete construction within a reasonable time of the estimated completion date. The Division may grant extensions of the deadline per Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, I I I.F.4.) 4. AIRS Point 006: Within ninety(90) days after issuance of this permit, the operator shall install a flow meter to monitor and record volumetric flowrate of natural gas vented from each low pressure separator. The operator shall use the gas flow rate listed in the application for actual flow rate until the flow meter is installed, not to exceed ninety (90) days after issuance of this permit. 5. The operator shall complete all initial compliance testing and sampling as required in this permit and submit the results to the Division as part of the self-certification process. (Reference: Regulation No. 3, Part B, Section III.E.) 6. The operator shall retain the permit final authorization letter issued by the Division, after completion of self-certification, with the most current construction permit. This construction permit alone does not provide final authority for the operation of this source. EMISSION LIMITATIONS AND RECORDS 7. Emissions of air pollutants shall not exceed the following limitations (as calculated in the Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4) Annual Limits: Facility MRS Tons per Year Equipment ID Point NO, VOC CO Emission Type Condensate 002 17.6 3.2 Point Tanks PW Tanks 003 0.8 Point AIRS ID: 123/9BDE Page 2 of 20 olor.�Depa en P ell Health and Environment •it Pollution Control Division Truck Loado. 04 Point FUG 005 11.3 Fugitive Sep-1, Sep-2 006 --- 15.0 4.2 Point P-1 007 --- 1.9 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. 8. AIRS Point 005: The operator shall calculate actual emissions from this emissions point based on representative component counts for the facility with the most recent extended gas analysis, 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. 9. The emission points in the table below shall be operated and maintained with the control equipment as listed in order to reduce emissions to less than or equal to the limits established in this permit(Reference: Regulation No.3, Part B, Section III.E.) Facility AIRS Pollutants Equipment Point Control Device Controlled ID Condensate 002 Enclosed Flare VOC Tanks PW Tanks 003 Enclosed Flare VOC Sep-1, Sep-2 006 Enclosed Flare VOC P-1 007 Enclosed Flare VOC PROCESS LIMITATIONS AND RECORDS 10. This source shall be limited to the following maximum processing rates as listed below. Monthly records of the actual processing rates shall be maintained by the owner or operator and made available to the Division for inspection upon request. (Reference: Regulation 3, Part B, II.A.4) Process/Consumption Limits AIRS ID: 123/9BDE Page 3 of 20 olor epa en li ealth and Environment it Pollution Control Division Facility Equipment Point Process Parameter Annual Limit ID Condensate 002 Condensate Throughput 175,200 BBL Tanks PW Tanks 003 Produced Water Throughput 118,260 BBL Truck 004 Condensate Loaded 175,200 BBL Loadout Sep-1,Sep-2 006 Gas Vented from Separator 12.1 MMSCF P-1 007 Natural Gas Consumed 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. 11. AIRS Point 006: Upon installation of the flow meter required under Condition 4 the owner or operator shall continuously monitor and record the volumetric flowrate of natural gas vented from each low pressure separator using a flow meter. The flow meter shall continuously measure flowrate and record total volumetric flow vented from each separator. The owner or operator shall use monthly throughput records to demonstrate compliance with the limits specified in Condition 10 and to calculate emissions as described in this permit. STATE AND FEDERAL REGULATORY REQUIREMENTS 12. AIRS Points 002, 003, 004, 006 and 007: The permit number and AIRS ID point number (e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification. (Reference: Regulation Number 3, Part B, III.E.) (State only enforceable) 13. Visible emissions shall not exceed twenty percent(20%)opacity during normal operation of the source. During periods of startup, process modification, or adjustment of control equipment visible emissions shall not exceed 30% opacity for more than six minutes in any sixty consecutive minutes. Emission control devices subject to Regulation 7, Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation No. 1, Section II.A.1. &4.) 14. This source is subject to the odor requirements of Regulation No. 2. (State only enforceable) 15. 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.) 16. AIRS Point 002: The flare covered by this permit is subject to Regulation No. 7, Section XII.C General Provisions (State only enforceable). If a combustion device is used to control emissions of volatile organic compounds to comply with Section XII.D, it shall be enclosed, have no visible emissions, and be designed so that an observer can, by means of visual observation from the outside of the enclosed combustion device, or by other means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XII. AIRS ID: 123/9BDE Page 4 of 20 olor Depa en .f P:'.11 Health and Environment it Pollution Control Division 17. AIRS Point 0' Rso is t rdke a r' monitoring, reporting and emission control requirements of Regulation 7, Section XII. The operator shall comply with all applicable requirements of Section XII. 18. AIRS Point 002: The condensate storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: XVII.C.1.a. Beginning May 1, 2008, owners or operators of all atmospheric condensate storage tanks with uncontrolled actual emissions of volatile organic compounds equal to or greater than 20 tons per year based on a rolling twelve-month total shall operate air pollution control equipment that has an average control efficiency of at least 95%for VOCs on such tanks. 19. AIRS Points 002 and 003: The flare covered by this permit is subject to Regulation No. 7, Section XVII.B General Provisions (State only enforceable). These requirements include, but are not limited to: XVII.B.1.b If a flare or other combustion device is used to control emissions of volatile organic compounds to comply with Section XVII, it shall be enclosed, have no visible emissions during normal operations, and be designed so that an observer can, by means of visual observation from the outside of the enclosed flare or combustion device, or by other convenient means approved by the Division, determine whether it is operating properly. The operator shall comply with all applicable requirements of Section XVII. XVII.B.2.d.(ii) All combustion devices installed before May 1, 2014, must be equipped with an operational auto-igniter by or before May 1, 2016, or after the next combustion device planned shutdown, whichever comes first. 20. AIRS Points 002 and 003: The storage tanks covered by this permit are subject to Regulation 7, Section XVII.C emission control requirements. These requirements include, but are not limited to: Section XVII.C.1. Control and monitoring requirements for storage tanks XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of VOCs equal to or greater than six (6) tons per year based on a rolling twelve- month total must operate air pollution control equipment that achieves an average hydrocarbon control efficiency of 95%. If a combustion device is used, it must have a design destruction efficiency of at least 98%for hydrocarbons. XVII.C.1.b.(i)(b) Control requirements of Section XVII.C.1.b. must be achieved by May 1, 2015. 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 constructed before May 1, 2014 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 AIRS ID: 123/9BDE Page 5 of 20 epa en P li ealth and Environment it Pollution Control Division are unDolor u i ibl 'or, a ed in Section XVII.C.1.e. The additional visual inspections must include, at a minimum: XVII.C.1.d.(i) Visual inspection of any thief hatch, pressure relief valve, or other access point to ensure that they are closed and properly sealed; XVII.C.1.d.(ii) Visual inspection or monitoring of the air pollution control equipment to ensure that it is operating, including that the pilot light is lit on combustion devices used as air pollution control equipment; XVII.C.1.d.(iii) If a combustion device is used, visual inspection of the auto-igniter and valves for piping of gas to the pilot light to ensure they are functioning properly; XVII.C.1.d.(iv) Visual inspection of the air pollution control equipment to ensure that the valves for the piping from the storage tank to the air pollution control equipment are open; and XVII.C.1.d.(v) If a combustion device is used, inspection of the device for the presence or absence of smoke. If smoke is observed, either the equipment must be immediately shut-in to investigate the potential cause for smoke and perform repairs, as necessary, or EPA Method 22 must be conducted to determine whether visible emissions are present for a period of at least one(1)minute in fifteen(15)minutes. XVII.C.1.e. If storage tanks or associated equipment is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor such equipment until it becomes feasible to do so. XVII.C.2. Capture and monitoring requirements for storage tanks that are fitted with air pollution control equipment as required by Sections XII.D. or XVII.C.1. XVII.C.2.a. Owners or operators of storage tanks must route all hydrocarbon emissions to air pollution control equipment, and must operate without venting hydrocarbon emissions from the thief hatch (or other access point to the tank) or pressure relief device during normal operation, unless venting is reasonably required for maintenance, gauging, or safety of personnel and equipment. Compliance must be achieved in accordance with the schedule in Section XVII.C.2.b.(ii). XVII.C.2.b. Owners or operators of storage tanks subject to the control requirements of Sections XII.D.2., XVII.C.1.a, or XVII.C.1.b. must develop, certify, and implement 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 AIRS ID: 123/9BDE Page 6 of 20 Depa en P li Health and Environment it Pollution Control Division Dolor t p sc ecti II.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: X\/II.C.2.b.(ii)(b) A storage tank constructed before May 1, 2014, must comply with the requirements of Sections XVII.C.2.a. and XVII.C.2.b. by May 1, 2015. Approved instrument monitoring method inspections must begin within ninety (90) days of the Phase-In Schedule in Table 1, or within thirty (30) days for storage tanks with uncontrolled actual VOC emissions greater than 50 tons per year. 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 Uncontrolled Actual VOC Monitoring Method Inspection Schedule Emissions (tpy) Frequency > 6 and < 12 Annually January 1, 2016 > 12 and < 50 Quarterly July 1, 2015 > 50 Monthly January 1, 2015 XVII.C.2.b.(iii)Owners or operators are not required to monitor storage tanks and associated equipment that are unsafe, difficult, or inaccessible to monitor, as defined in Section XVII.C.1.e. XVII.C.2.b.(iv) STEM must include a certification by the owner or operator that the selected STEM strategy(ies) are designed to minimize emissions from storage tanks and associated equipment at the facility(ies), including thief hatches and pressure relief devices. XVII.C.3. Recordkeeping XVII.C.3. The owner or operator of each storage tank subject to Sections XII.D. or XVII.C. must maintain records of STEM, if applicable, including the plan, any updates, and the certification, and make them available to the Division upon request. In addition, for a period of two (2) years, the owner or operator must maintain records of any required monitoring and make them available to the Division upon request, including: XVII.C.3.a. The AIRS ID for the storage tank. AIRS ID: 123/9BDE Page 7 of 20 olor epa en li ealth and Environment it Pollution Control Division XVII.C.3.b. TJJ n here ief 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 airpollution 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. 21. AIRS Point 004: This source is located in an ozone non-attainment or attainment- maintenance area and is subject to the Reasonably Available Control Technology (RACT) requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to truck tanks shall be conducted by submerged fill. (Reference: Regulation 3, Part B, III.E) 22. AIRS Point 004: The owner or operator shall follow loading procedures that minimize the leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation 3, Part B, III.E): a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or other liquid or vapor loss during loading and unloading. b. All compartment hatches (including thief hatches) shall be closed and latched at all times when loading operations are not active, except for periods of maintenance, gauging, or safety of personnel and equipment. c. The owner or operator shall inspect loading equipment and operations on site at the time of the inspection to ensure compliance with Condition 22 (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. 23. AIRS Point 004: All hydrocarbon liquid loading operations, regardless of size, shall be designed, operated and maintained so as to minimize leakage of volatile organic compounds to the atmosphere to the maximum extent practicable. 24. 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. 25. AIRS Point 005: This source is subject to Regulation No. 7, Section XVII.F. leak detection and repair requirements,which include but are not limited to: XVII.F.1. As of the compliance date specified in XVII.F.4, the provisions of Section XVII.F. shall apply in lieu of any directed inspection and maintenance program requirements established pursuant to Regulation Number 3, Part B, Section III.D.2. AIRS ID: 123/9BDE Page 8 of 20 iiolor- jDepa en P .li Health and Environment • .it Pollution Control Division XVII.F.4. Req ,�._ ""s , e ct',r,.- ' ies XVII.F.4.b. Owners or operators of well production facilities constructed before October 15, 2014, must identify leaks from components using an approved instrument monitoring method within ninety (90) days of the Phase-In Schedule in Table 4; within thirty (30) days for well production facilities subject to monthly approved instrument monitoring method inspections; or by January 1, 2016, for well production facilities subject to a one time approved instrument monitoring method inspection. Thereafter, approved instrument monitoring method and AVO inspections must be conducted in accordance with the Inspection Frequencies in Table 4. XVII.F.4.c. The estimated uncontrolled actual VOC emissions from the highest emitting storage tank at the well production facility determines the frequency at which inspections must be performed. Table 4—Well Production Facility Component Inspections Thresholds (per XVII.F.4.c)—Well Production Facilities Approved Instrument AVO with Storage Tanks Monitoring method Inspection Phase-In (tpy) Inspection Frequency Frequency Schedule > 0 and < 6 One time Monthly January 1, 2016 > 6 and < 12 Annually Monthly January 1, 2016 > 12 and < 50 Quarterly Monthly January 1, 2015 > 50 Monthly January 1, 2015 XVII.F.5. If a component is unsafe, difficult, or inaccessible to monitor, the owner or operator is not required to monitor the component until it becomes feasible to do so. XVII.F.6 Leaks requiring repair: Leaks must be identified utilizing the methods listed in Section XVII.F.6. Only leaks detected pursuant to Section XVII.F.6. require repair under Section XVII.F.7. XVII.F.6.a. For EPA Method 21 monitoring, or other Division approved quantitative instrument based monitoring, at facilities constructed before May 1, 2014, a leak is any concentration of hydrocarbon above 2,000 parts per million (ppm) not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation, except for well production facilities where a leak is defined as any concentration of hydrocarbon above 500 ppm not associated with normal equipment operation, such as pneumatic device actuation and crank case ventilation. XVII.F.6.c. For infra-red camera and AVO monitoring, or other Division approved non- quantitative instrument based monitoring, a leak is any detectable emissions not AIRS ID: 123/9BDE Page 9 of 20 epa en P li ealth and Environment it Pollution Control Division associDolor e ' nt suc neumatic device actuation and crank case ventilation. XVII.F.6.e. For leaks identified using an approved instrument monitoring method or AVO, owners or operators have the option of either repairing the leak in accordance with the repair schedule set forth in Section XVII.F.7. or conducting follow-up monitoring using EPA Method 21 within five (5) working days of the leak detection. If the follow-up EPA Method 21 monitoring shows that the emission is a leak as defined in Section XVII.F.6., the leak must be repaired and remonitored in accordance with Section XVII.F.7. XVII.F.7. Repair and remonitoring XVII.F.7.a. First attempt to repair a leak must be made no later than five (5) working days after discovery, unless parts are unavailable, the equipment requires shutdown to complete repair, or other good cause exists. If parts are unavailable, they must be ordered promptly and the repair must be made within fifteen (15) working days of receipt of the parts. If shutdown is required, the leak must be repaired during the next scheduled shutdown. If delay is attributable to other good cause, repairs must be completed within fifteen (15) working days after the cause of delay ceases to exist. XVII.F.7.b. Within fifteen (15) working days of completion of a repair, the leak must be remonitored to verify the repair was effective. XVII.F.7.c. Leaks discovered pursuant to the leak detection methods of Section XVII.F.6. shall not be subject to enforcement by the Division unless the owner or operator fails to perform the required repairs in accordance with Section XVII.F.7. XVII.F.8. Recordkeeping: The owner or operator of each facility subject to the leak detection and repair requirements in Section XVII.F. must maintain the following records for a period of two (2) years and make them available to the Division upon request. XVII.F.8.a. Documentation of the initial approved instrument monitoring method inspection for new well production facilities; XVII.F.8.b. The date and site information for each inspection; XVII.F.8.c. A list of the leaking components and the monitoring method(s) used to determine the presence of the leak; XVII.F.8.d. The date of first attempt to repair the leak and, if necessary, any additional attempt to repair the leak; XVII.F.8.e. The date the leak was repaired; XVII.F.8.f. The delayed repair list, including the basis for placing leaks on the list; XVII.F.8.g. The date the leak was remonitored to verify the effectiveness of the repair, and the results of the remonitoring; and XVII.F.8.h. A list of components that are designated as unsafe, difficult, or inaccessible to monitor, as described in Section XVII.F.5., an explanation stating why the component is so designated, and the plan for monitoring such component(s). AIRS ID: 123/9BDE Page 10 of 20 Illolor. Depa en": P •Ii Health and Environment it Pollution Control Division XVII.F.9. Rep a. he =•e ->>,ra.$,kx•, z `__ facil' .•bject to the leak detection and repair requirements in Section XVII.F. must submit reports as specified in Section XVII.F.9. 26. AIRS Point 005: Minor sources in designated nonattainment or attainment/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 must 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 27. AIRS Points 002, 003, 005, 006 and 007: Upon startup of these points, the owner or operator shall follow the most recent operating and maintenance (O&M) plan and record AIRS ID: 123/9BDE Page 11 of 20 olor Depa en P li Pollution ealth andControl EnvironDivisionment it keeping form th • io to strate compliance on an ongoing basis with the requirements of this permit. Revisions to your O&M plan are subject to Division approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.) COMPLIANCE TESTING AND SAMPLING Initial Testing Requirements 28. AIRS Point 005: 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. 29. AIRS Point 006: The operator shall complete an initial site-specific extended gas analysis of the natural gas vented from each low pressure separator in order to verify the VOC, benzene, toluene, ethylbenzene, xylenes, n-hexane, and 2,2,4-trimethylpentane content (weight fraction) of this emission stream used in the permit application. Results of testing shall be used to determine site-specific emission factors using Division approved methods. Results of site-specific sampling and analysis shall be submitted to the Division as part of the self-certification and used to demonstrate compliance with the emissions factors chosen for this emissions point. Periodic Testing Requirements 30. AIRS Point 005: 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 31. AIRS Point 007: 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. 32. AIRS Point 007: 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. 33. AIRS Point 007: All pump replacements installed and operated per the altemate operating scenarios authorized by this permit must comply with all terms and conditions of this construction permit. ADDITIONAL REQUIREMENTS 34. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No. 3, Part A, II.C) a. Annually by April 30th whenever a significant increase in emissions occurs as follows: AIRS ID: 123/9BDE Page 12 of 20 Da olor- 1 Depa en P li Health and Environment • it Pollution Control Division For a •.=•13 ,a 4 For sources emitting less than 100 tons per year, a change in actual emissions of five (5)tons per year or more, above the level reported on the last APEN; or For volatile organic compounds (VOC) and nitrogen oxides sources (NO.) in ozone nonattainment areas emitting less than 100 tons of VOC or NO. per year, a change in annual actual emissions of one (1) ton per year or more or five percent, whichever is greater, above the level reported on the last APEN; or 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. 35. 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 36. 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. 37. If this permit specifically states that final authorization has been granted, then the remainder of this condition is not applicable. Otherwise, the issuance of this construction permit does not provide "final" authority for this activity or operation of this source. Final authorization of the permit must be secured from the APCD in writing in accordance with the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation No. 3, Part B, Section III.G. Final authorization cannot be granted until the operation or activity commences and has been verified by the APCD as conforming in all respects with the conditions of the permit. Once self-certification of all points has been reviewed and approved by the Division, it will provide written documentation of such final authorization. Details for obtaining final authorization to operate are located in the Requirements to Self- Certify for Final Authorization section of this permit. AIRS ID: 123/9BDE Page 13 of 20 olor epa en P li ealth and Environment it Pollution Control Division 38. This permit i m t y an pleteness 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. 39. 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. 40. 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. 41. 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. 42. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution Prevention and Control Act or the regulations of the AQCC may result in administrative, civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121 (injunctions), -122(civil penalties), -122.1 (criminal penalties), C.R.S. By: Carissa Money Permit Engineer Permit History Issuance Date Description Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating Company LLC AIRS ID: 123/9BDE Page 14 of 20 l olor. Depa en • P •li Health and Environment •it Pollution Control Division . 111 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) Benzene 71432 9,650 Yes 483 n-Hexane 110543 49,994 Yes 2,500 Toluene 108883 5,686 Yes 284 002 Ethylbenzene 100414 377 Yes 19 Xylenes 1330207 1,524 Yes 76 2,2,4- 540841 2,230 Yes 111 trimethylpentane Benzene 71432 828 Yes 41 003 n-Hexane 110543 2,602 Yes 130 Benzene 71432 766 Yes 766 n-Hexane 110543 3,518 Yes. 3,518 Toluene 108883 1,418 Yes 1,418 004 Ethylbenzene 100414 257 Yes 257 Xylenes 1330207 1,172 Yes 1,172 2,2,4- 540841 420 Yes 420 trimethylpentane Benzene 71432 138 No 138 005 n-Hexane 110543 624 Yes 624 AIRS ID: 123/9BDE Page 15 of 20 olor epa en P li ealth and Environment • it Pollution Control Division Tol 8 222 Ethylbenzene 100414 40 No 40 Xylenes 1330207 177 No 177 Benzene 71432 1,268 Yes 63 n-Hexane 110543 7,598 Yes 380 Toluene 108883 842 Yes 42 006 Ethylbenzene 100414 101 No 5 Xylenes 1330207 193 No 10 2,2,4- 540841 4 No 0 trimethylpentane Benzene 71432 146 No 7 n-Hexane 110543 901 Yes 45 007 Toluene 108883 100 No 5 Ethylbenzene 100414 10 No 1 Xylenes 1330207 34 No 2 5) The emission levels contained in this permit are based on the following emission factors: Point 002: Emission Factors Emission Factors Uncontrolled Controlled Pollutant lb/BBL lb/BBL Source Condensate Condensate Throughput Throughput NOx 0.068 Ib/MMBtu 0.068 Ib/MMBtu AP-42, Table 13.5 CO 0.37 lb/MMBtu 0.37 Ib/MMBtu AP-42, Table 13.5 VOC 4.0131 0.2007 E&P TANK n-Hexane 0.2854 0.0143 E&P TANK Benzene 0.0551 0.0028 E&P TANK Toluene 0.0325 0.0016 E&P TANK Ethylbenzene 0.0022 0.0001 E&P TANK Xylenes 0.0087 0.0004 E&P TANK 2,2,4- 0.0127 0.0006 E&P TANK trimethylpentane Note: The controlled emissions for this point are based on the flare control efficiency of 95%. A HHV of 2,946 BTU/scf was used for combustion calculations. Point 003: Emission Factors Emission Factors Pollutant Uncontrolled Controlled Source lb/BBL Produced lb/BBL Produced Water Throughput Water Throughput VOC 0.262 0.0131 CDPHE n-Hexane 0.022 0.0011 CDPHE Benzene 0.007 0.0004 CDPHE AIRS ID: 123/9BDE Page 16 of 20 olor Depa en P li Health and Environment it Pollution Control Division Note: The co is ' fo int n the control efficiency of 95%. Point 004: Emission Factors- Uncontrolled Pollutant lb/BBL loaded Source VOC 0.2771 AP-42 Benzene 0.0044 AP-42 n-Hexane 0.0201 AP-42 Toluene 0.0081 AP-42 Ethylbenzene 0.0015 AP-42 Xylenes 0.0067 AP-42 2,2,4- 0.0024 AP-42 trimethylpentane The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1 (version 1/95)using the following values: L= 12.46*S*P*M/T S =0.6(Submerged loading: dedicated normal service) P(true vapor pressure)=6.88 psia M (vapor molecular weight) =67.18 Ib/Ib-mol T(temperature of liquid loaded)=524 R The uncontrolled non-criteria reportable air pollutant (NCRP)emission factors were calculated by multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor. Point 005: Component Gas Heavy Oil Light Oil Water/Oil Connectors 1217 0 571 534 Flanges 51 0 16 20 Open-ended Lines 37 0 6 2 Pump Seals 2 0 0 1 Valves 177 0 72 58 Other 86 0 8 20 VOC Content(wt. 0.2442 1 0.9968 1 fraction) Benzene Content(wt. 0.000476 0 0.0158 0.0012 fraction) Toluene Content(wt. 0.000324 0 0.0292 0.0003 fraction) Ethylbenzene (wt. 0.000033 0 0.0053 0.0001 fraction) Xylenes Content(wt. 0.00011 0 0.0241 0.0001 fraction) n-hexane Content(wt. 0.002931 0 0.0724 0.0001 fraction) *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): AIRS ID: 123/9BDE Page 17 of 20 olor epa en li ealth and Environment it Pollution Control Division Component Gas ervice Heavy I ig t 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/R-95-017 Table 2-4 Compliance with emissions limits in this permit will be demonstrated by using the TOC emission factors listed in the table above with representative component counts, multiplied by the VOC content from the most recent extended gas analysis. Point 006: Weight Emission Emission Pollutant Fraction Factors Factors Source of Gas(%) Uncontrolled Controlled Ib/MMscf Ib/MMscf NOx(lb/MMBTU) -- 0.068 0.068 AP-42 CO(lb/MMBTU) -- 0.37 0.37 AP-42 VOC 56.2 49,633 2,481.6 Gas Analysis Benzene 0.12 105.12 5.2561 Gas Analysis Toluene 0.08 69.781 3.4891 Gas Analysis Ethylbenzene 0.01 8.4040 0.4202 Gas Analysis Xylenes 0.02 15.968 0.7984 Gas Analysis n-hexane 0.71 630.09 31.505 Gas Analysis 2,2,4- 0.003 0.3014 0.0151 Gas Analysis trimethylpentane Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collected 9/11/2013 of the gas vented from the low pressure separator at State Antelope J-F-28-HNB to estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow. The controlled VOC and HAP emissions factors for point 006 are based on the flare control efficiency of 95%. Emission factors for CO and NOx are based on AP-42 Table 13.5-1. A HHV of 1,901 BTU/scf was used for calculations. Point 007: Emission Emission Factors- Factors- Uncontrolled Controlled • Pollutant Ib/MMscf vented lb/MMscf vented Source NOx 0.068 0.068 AP-42 (lb/MMBTU) CO 0.37 0.37 AP-42 (lb/MMBTU) VOC 14,284 714.21 Gas Analysis Benzene 27.823 1.3911 Gas Analysis AIRS ID: 123/9BDE Page 18 of 20 olor Depa en P li Health and Environment it Pollution Control Division io Factors- Factors- Uncontrolled Controlled Pollutant lb/MMscf vented Ib/MMscf vented Source n-Hexane 171.45 8.5725 Gas Analysis Toluene 18.963 0.9482 Gas Analysis Ethylbenzene 1.9609 0.0980 , Gas Analysis Xylenes 6.4430 0.3222 Gas Analysis The displacement equation can found in "EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10-Displacement Equation (10.4-3)." Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,287 BTU/scf was used for combustion calculations. 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 and HAPs NANSR Synthetic Minor Source of: VOC MACT HH Major Source Requirements: Not Applicable Area Source Requirements: Not Applicable 8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be found at the website listed below: http://ecfr.gpoaccess.uov/ 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 SubpartA—SubpartZ 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 AIRS ID: 123/9BDE Page 19 of 20 olor Depa en P li ealth and Environment it Pollution Control Division 9) An Oil and Gas I on 'o 't tion F 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-certifiication can be found on our website at: www.colorado.gov/cdpheThilgaspermits AIRS ID: 123/9BDE Page 20 of 20 Division Information Engineer: Carissa Money Control Engineer: NA Review Date: 05/20/2014 Application Date: 12/09/2013 Facility Identifiers Permit No. 14W E0156 AIRS County# 123 Weld Facility# 9BDE Facility Type: exploration and production facility E Located in the 8-hour non-attainment area? 0 True Minor 0 Synthetic Minor for: t✓ VOC r NOx r CO Administrative Information Company Name: Bonanza Creek Energy Operating Company LLC Source Name: State Antelope F-32 Production Facility Source Location: NENW Section 32,Township 5N, Range 62W SIC: 1311 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 Requested Action Self Certification Required? Yes Issuance Number: 1 Source Description: Oil and gas exploration and production facility known as the State Antelope F-32 Production Facility,located in the NENW Section 32,Township 5N,Range 62W,Weld County.Colorado. Point Name Type Control 002 Condensate Condensate Tanks Flare Tanks 003 PW Tanks Water Tanks Flare 004 TL Loadout None 005 FUG Fugitives None 006 Sep-1, Sep-2 Separator Venting Flare 007 P-1 Pump Flare Six(6)500 bbl above ground atmospheric condensate storage tanks.The condensate storage tanks are controlled by enclosed flares.Each flare has a minimum combustion 002 efficiency of 95%. Requsted Throughput 175200 bbl • Control Flare Efficiency 95.00%I Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 4.0131 lb/bbl 351.5 tpy 17.58 tpy E&P TANK Benzene 0.0551 lb/bbl 9650.4 lb/yr 483 lb/yr E&P TANK n-Hexane 0.2854 lb/bbl 49994.4 lb/yr 2500 lb/yr E&P TANK Toluene 0.0325 lb/bbl 5685.6 lb/yr 284 lb/yr E&P TANK Ethylbenze 0.0022 lb/bbl 376.8 lb/yr 19 lb/yr E&P TANK Xylenes 0.0087 lb/bbl 1524 lb/yr 76 lb/yr E&P TANK 2,2,4-TMP 0.0127 lb/bbl 2229.6 lb/yr 111 lb/yr E&P TANK Nox 0.068 lb/Mmbtu 0.60 tpy 0.60 tpy AP-42 Table 1 CO 0.37 lb/Mmbtu 3.24 tpy 3.24 tpy AP-42 Table 1 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 11.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. 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. P NSPS Kb: for storage vessels greater than 19,800 gallons after 7123/84. The 500 bbl tanks are above the minimum capacity threshold of—471 bbl. However,the tanks are located at the wellhead site,store condensate,and are prior to custody transfer;thus,the tanks are exempt from NSPS Kb (60.110b(d)(4)). NSPS OOOO:for storage vessels in the natural gas production,transmission,and processing segments. 14WE0156.CP1 123/9BDE Six(6)500 bbl above ground atmospheric condensate storage tanks.The condensate storage tanks are controlled by enclosed flares.Each flare has a minimum combustion 002 efficiency of 95%. This source is not subject because each tank emits less than 6 tpy VOC. Regulation 7—Volatile Organic Compounds XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS (Applicant is subject to the emission control requirements for condensate tanks since it is located in an attainment area.) XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS... (Applicant is subject since actual uncontrolled emissions are greater than 20 tpy of VOC.) 14WE0156.CP1 123/9BDE Two(2)400 bbl above ground atmospheric produced water storage tanks and two (2)60 bbl concrete vaults for produced water storage.The produced water storage tanks are controlled by enclosed flares.Each flare has a minimum combustion 003 efficiency of 95%. Emissions Calculations Requsted Throughput 118260 bbl Control Flare Efficiency 95.00% Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.262 lb/bbl 15.49206 tpy 0.774603 tpy CDPHE Benzene 0.007 lb/bbl 827.82 lb/yr 41.391 lb/yr CDPHE n-Hexane 0.0221b/bbl 2601.72 lb/yr 130.086 lb/yr CDPHE Regulatory Review Section II.A.1 -Except as provided in paragraphs 2 through 6 below,no owner or operator of a source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess of 20%opacity.This standard is based on 24 consecutive opacity readings taken at 15-second intervals for six minutes.The approved reference test method for visible emissions measurement is EPA Method 9(40 CFR, Part 60,Appendix A(July, 1992))in all subsections of Section II.A and B of this regulation. Section II.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity for a period or periods aggregating more than six minutes in any sixty consecutive minutes. ulation 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. 14WE0156.CP1 123/9BDE 004 Truck Condensate Loadout Calculations L=12.46*S*P*M/T(AP-42:Chapter 5.2, Equation 1) L=loading losses in lb per 1000 gallons loaded Factor Meaning Value Units Source S Saturation Factor 0.6 AP-42 P True Vapor Pressure 6.88 psia Sales Oil Analysis documenting RVP 9 and AP-4 M Molecular Weight of Vaf 67.18 lb/lb-mole Sales oil analysis for RVP 9 and interpolating va T Liquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver, CO L 6.60 lb/10^3 gal 2.77E-01 lb/bbl Annual requested Throughput 175200 BBL/yr 7358400 gal/yr Annual requested VOC emissions 48554 lb/yr 24.28 tpy Control: None Efficiency: 0.00% NCRPs Component Mass Fraction Benzene 0.0158 n-hexane 0.0725 Toluene 0.0292 Ethylbenzen 0.0053 Xylenes 0.0241 2,2,4-TMP 0.0087 Source: Condensate analysis Emissions Summary Table Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 0.2771 lb/bbl 24.28 tpy 24.28 tpy AP-42 Benzene 0.0044 lb/bbl 765.99 lb/yr 765.99 lb/yr AP-42 n-Hexane 0.0201 lb/bbl 3518.31 lb/yr 3518.31 lb/yr AP-42 Toluene 0.0081 lb/bbl 1417.53 lb/yr 1417.53 lb/yr AP-42 Ethylbenzen 0.0015 lb/bbl 256.80 lb/yr 256.80 lb/yr AP-42 Xylenes 0.0067 lb/bbl 1171.80 lb/yr .1171.80 lb/yr AP-42 2,2,4-TMP 0.0024 lb/bbl 420.14 lb/yr 420.14 lb/yr AP-42 Regulatory Review 'Regulation 7-Volatile Organic Compounds 14WE0156.CP1 123/9BDE 004 Truck Condensate Loadout This facility is not considered a bulk plant(in Reg.7)because it does not distribute gasoline. 14WE0156.CP1 123/9BDE 005 Fugitive equipment leaks Regulation 7 Information Operating Hours: 8760 hourayear Emission Fedor Source EPA-453/R-95-017 Table 2-4 Control Efficiency Source None Calculations Emission Factor lkybr- Emissions SeMce Component Type Count source) Control(X)Pollutant Mass Fraction gpyl Table 2-4 Table 24 Reg.3 • Connectors 1217 200(04 5.00505 0 0% \/0C 02442 40600634 Flanges 51 390E-04 5.70E-06 O0'% Benzene 00--0476 0.0086937 Open-Ended Line 37 2.10E-03 150E-05 05% Toluene 0000324 0.0059175 Can Pump Seals 2 240E-03 3506-04 0.0% EOylbenzene 0000033 0.0006027 Valves z 4.50E-03 2.50E-05 01% Xylenes 000011 0.002009 Other 60 0.806-03 1.20E M4 O0% n-Hexane 0002931 00535317 Connectors 2.50E 06 7.50E-06 0001- VOC 1 0 Flanges 390E-0] 3.90E-02 00%, Benzene 0 Open-Ended Urns 1.40E-04 2.20E-06 00m Toluene 0 Heavy Oil Pump Seals 0016.00 0.00E+00 r00%, EmNbenzene 0 Valves BA0E-06 840E-06 00% Xylenes 0 Other 330E-05 320E-05 9.O:'d n-Henna 0 Connectors !174 2.10E-04 7.50E-06 0 VOC :10.466 3.5545833 Flanges lb 1.10E-04 2.40E-06 0001 Benzene 00158 00563427 Open-Ended Lines 5 1.406-03 1.40E-05 00'% Toluene D 0292 0.104127 U O11 Pump Seals 0 1306-02 5.106.04 0 Elnytbenzene 00053 0.0368596 Valves 72 2506-03 1.90E-05 004% Xylenes 0 D241 0.0859405 Other B 7.50E-03 ]106-04 00% n-Hexane 00724 0.258176 Connectors 034 1.10E-04100E-05 00% VOC 1 3.3244778 Flanges 20 190E-06 290E-05 00% Benzene 00012 0.0039994 Open-Ended Lines 2 2.50E-04 3.50E-06 007v Toluene 00003 0.0009973 Water/Oil Pump Seals 1 2.40E-05 2406-05 0.0% Emylbenzene 0000'1 0.0003324 Valves 58 9.80E-05 970E-06 003 Xylenes 00001 0.0003324 Other 20 140E-02 5.90E-05 0 nMeaene 00001 0.0003324 Emissions Summery Table Pollutant Uncontrolled Emisnicns Controlled Emissions Source VOL 11.34 Ipy 11.34 MY EPA-453/H-95-017 Table 2-4 Benzene 13805 lb/yr 13805 lb/yr EPA-453/R-95-037 Table 2-4 Toluene 22200 lb/yr 222.08 lb/yr EPA-453/R-95017 Table 2-4 Etdybenzene 39 67 3067 lb/yr EPA-453/0-95017 Table 2-4 Xylenes 176.58 lb/yr 176.56 Ib1yr EPA-453/R-95-017 Table 2-4 n-Hexane 624 08 lb/yr 624.08 lb/yr EPA4637R-95-017 Tede 2-4 Regulatory Applicability The date of intones'for determining abeder the source is new or modified is therefore November 20.2007 ghe dale of Reg.3 the 8-hour ozone NA area designation).Since the site was built alter lye dale above(npereti0n began 9/19/2013),this source is mnaiemee'new or nwdihed.'operator hes agreed on the Bivision'a standard condilins. VOC and HAP concentration for gas service am based 0n sales gas Sample collected 10/30/2013 from Slate Antelope t 1-14.32HNe.Since site-specific and within 1 year of applmatmn dale.n0 mite aampbng required. 14WE0156.CP3 123/9800 006 Two low-pressure separators controlled by enclosed flares.Each flare has a minimum combustion efficiency of 95%. Equipment Description - This source vents natural gas from: a well head separator Emissions from this source are: routed to a flare 'Natural gas venting from a wet head separator.Emissions from this source are routed to a flare. Calculations EfNssion Cakulauon Method EPA Emission Inventory Improvement Program Publication:Volume II,Chapter 10-Displacement Equation(10.4-3) Ex=O•MW•Xx/C Ex=emissions of pollutant x 0=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) 12.059016 MMscf/yr 1376.6 scf/hr MW 33.5 IMbmd 0.0330384 MMsci/d mole% MW IbMbnwl mass fraction IMr Ib/yr spy Argon 0.0100 39.948 0.004 0.000 0.01 127.11 0.06 CO2 2.6100 44.01 1.149 0.034 4.17 36548.08 18.27 N2 0.1100 28.013 0.031 0.001 0.11 980.45 0.49 methane 36.4647 16.041 5.849 0.175 21.25 188113.02 93.06 ethane 24.3204 30.083 7.311 0.218 28.58 232635.34 116.32 propane 22.6132 44.092 10.059 0.300 38.54 320050.62 160.03 isob lane 2.3670 58.118 1.376 0.041 5.00 43770.51 21.89 n-butane 7.2540 58.118 4.216 0.126 15.31 134140.79 67.07 isopentene 1.1875 72.114 0.856 0.026 3.11 27247.45 13.82 n-pentane 1.4761 72.114 1.084 0.032 3.87 33889.44 16.93 cydopentene 0.1075 70.13 0.075 0.002 0.27 2398.75 1.20 n-Hexane 0.2771 86.18 0.239 0.0071 0.87 7598.29 3.80 cydobexene 0.0699 84.16 0.059 0.002 0.21 1871.78 0.94 Other hexenes 0.4770 86.18 0.411 0.012 1.49 13079.59 6.54 heptenes 0.2098 100.21 0.210 0.008 0.76 6689.43 3.34 metylcyclohexene 0.0506 98.19 0.050 0.001 0.18 1580.85 0.79 • 224-TMP 0.0001 114.23 0.000 0.000003 0.00 3.83 0.00 Benzene 0.0510 78.12 0.040 0.0012 0.14 1267.87 0.63 Toluene 00287 92.15 0.026 0.0008 0.10 841.49 0.42 Etirylbavane 0.0030 106.17 0.003 0.0001 0.01 101,34 0.05 Xylenea 00057 106.17 0.006 0.0002 0.02 19255 0.10 CBx Heavies 0.1053 114 0.120 0.004 0.44 3819.49 1.91 VOC mass frac 0.5615 Total VOC(Uncontrolled) 299.26 N2(42 Mole%,MW.and mass fractbns from LP separator gas analysis collected 9/11/2013 at State Antelope J-F-28-HNB Emissions are based on 8760 hours of operation per year. I used the source's assumption that the average MW of C84 is 114 14WE0156.CP1 123/9BDE 006 Two low-pressure separators controlled by enclosed flares.Each flare has a minimum combustion efficiency of 95%. Flaring Information Equipment Description Flare to combust produced gas until pipeline is available at this wellhead facility. Manufacturer Leed Model L30-0010 48" Serial Number 21310,21309.21311,21312 Gas Heating Value 1901 Btu/scf Throughput 22924.18942 MMBtu/yr VRU Information-Not applicable Equipment Description Make Model Requested Control Efficiency Annual Bypass Time Backup I Flare Overall Control 95.00% Combustion emission factor source: AP-42:Chapter 13.5 0.07 IIb NOX/MMBtu 0.37 llb CO/MMBtu Emissions Summary Table Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source VOC 49632.89 lb/MMscf 2481.64 lb/MMscf 299.26 tpy 14.96 tpy Gas Analysis Nos 0.07 lb/MMBTU 0.07 lb/MMBTU 0,78 spy 0,78 tpy AP-42 CO 0,37 Ib/MMBTU 0.37 Ib/MMBTU 4.24 tpy 434 tpY AP-42 Benzene 105.12 lb/MMscf 5,2561 lb/MMscf 1267.67 lb/yr 63.38 lb/yr Gas Analysis n-Hexane 630.09 lb/MMscf 31.5046 lb/MMscf 7598.29 lb/yr 379.91 lb/yr Gas Analysis Toluene 69.78 lb/MMscf 3.4891 lb/MMscf 841.49 lb/yr 42.07 lb/yr Gas Analysis Xylenes 15.97 lb/MMscf 0.7984 lb/MMscf 192.55 lb/yr 9,63 lb/yr Gas Analysis Ethylbenzene e4O40 lb/MMscf 0.4202 lb/MMscf 101.34 lb/Yr 5.07 lb/yr Gas Analysis 2,2,4-trimethylpent. 0.3014 lb/MMscf 0.0151 lb/MMscf 3.63 lb/yr 0.18 lb/yr Gas Analysis Regulatory Applicability /1OCC Regulation 1 This source is subject to the opacity requirements for flares in Section II.A.5:'No owner or operator of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions into the atmosphere of any air pollutant which is in excess of 30%opacity.' AOCC 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." • 14WE0156.CP1 123/95DE One(1)water transfer pump,rated at 600 scf/hr(Sandpiper,Model G1 F, Serial number 2040603).Emissions from the pneumatic pump are controlled by enclosed flares.Each flare hes a minimum combustion 007 efficiency of 95%. Pump Information Manufactur Sandpiper Model Number:CIF Serial Pump Number:2040603 Information Pump capacity 9.1 gallons per minute pumped natural gas 600 scf/hour used consumpti0 Control Flare 95.00%Efficiency Calculations 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 600 sd/hr MW 122 lb/lb-mol Hours of Op. 8760 hourp7 Requested Throughput 5.256 MMscf/yr Component male% MW mass fraction Component lb/hr lb/yr tpy CO2 213 44 0.0422 CO2 1.484 12997.159 6.499 nitrogen O73 28 0.0092 nitrogen 0.324 2834.634 1.417 methane 74.02207 16.04 0.5348 methane 18.797 164657.583 82.329 ethane 12.4308 30.07 0.1684 ethane 5.918 51838.050 25.919 propane 6.9988 44.09 0.1390 propane 4.885 42793.699 21.397 isobutane 06431 58.12 0.0168 isobutane 0.592 5183.466 2.592 n-butane 1.8992 58.12 0.0497 n-butane 1.747 15307.789 7.654 isopentane 0.3175 72.15 0.0103 isopentane 0.363 3176.846 1.588 n-pentane 0.3904 72.15 0.0127 n-pentane 0.446 3906.270 1.953 cyclopentane 0.028 70.15 0.0009 cyclopentane 0.031 272.397 0.136 n-hexane O0754 86.18 0.0029 n-hexane 0.103 901.144 0.451 cyclohexane 0.0189 84.18 0.0007 cyclohexane 0.025 220.641 0.110 Other hexanes 0.1286 86.18 0.0050 Other hexane 0.175 1536.964 0.768 heptanes 0.0578 100.21 0.0026 heptanes 0.092 803.258 0.402 methylcyclohexa 0.0142 98.19 0.0006 methylcycloht 0.022 193.362 0.097 224-TMP 0 114.22 0.0000 224-TMP 0.000 0.000 0.000 Benzene 0.0135 78.11 0.0005 Benzene 0.017 146.237 0.073 Toluene 0.0078 92.14 0.0003 Toluene 0.011 99.669 0.050 Ethylbenzene 0.0007 106.17 0.0000 Ethylbenzene 0.001 10.307 0.005 Xylenes 0.0023 106.17 0.0001 Xylenes 0.004 33.865 0.017 C8+Heavies 0.0306 116 0.0016 C8+Heavies 0.056 492.261 0.246 Mass Fraction VOC: 0.2439 Total VOC 37.539 Heating Value I 1287 BTU/scf Combustion emission facia source: AP-42:Chapter 13.5 14WE0156.CP1 123/9BDE One(1)water transfer pump,rated at 600 scf/hr(Sandpiper,Model G1 F, Serial number 2040603).Emissions from the pneumatic pump are controlled by enclosed flares.Each flare has a minimum combustion 007 efficiency of 95%. 0.07 lb NOX/MMBN 0.57 lb CO/MMBtu Nole1 Mole%,MW,and mass fractions from'. Sales gas analysis collected 10/30/2013 al Slats Anlelop 11-14-32HNB Emissions Summary Table Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source V0C 14284.28 lb/MMscf 714.21 lb/MMscf 37.54 tpy 1.88 tpy Gas Analysis Nox 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.23 tpy 0.23 tpy AP-42 CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 1.25 tpy 1.25 tpy AP-42 Benzene 27.823 Ib/MMscf 1.3911 lb/MMscf 146.24 lb/yr 7.31 lb/yr Gas Analysis n-Hexane 171.45 lb/MMscf 8.5725 lb/MMscf 901.14 lb/yr 45.06 lb/yr Gas Analysis Toluene 18.96 lb/MMscf 0.9481 lb/MMscf 99.67 lb/yr 4.98 lb/yr Gas Analysis Xylenes 6.4430 lb/MMscf 0.3222 lb/MMscf 33.86 lb/yr 1.69 lb/yr Gas Analysis Ethylbenzene 1.9609 lb/MMscf 0.0980 lb/MMscf 10.31 lb/yr 0.52 lb/yr Gas Analysis 14WE0156.CP1 123/9BDE 0 IIa ziC.2z2222222 2 2 2 2222222So00z0z022o SS000a r,� 0m 00mmgsbgMigm 00000000 0 0 0 0 0 moo a m m m mm ow ip nyqyqpp ma immp 6010NS C1N ^O!N VI W tOm_ Nn 'NN a N ^ nN TOnNa'OQN N G M 01 10 O (V m F N mOC ON N Vic N n a g 8 2 QOM W Nn .-. 0 Q , •0N�^'NQ1ini •; e n n op,MO e�vlom up SfE m wt t 3 c a O 0 E n UQW NNNNNN 0 0 0 0 0 0 0 2 m y N y N y N Ny N o r r r r r r 0 N N Qnp Gnp Gnp Gnp Gnp nGp O cn N N N N N N 01 01 m m 01 N m N m_ m_ N_ N M LL Yy000Y_Y YYYY C &_1 K th 2-'.n.x^ C Z 0 F Z Z Z Z Z 01 N N N N [0 MMM0`d laG 0 !CNNrr r rraWWW NNN NNNN v v v y y Q NNQQQQQQ %'7 '70.00•00.00 000 as n a v.I nI u as aaa a g as 122222 ww< <wwwwww o 0 0 ¢¢¢ «¢¢ w w w w w w on<000OOO a mmmmmm m m m mmmmmmm > 'y,m J z 01 01 OI OM o o m Oi OM 0�01 0�01 01 m OI '�r $I N I . § t §§§§§§ § § § §§§§§§§ 2222a2222 m e22 222222222 'E aaaa as paa�pa a a a a ta{m aaap as a�OZ BZZ dy aa33 MONeNNOONWNO ,rN GC1cCJ�nNO OV Ats N YNi N O NOOO, 181"ONmpOOQgg 8 . OOocGO f0 O O �OOOOOO QO O^ to r ea o fO C p 8c y J Lk 0 0 0 C C C m a m C a a a W Eie £-5 c5 c$—. Q 7 o o a m m c E E mg m m c g2 g 0 0 m m c E mwo a 2igSm5 pqc xm mcm82 m c c1 .0 m%% ES a o M , E- 2. 0 '" g o N g o T Q m o N J m T m o m T Q 0 NO 0000SOSSfNo s4o5OSz1`i- 0 m mS5 . 060P0§$Cif a>z o m r x w c N > m C >m X W N c > m X W C > Z O m x W N C - c m _ r a € C0 o. U '- O N N NNNNNNN t0V f0V f0V N0 N0 {0y NO1n OONONIn 0 p ppg (;r tp� p ,`Qm r,,-NN V.pONN Np 8N 8N 8N N N BNNNNN pN NNN d' 0 0 0 0 O 8p 8 y O 8 8 O O O O B Stp§(p§1 O O O O S O O O S O S O O O S 47 nn nn n OQ OQ OVQ dO 't n n et Qrap V M M CO CO CO CO 0000000001 o g o 0 o c o 0 0 0 0 F a m II • g m Z v o- >- Z > Z Z Z Z > e e e e t N o oc N T T co m m w w Vl C) cr. coo `y' w M o - ti a • "Z 2m LO •• 0 m N N n N N I- Q ' ' O J m o ALE n UKW ` a m c 12. 0 c E a U Q W 0 U 0 4) N N _ _ LL T T T T T T • m m m m C m G m Q N Cl Q Q Q 6 6 a Efacco_ o ca oil w U' Q Q 0 0 0 0 U J J c t m CO CO U U V U O• m n m m m m E• a a a a a a a a w g m M N'O m — N p u� m o o m m 4 O? �• 8▪ m 'm c m J LL N c_ W m N C O N N C a N m W N 2 U C J 0 T N N v m a > z o m r x w c m Z m m NN NN N " 0 0 0 0 y o 0 0 0 a m m M n • m m a m m m m m NIN N 0 0 0 0 O 0 0 Q.0 0 4 0 N 77 M L7) M tt 0 0 .o a 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) ��1' ?G' AIRS ID#t: 123/9BDE - 0 02. ❑ APEN update only° El New or previously unreported battery ❑ Modification to existing sources O Previously grandfathered battery' O Registration for coverage under general permit no.GP01 ❑ Synthetic minor facility 1 1 Vv E 0 1 56 &cancellation request for individual permits: - ® Located in the 8-hr Ozone Control Area ® Application for or Modification of an individual permit ❑ Registered under general permit no.GPOI ❑ Administrative permit amendment' ❑ Permitted under individual permit: ❑ 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 Name': Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960 Mailing Address": 410 17u'Street,Suite 1500 pyoung@BonanzaCrk.co City: Denver State: CO Zip: 80202 E-mail: Ill Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331 Tank Battery Name t: State Antelope F-32 Production Facility(COGCC#432686) Number of tanks: 6-500 bbl Location12(QQ Sec.Twp.Range.): NE/NW,Sec 32,T5N,R62W County: Weld Total tank capacity[bbl]: 3,000 Calendar year for which"Actual"data applies": 2013 Year(s)tank(s)were placed in service1s: 2013 Control Descriptions: Four(4)Leed L30-0010 48"SN:21310,21309,21311,21312 Control Efficiency": 95% Condensate Throughputs'[bbl/year] Requested": 1-75 145 3 CD Maximum for PTE calculation": 1.7-5470-- I -5 c-)CS (-O77, Actual20: 146,000 While Controls Operational" 146,000 / iS/..:10- Other equipment at facility': Heater treaters,produced water tanks,natural gas-fired engine,high/low pressure separators,pneumatic pump. Comments: Two(2)year update to SSEF required. Estimated emissions at throughputs listed above. Use NM 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" Actual Emissions2s Pollutant's [lb/bbl] PTE25 Uncontrolled26 Controlled" Uncontrolled26 Controlled" VOC[tons/year] 4.01 -/ 351.54 351.54 ,/ 17.58 t / 293.0 ✓ 14.65 NOx[tons/year] 0.60 0.60 0.50 0.50 CO[tons/year] 3.24 3.24 2.70 2.70 Benzene[lbs/year] 0.055 '-7 9,650.4 9,650.4 t/ 482.5 v' 8,042.0,-s,/ 402.1 f n-Hexane[lbs/year] 0.285.,/ 49,994.4 49,994.4 ,/- 2,499.7 41,662.0,,,/ 2,083.1 ,....Wells serviced by this tank or tank battery's API#: 05-123-37235 Name: State Antelope 11-14-32E-NB ®Newly Reported Well API#: 05-123-37234 Name: State Antelope 21-24-32HNB ®Newly Reported Well API#: Name: O Newly Reported Well API#: Name: ❑Newly Reported Well API#: Name 0 Newly Reported Well API#: Name: `'i ❑Newly Reported Well '.. API#: Name: ❑Newly Reported Well u. The signature below indicates that I have knowledge of the facts herein set lath 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 generafpermit GPOI,I further certify that this source is and will be operated in full co ance with each condition o ral .1 GPOI. Ira: 72 ‘� /3 Signature of Legally oriz Person(not a vendor or consultant) Date David J.Lillo ta, Vice President,Rocky Mt.Asset Management 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 or information call: filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-BI 30245 (303)692-3150 $250 General Permit fee for each new GP 4300 Cherry Creek Drive South registration to: Denver,CO 80246-1530 FORM APCD-205 Page 1 of 2 FormAPCD-205-E&PCondensateTankAPEN.docx x o a 9 O r o ml p a O e o f ° e Si oa0 in E O o. a \ Y O 0 C '0 pe W CO�"' WO Y N N N ca Os a 2 m u •2 pe.�, Y b‘.7”0 N N L' W o e Y 0. o a $ a �coq Wa ` ^~�u III o00 y 3 $.' Ga OO m °et a a e ° m X ea >la 2 5 2 L' .°0, ° on. en en m 2 Gq e a >. u V u '� ,oh_ a as w 8 -9 a es '2 •5 ,.; ;, 2 gj w° ' - 8 1. B a 4 o a a q a i W — 9 ba 2 h Y o W .. m ° cC W \ I !ar ii E E • 43 y€ A u a y ee m z a : ei $ pjW ° y r F Y V a la ° {Y Y O 2 Q N t 2 a Y v N V 0 ie - g a .0 0 w w ° a a '° a el„3 °u wY 7r « m z u la L U �C 2� a o `e° .- O U —• o G u e ` a e d c 2 L u s ow a q u £ m o 0 0 0 0 ° "-• u Sp a a' g a w so .. asii •ce e m ❑ ❑ 0 u o v ,Y, Z z Z Z 6 g m .a9a. a .tea °m 7 d o . .Y w 3 .°�. Q 3 ❑® ® ❑ t `.°. T d C R W 3 •T-' r 'O a+ 2 2 E .• o 4 € 2 a Y 9 2 o 0 e t t E s o .. 04 7 U a' ,°°, 2 .54 L Y. 09 ea 9 a ,a° .. 0..'0 9CZ2es '-' eo °o e2 •• of o `o e g z c aa t = esZ0 so • u Q ma .uoa wo9pW� eQ0.1 �'O 0.5 c AZ el o t - a 2 .5 ° e .5 M 2 a 2 a v u u u o = c ., •� °a y ,°e eJ, � U � > > o O �rg u ;e F a ¢ o ° 2 err r r V o° wy a h= a°. 0U .4i om zz .. L $ e a m q t p" a .e Y .a G .5 °' Y .a9 U e a �° w'� W a Icy rJ'- 'C {) 2 0,. .. .>4 q L Y 0®❑ ❑ ® x • c �.I 62 op,� Y P� a al a Y 3 G Y 5 • Y a tl F 2 �•/ I-. W t LUQQC 2 . Q a p W 9Y u , Q u 2a'' u z 5 a' a "n O (4 p , O ea 0g 0 WWW .q ills ate+ g a B ▪ y a 0 2 O. F 2 a 2 U U E e �+ w .'J ' °O a 'YJ 'J ` T. o C Z °o a S a a ❑ ❑ z z ❑ ❑ o h nm .O so • ° `o e 2 .0 o 1• 03 03 S ® ❑ ❑ ❑ •o to 'a 0 w v s 3 m o 9 ,C 2 ri'J 2 a a'N O ,C 4 y N O 2, s y 0 w .0 O o 0 0 ,5 m 9 0 j+ m 4. d I ° .2+ U P z z z .z C o •Cp .-i to '$ 4L N Y m i ° u W 2 G 0 n ° 3 5 ° yq i m e Hen en 2 O ❑❑® m' N 98. (6 G31 /�� — >9 0 N .0 -• U d 0 6 ^ a �Y a .�i i� T 00 e N •O L o .� 0 ti• 'o u 9 T/ m a 9 W a u' v o ° e el n r r ° °� ° �° 0 0 0 = v° — o UU o s � - .0W a0 a rrr U t _ i�' U V L 2N I a a m 9 m Q -° L O pvy "> c a m c s I 2 (� a S .U7 0. .. ,mil, « `cd au a vo \ W y0 .� h� S 'o t,g ≥. u 'y 5 m 'o �. i O 4 m r Lia -- J •R Y 7 .0 .Y' > m ....° \ gild. W a-... e. ° V N O 5p w' a 2 - P. 4 ' 'C .`. 0 C1 Ueo a e. eslF 5 20 g e ' c o a ' E '� WI a 59 v▪ 4ain o 0.�' 3 0 U 2 "" ry°o E c 0 U vs r Z Y c 8 ^p 2 s,`" 14 'Q `u`u c • cv Oy a ^+ Yi V S 9 L C 5 �' 00 O Y fi e e tit m' s° a e « g w c 2 °3 el a .5 U W 5 M W w y 6n e�e1 C o e S y ? y 8 • :: '�p,i C 'i... O •'I F pi day 'e eo Pa .i° 00 ? 1 ' re o S Na 441 m e ao 1,1 •� y Q, U ° m �" a m u c a g ° Si .E E .5 to 0 2-. r Q ` � C7 r w = b'. E. 8 Kt 1. -• Y a .• cog es E. FI e a i .tea a m V s 0 ca 0.a is i'm O 5 4 en ^ .5 e a o w a w g 9 W Q O a1 ... .. .. .. ,m, y� Y y" p2 'O S° ago ° W It,�Jm .�L N ?r. y� .W. % N .Q E qYq q2q a y U pi y o '�O C i �n8 O le 0 TJ V o ❑ It 2a d 2 2 g' 2 E V E '3182 2@ °2p' s E > o E ° p, ea e p c .0 0 s r v 3 a U 00 0 _t en a 5 283 .° 2 2w° 2 s f 3 ill e l l e m ° �yj+ '"r' p a o .5 �..' ,� p x c « « sa a s p ° '° u'� « °' o, .m °' gee ° W B _, o 5 ur o c 2 0 m °° al 6ss = 2 ¢'7 .'.' m 8 2 r g e W .�i , W . U ti A`2. V @ C u _ X C O _ w d y e u. g L 8 9 ri v: a Z ? E.01 01 e 3 2 2 w g G:S cGyi c:i — W 11 `_ U .V . u k in m 0 0 o f S S S _ m U G 0 O Z P v it y y O C O " " h F c wo O �' ° v _o u; U _-' $ a W w n .� w. Ei Q.' 3 40+ .0 m r' a0 OS N O ri as �+ u 4-4 0W N. d 8 N' c u \ j tp V E .4 (3 : .E 4 •N.• O E tii o o } R' S �, u E c u o. p 'S `° n en 0 c4 = c c a o, q c d C CO u N H Eli fl 4 G u L I^ a a N m 0 E."- y 0 0 A 6 a A u ❑' C0 L ? E yo .ei y s u — w A y M . u d W Z 9 9 N N O ^ 'JO „ 9 w C R W A 0.. o M A .E vN W " E d .U. W € 3 m ° Z No i >," " a u w _ a m E e a a `o M 3 a 0 c a o d cap o "' O _, O L. O R M a G C itt A E 0 3 W N c m 0 .o ^ u c ,D ce a ❑ u v o `� d .G •- . c a O C i O U o r0 CO q Cv to to aN a CS u7 •a. Q E W C n o .. is O m .2 C c a _ y: E i o s3 $ A v w o o = °i \ u F =l• peel Ira . v .v 'N O F m 2 o I. u $ u— v oc O g V ❑ o e v °2 E do m E LO V 2 'J F O O L.: O u O N 0 pp O ' y tE U 7 O O JN54 .. C eo O B N o E _ 3 p !�] — ou u c } 0 e u o E "c y O Y O d m u 'e u c F o $? m e T C 'v; w E�+ o '° 'u m w " Q O v E -2 " c -o 2 eo U = E'❑c z v w W m ❑ vm e a Y.E .�9. m a .u-1 y E I a Q m a To L C 0 u E ,_ C. p e .y03 .5 e U d - n O e Q l u > E w '� u x Z A e E o qT '0 a a a , y 'o t OZ N no a 3 W °-' 'n a °o ¢ O a a = `e E A ; v E _ ._ m 'a — •u € •c v m 'C �+ E E 9 c e ro f= Ec a o c a. d E °1 U u u N y - v L y E 0 t° (� di u m o r O E o o m m c co Q E J a _ l _y q .5 O F > U u Q D e ; c c u u y e I,� ' n w y a A O 0 r Z c u 8 a E fA °y no o E. U U = E a ` 1p� N CO C $ • Q v u CO 9 N O co c B A s oTi� y L O O O L C 'y �A�^^ .. W V e e e Le. O d C co yC O •. u L - O o , A O pc cE 0 to ❑ - vL's o ' z d w > q 0 z LE cl ZLU _ 3U Q c p,.� d � y L O E. [r. Q t W >' E v 5 Q oO4. A z 3 U J J C 0� O U N n •i"' y Y co Q ct p 4, u a. Fr S E, Ea v 'L' 9 9 > "e Uwa G e E TO a, 2 E= � > ❑ Z o . O O .0 C n s• ti W u, p ym e Z` d y p e c u u ititz 0 0 ❑ O Y N 1 L c t. ! L, o t� CO p, a. ,.. 9 .r E O W a G ` e G w v Q 4 . = O._ N Q E U t a ..1 .' a 8 s ., w �L(1 [y7 v �r q y a C C Li .N O Z C I_m °JJ'' e i .c. c .E o tytl o a u : O C ut cot .2 4,1 '_ EV 6... ❑ AS Cy V •y .� 0 S Q m p A C V Co) A O 0. a A C IX na O., in L y y of U v U A 'W 0 G. x v u o0. N 0 al ca w w y .E U " m d v v .j W o v it U v o a ' u .. o c v qm u m v o c <� ` c o Q e � � z O '� � U 'F r) r.-in a ¢ •• o Z � � U di ? t m c in q U .� 1 0. W F = p '? c O d W Q a] d ❑ 0 d ❑ Gil o u en _ x °9 V 7'o 0 0 3 3Q Q 3 3 `o E ° E —Le vs,. 6 6 3Q a T 'gC •gC CCQ `QgC 'QgC . a bout u4. 4 N N N in vs en ? J E a ❑ O F7 F1 Ll F7 Ll Y °o• 7ate uj a� - bbe w .$1•a90 W M C '� 9 0 0 0 0 o a m 'a 9 aa.-.1...L......„7 0 ..= ? P O Q e o ▪ eb ra .". a 5 € o a o I Z �Z �L Z Z S . .q 41 — W a u 7 M I 7 C Y ° y �E I e _ w u m a. N s V e v $ m a 2 id 3e. Y : ra m, �' 1 a m °- a a < m ° ° ° E wte a. 3 r ° ° 0 m J+ i� et. ° e ° ° a c 2 C 9 a 9 O F w° a a o CI O 000 a °o u▪ g u a z; 2 9 . t u 5 L. yy e aa ea a 6 C ❑ ❑Di, a Iii a •� 0 6e y p p e Ya p P•- - 9 I u .1 d i a u 0 0 5 € a Oe iz eo a� • 6.,Uaoe o Cgc � = m o U $ o. s v « y m .9 o Q fSm �'O 8 o 5 c. a i s fA E o .°°, Z P a a. m Z T _ ,800, ' o .U 9 u o E . o g 'a° 'fi r h.i E e m < a 88 S Ali e. ed � 11 ' o " z o 8 e S �T5 V a Q q a s a o u $ 5. ° r o u.� g e ,. �ap 1 pw, a ;5 U a •° g= x 4°u F° u�'e'.9 x Ue s O w° Q vi 6 G x E e e 2 •Q o Ci '"q uu 6 O O a W 7 Z 0 C. pO. 1 PW�. .9..° m V 0. m C `e 0 m u S Q « $, 1 $ `d 6 44 a X awe a a� - Ti T A „I. � I e e e e ° e �°Pmi 5 '� 2 .5 a+. E N 9 A -- MI 8 E a oG PG ❑ ❑ a a ❑ ❑ 1u ° ^ _' $ 9 e c - Q 13 '-e Z eZe• `� c 2a. .e �o o a• $ .m. o j u 9 ° q n ° O. 7 Q t� 3. R $ et ® ❑ ❑ ❑ < O AT S 0 oG C Co. x S m .p V N R D € C u°3 ' y �' O 'C W cm v y. ° i x. o li u o.= ° c °0 bc, G t p CIS u m .a N a u W a 41-.4 f o y ° c I a v.I me u o y. Q m .a i ° m G� .� ' n ^+ a °u, m `o a ee T 0 8. ° L' a. 9 ° S e ° � 7u p P ... T O — Y 45 al m e. -MN 1 N G 0. sa Q e ° A ,Q y yyp :....13 s 2 S . d m E ,�O y q J8 u Y ant- ; 1 g p 44 _ m y F y .m. Fn .. RI/�< 6 O S a m m # ^e u C ,6 N N �1 O p 9 e of Y p w Fy G '-JT O O �i ° 9 n mT 0 T�• 9'O a d L O Q d - J ;Aso 2. cn 0 Q o o v o c TO `� e' u w p zo y P U U O > a ""is 1 .M. v a°. �'. o i S CO u Q o " H > c 4 Zy V W N 3 6 PI - u v0U A e E. a :s $ $ as 3 Lieu , F e 'd- d c O. QLL S nU.l 0. 9 . 0 2 1 i ttyy Vei e $ . ' o 2 O u �," ,.� a E' o e 0 Ea 4 ," c We a U Cos G [' $, 8 a e G 'a o .m • 1a d h u p°a ' ?O go 1 h m e e. N.?kg u mph•° O u NZz ..E. N w a •2 Z g �D 2 0 g e .B.0 O0 �m3 5 i sE Q ° F °+ Op Z ^ 3 u K. Q u z gaa� X • ? a .. E e . a 9 e O a LE .m •-• v� IS a U gg 4 u 012005 Y. ,� ° d a s 0 .� W 6 e � F m .$ a ao a °uo5 � sIxxx ° • —`° 8a 8 ° E.=_� a T oa > US $ w yU a m e3 •' a9 5 s° EJ.8.E awo • as ceoa w 8rvu 0 a lit e8 - i i°, v .9 �. a u m o u EEE€ w: P—' PE I lob.a 7 °e Po b a e e m °e 410 0V &rm u meou49 e v v 3H a GIry e V O a T P y 9 L ', gut a m m y • 4 Cl a m m .. a G O• a E 8 ova 3 e a.0 -4-. 02 o2 el . � m � q a s f� a`+ u v c n " . o c o x _2 2 . E =- = g °° y m .ciy a � ppU� = a e E e E m e o o, v g o. ° ' ='°. mg ti ? 1 ZS Pi: ^ Z > 3•�'� d 7 •'a I ZZ 9 oa I2 '6 :I.g uE Ie .E WamP. Wgo wS '� C CT r� m O Q M 9i „may t, m '.. ''J • "..7' O p '. .22. .,.. ... ..T O rJ' N 3 Rm •q4. o tog :5 e E e • 7 'a = •5 ' 0< nu a 8 0. 2 $ w ° s'' ^a g ee..Z-i W 0 o u U 'n° 2 E W D E c 3 Pww Vi w CM w Z• ° c! ♦ ♦ ♦ ♦ e. g Z ♦ � viF ♦ .33 y C) 0 0 0 0 0 `p p o c G 'U' c 0 0 0 0 0 Zw m 55 O c o o W 1 y E `ma .- ° N o o e 1- °d e U m o ro W W m am . 0 M. B. a i q o o W Q C o Q 7 u U . a O a o y a, O a t0a ti CS '� T `a V o V o = u CO �" ..•‘ 2 CI .p y g d Qt � �' E .a O s c cu E C c .s u u ❑ o o ,p -- 'u c U 5 S C�' U E- GCi n v` CU E m v a' 4 w E . .E o E> F mo C3 a t'a a N N O w . p y W ].� C C O! Q O O ‘`O �. 'O a0 P g` M M r ON U © t -' d 4 2 9 « 6i O ❑ N O O O O w y s.Oli E C 3 3 a ]� a = u a a e uIS. .C L 0. 9 ' O o at o o p o ea a) FBI °� a h y ' O ° C °a C 2-o e OI's E C C °+ .L. ct▪ 11 $S v ' yea 2 . V F r. O A C O'S ea u o• >-. ' C, d V s' cn Y C .Nj w• , O G Y E O = t CI 00 F ° O ° U ❑ a Ts o C 9 Vi L 2 • ` a N v m L. c d = F y so O O Is m G L 0 .. mu 0 Q a .J E o 0 C C d s R E.i N O o c c rr' o ~ v d m Oct V " W x ❑ w 'o s' , ° " a -- v mg,- a.h. 0 ❑ a s a > a1 e d._ a .a w0 o � zh ❑ t W ;E 3 " m et°o m e`°n m es 4., ° '� o O N O Sp a a c a E e e e e e e d ' ? m W 0 o,o Qd ° .0 T., .7 .y " e c O C r� c�0 0 v x A U d o � a a a L a e ° • N t. a a v 3 rs o G d u dg .i°. hIll C a, .N En u d Sui .2 o oil U F > U sO s. m a n ° \ F ° E v 2• s O B 1,2 cg e W 4 ocPs •e in a o° e y u m �'5 O• `� C o 0 0 0 o ai L_ W 1 .i_E .u. c °' 3 .. o v 'C c E d W F., .OO n Cl E C Lci s' u C d O \ A n .p '1 '-' _N V ca 0 L 0 044U1A " o W • ° ° O I4, U „ A sql H u�y — v > o E V •. o to= is w o d z v u Z V x � ❑ " ° g U. ° o i . o o¢ . = d� QZ '• u1 E 'w „ c ? •E G cQy !? Q �'�' m teg '" 3 , d w as •o o z „c?, u �i 4 �' .,.7,, 11.5, o = yo t Ca a J y 6n 1' N ri . C c n g ` T E ;i °' o a O Fa ° o a' O Hi — > ❑ G O T ? W I i U C�1 o c ` co W C U Y O N N c ilM 0 L L O 0 •• Y., a Ii N d a) azJ1194 ! uo -• p"F.' ° t ° v e C U "Q -- .ya. uift. a ��. O ou o v G D o D u V1 0 a E 4 = m " 20 u m U E .� .a .°a c. . Q 0 d 80. �' 0 4664 is s a .4, ue A v O" v \ T C4 C. W • aZS A e o L , G ?�.` '. € U �i .C. m co '-" n e .7 "� = i"00 e .. a .F. o iH 6.2 Ciii R - u °Do > uf. d G e W U v V' ° °' r O o y >g4 19. I o o v o o G w' al O e c CI o 000 c o h o E x U F. CC c o .u. C m Je 6 o n o >ea cn O > H 0 o f4 c Z O> O u o - a. x 0 0 au n v� a y - . 'ate+ 4 m F _ X m O O Q W 0 0 • ® W V. v0.0 ] x S rif _\I ,p S. O 43.) •• — d 'l G O 5 O _ a O 5, a a a m r ^ � z = •o aE E z _ = a ° N , ❑ 0 O ° 01 C e N N N £ V g = 6 o ▪ Ca '� N 3 .. g 9 a 9 > e en en `^. $ o `O ea W e i° ap, u o = e .g °a m -p .9 a• o ? 0 c a w', N Y a — = i p e Ti o ;-. r a0 Y r W [wj •• Oy al % .ei y O ° € •w 0 E w A .: a m r. as W jj €0 O 4d a re a g• u c, ° « a 8 0.GGGG. u 3 �cla q q L a 01 u N 4 4 I w r m q a w a v u o O .. ° N. u 6i yxa d o E -- .22E .2Y ° m ggq0q. ° a i. i 3 v a al a 8 0 — -0 .a C L •e •‘.' F` e a ° a ° a. `o 0. a z e . m a; 0 •.., o v. 0 e a Y B K y O 3 p� a v 3 u a a a 5 = T T 8 6 a ❑❑ 3 ae •� g •o 2 "a e ° Y € u w o. 5 0 a S o 0 in U CCC a i+ .5e u a' �3 2 F w '° aY. d a °°' Y 3 Q 33 > > Cle 0 u 2 0.1 v Y On O. a .o o o f `b o Ell fi b p�p U ° a w m ra a o ¢ 7 a E war Ui o U 8 s 1 8 K O cnP.2pp O O : 4 B. ° .Y Y w • O L a Y �j �• 9 L S e O u .5 ; a M 'v a 3 a °' • al , Y U g o .5 o x Y WO O >e, e a P 8 . ya `Y• ¢ o g e 0 .0 a r' •a = ° u u m E ' ¢ 6 ¢ 9 `dm �' L U sE2 = . QU > as°w z ar U U t. •0 3 ,Vr! 8 •� a o Y .o ° °r m.a tom' .w — pUp.�, g ° '5 aw, E. 8 .o• {�s77 G 09. y o v� � �' N v 'g .�" UQeO w° 6h ¢ 6 �' v as Z. A fi ° Y CI 0 m 0 , U U s F V 8 C C Y Y Y Y 3 w OO 0 D p O D C O w � < O 1'i m C ai a ❑❑ aa ❑ ❑ • Q Y Q Q Y Q . u tie, NO �' o. O L O �" a O V % . Z o ° O ❑ ❑ e .. 9 O cid• tp cz wi C C � Tj V O 0 0 Y w .+ W G L [t. eu a a z z z °Y .. .w e u .°.O ' `a vim` E r C •N O 'a O 41 $ s n ► O ® ® k V a r 64 E ..1 '� a .^, H n S E 8 • q en g Y G ` e wq et a0 N ell Y Y ^ Y I d v w ° 2 „ n -N C Y C Y N •N Y •9 a Y .st Q� N a C CY � J Vj O .� O• 0 r a Y ® O O T C • O 0 . W z � Uw N O 9C'l ao w x 3W I 1.3 e i r., rl N .. Y ^ _ Y z z ° . W o o w ' ^o• a ^o m T O S' O N C :Q ': , .J O .7 E o �yy L a a u a c e Y m so z r o o ems • — a oeo .4o g CO O . •- 3 a M Y W .. v in h .0 O .e v c e Y ''�' $ E o a u °m VI vs ° Y $ Y •5 a h c a m x 0,2 p5, C ¢ Y W O " N Z U 5.3 lip a C O a U L O b ' O [-. a) 0 W daoF y g c v r z E = {as. o °w > e a .. Cr) Y Y g>04. e a °OO� s N, a. C r U S e. Y v N T 3 D z O Q Y en r p z 0 Y �: tEl L a Ce a CO ° F r ° y U :: a y 4-“) .%. a E 2 g 2 e� •5 W a ti u 2 a ea W a e UU' -- . i� , cn ° mob', . N ec f ? '" c N a 0 o, :° Y>_ en W ^ r a ... ° U .ei e 0 i, .r .c-„a ° y to c ° O W U 0.7 J e, 0 O © G . $ .a Y .. o o z y� ►1 u ti .9 COca .a m a G o. a r y `• o 8 o• c Y 8 •a 7 '' ,�' w C9 O 0 ° E — a c c `' u� O . a 2 py Z Q ti T z ° 9 U 9 m0 O C o' 3 T 6 8 a h u It " w a ¢ O Gl o c °° F° a 9 x q a a ° e '5 C D C �' e fi rn 5 :S e . e x 'V •o ° m h T �• a .�Y. cn 8 U c y y Y € d = = s a v a° m w O aw w in a m w° Z a1 3 = v, 4 4 ;a m 0 a 3 ® W 0 c V O U 0 V 0 u a co cn Z O 000000 0 Y O O O O O O O G m 0 V a k. .00. 0. 0. G. P, P. a o 'c w ga E g ? O o o -g -g - l g ° u y e ai a o .� y up a .2 .°- .2 J .u-1 5 i d o. •y c. "y O = v el a a a a a a `2 u a , _� .ei m — O .. W W W W W W W v. E - w e ° m C T O W C y a m °> > Y '3 W ? Po s o u d ne e 4 ° U 7 O E c >> e l s e `, c _ ti e y 0 aad o al a ? - C^°, 0 0 � Gr�A UUy a+ m/ U O cui V = _ o o p, ,N c O.' G H `" W (� oe a 72 z c. �' a H N N ti r N E .y w O d a E ❑ p , > = U S OW = u ,o E OP L a W > — > a t m e R O ,�-. O 0 M > C E 0 6 > m c a a o c .ty o o e: c o S U \ LC O a o a 0. u x to .� y 4• o o a r- E .G ¢ G c y M ray s c c O = o a o N G 9 iY.i .S. c i ❑ ~p d C o y d frr A A 20 a u oo a e i4 E ❑ c c w '° �'/ I q o eA `: `o s Lee W U v o v 3 v, a. X II y Z q o g ` .7 r5 o e a t ` v a v to u r 0 Q I `O -c u .o O W B p O v u w a \ _'O_ /,; G 7 c a .a © �ja' o m ° a a N m p u C c e t 21 r 'v Vi U 2.1 ❑❑ E w u o vri v o o c Q ] v fi o?,` a ei°o 40 z t o . :?1/41/4 U e ' m I� o .7 a O ^e - 9 n u ,�, W � w U W W i 4 > O e h E 9 g . 't 9 v L out g d .a o e b E w w o; � w 9 ., _ A w a o e r°0 I.P. 9 'E a, C 00 m s n O q Z N 0 m,� c� .d. c ` q el y G 1 DOD R d E C y •.E a Y e 0 0 a. L a. ei chet o v%m cc W '� _ W ' eo U � w = = Vj d w c e Q. m p u e C C •y \ Fi 6. 4 .,y x Vg N E .a '� E. E e e4 .7 u' Ly 05 ¢ e W aI « e v c e c mY Y h.2 O x n p $ 42 aill ' 0 0 l w e 7 0 ° w O ., = E R o 2 E u 3 a c ', g E u a u c o p ❑ U 3 U 6 E I� 7 tW C U ecj _ O 4 y j O — 4 I—I t../\ ^ - O p M my _ e, a r.i k., yc F _ 1 Y ZC ect r, • G c v h 0 ° 0 V O O t ,c .v. R m ca r. T G U L o Z Lt.1 `c° to E :'q` '0 ° H o c u '1/4, y c.v.' m '`a ' C a W O e, v ct T 6 cn py on o pp 0 eC y{s. N Y q Ci L., p y c'15 :2 'W of W ? °o o a c d v L O W 2 ai Wo $ >: 0 6 u W il��`.. y! S a •G .9 , w a .ON. (~ = p , -- i '� mr �C..; a .ry 0 �A � E .o Z m E .ei E •��. 6 e a o t " c.0 u e '� "o ' d d ow 0 I-4 d .ei C W w = 0 N h en N ti P?', a n'i C Q T _v U R e PNS a fi e a �" L:„ c G a oIII O O O O O .y o C '� . E V C R ' .- u 2 q m o a 0: n o ai o E m E y m 0. c A 8 R a o f v a a°° w [- w m - d I a. I a -a I _ w u u m oC u o o [ligg 'zm a e,y 01 .6 c d a o .5 E U 0 c E c . ew .e. e c c.., e �a d v v h w . 0 W , O cH z a SI u > > 0 7 O N Q O I'U O E G y a > L O > u O T K S a 0 R a c o _ 0 c A a a1 F . c a>- ' Co u :� Z el c W U X O a > O L) u ® it m Cl') (n "® CI) V1 rn k ^ Y U co o m a rs d a : co N 9 . 61,4 ❑ ta E zY � r, r, M h � F. `o O > [4 mm aaa 9 = q Era W , o a aAA '° " E mein la 5 rn m K o 2 F E 9 e C .S � � .. E Meno 0 o m .q a s .-1. o a. a 9 �3 .° h o _ 5 m Y N W .. Y 1 °y , 9 9 a e° E " € y la i o m » a W m G C c N • S V y Y . r t°�yy a a d i 4� I1.y,.yI �v 0 9 •O u >:":1 r Y n Y to is-. .o O 9 S L y s ❑ a W m W W '�> g9C 4 a W 3 Y Y ° ° TS a ..• E . U [y ` 0.o es o e0 6 00 ° E. o G S Q O d m m c°i 4 4 C7 ca in +y_' FC/4y� _ pa, a tam u__ D__ - .2. [o • S E e L« ' u ; ° C n o Y ° c c z Fr v ❑ T n • q T 5 Q C 6� 9• T O 0 E Y b O � l O O N O pp Q 'E v Y C W III L q C Y '.°;. A m W W V 0 a O y .' a 0 O Cal .Vi L '°• E a1 •Yi .❑Y. :: • a C y W t E y.. oD O I.J • r S 0 EL Vii ° O ,°„ Z a a e u W m E •v ° q ag Q �e 'O o .5 ❑ v v o O7 22 ° 2 : c ° m Al" U o Y u o 3 'e .5 a ° c u o Y '� •e rte, a 3 0 �o .a .c u, p q 5 C p, Q o °' w °- $ : U ❑ , o V U > m WA. R1 W u U U O ., z 7 U I1IHII ao . 7. W a u Yv UQeG w Ern 6 Qc q — a. O rea aX UU .5 - -Y o ti- = d U U ;, x 5' s . 9T • C INS a e 0 3 > O iv a a ❑ ❑ a Cr ❑ ❑ "ii 4 • O m mae 0o-a yyy E o •a°as ;; .Y. O rn 'F� Y C-.. o a xr Sa z .0 � > R x. o G v re _ w N E m l ix a ill: I g el en en m o en SFr. 3 a 0 m P. • 6 ., d C c a >Y YS N O P Y aNi u o i� � y O ,� W n. 3 O CO° 4 N Y 2 >.' Ll >O v E 9 m ct di L N .Y� W.;. $ a C O ° 9 C 9 N el N T Y ® O x ii V rt 1 • yy • �] C. Y U 6 z i U .. M m ° N" 0 a' a O F E w z tiIi Y v • Et- U LO' 'Z•0. g ,0 ° •. Pte" Y 2 .� T X • > • 2 0 -V 9e� C g d vle I co ° y nitt W C P N F • O Qa CM F� .o r = 3 .; Y > g O WI o F p ° Z5 0 E o e c a _ .5 U▪ .l N 8 a N F N a 1 v C v v y > '3 U rn 9 Oc9 . E " Y z c: m a be ❑O 9 F� ' ^ o as '— Y U u y h U a E S ' C ` as 7 M O W . i e^ 5 r e a. Y AO = m C ^ as e ur m Q„�°8 .�. a ie a c a a W Y •° .. en > X mm p n `s a .mi r y a°, it .i°. O Q, It $ 9 I £ q •� m V`i a e G Or a q ba, Y ° m 'g �qa m o. .o °°' .9 La c ep N L ° 1.4 o 0 L O C.a E .5 O Y .Y. p, GI E it d qd o y .. o ea v° o m ` o U i c° .FF. Q e a $ . C..7 E ,O, C 'W •d t .P•d' C7 ❑ o q 9 —c• °c a Ln „ a = m 3 a a m I ° T .r T za°a - 9 es U V I In G '% .P q V G x O' ° a .°❑ .. d A o Q Q enes, > �. z �` ° a o P. .5 F" 5 m t x v 0 p E. ° A 2 o ° ' E 4 , o FF'yj o E h ❑ ❑ 9 e •es x 7 5 z ° % 3 0 a U FG O °e. E ti n°'e• w m a w w n w` z c� 3I n 6' 000 ❑❑ O 0, >Y ® f� _ W N 3 O .Q N M nl nl M Nt M N cni f+l N 'O �, o E p ^o` m .`c na°, " x Pr .� x x `m rn « G g g g tL O U �r m O O. 6, 0 0 0 0 0 0 y L U m,§ V ± Q w /Y W L 6 < C. L 1 S 0. 0. 7 L r°i. 0 oQ 7. .w 0 C U en - 9 e GOi ¢ 0 ao. x V — C m o °; 0 �n .1- w 0 al a 0 m8 a c r g _ — o ° ? E Z '" a cq . r U E al FT4 E c v. n 10 a k- le c� .L. pp ° 'r .. El C a .Mr g .- 0 U .H.. 0 0 4 .d+ ❑ y? c °� o d 4 � E z { Q. ae. � � m E c Co .a, y °' u c_ F c a H CJ O A oE' v q S a en a „ a m o w m T 0. ? l3° _ T. M v 9 c L o , a z v e E,' m a c O a O '� �� O k� i e 1-4 .E a O E O 3 W r 3 c m a e �ryryb k,_R In .0 yy o o ^ Ia W e = a ] r ei e M z d :3 n a c Z 0 q a o m o h .m o _ ?+--. E i oce a ie tl =?v kr, pp 0 in N .Z. v. C r F'S 'e7 Q s a U 'o Z .0 0 U v PPDD U Y2 c 0 O J O e E c C m .. .tl U Q O ❑ > i O ❑ .. 1 m Tiy. G r ,, V. _.../ . L r7 v ri c acI. . EGO ' �° o e N w 0 . p.`n r E c. m rn i ° ° �+ eV 8 t L ooa 0o CI a tl F o ° i-1 p o �' d Q 0 0 .o. d a., q tl Qi fn N m m 0 0 ... 0 O y o G U 4J Y y o p U ° o' a 'J `� 0 CO 'a'+ >, p fn _Q 6 m a = W .E m « 0 .a a L 0 W. w y 40 p u a p a w b z. E « E GI q tl $ `J 3 d d o o m F. g Q f d c 1 tl > E w d i S '�. a o` 0 ad U E o °". c a a a a a a a a a � .. E E Ca Z N 50 W t on p'3 G CZ a .. U o '� N Cr r `� -.5.i Poi o€ETS ?.' .4 d 4 o r O E c n W a `A �° en 7 ` v L E- C °p U H 9 U p O Rl O '>� Q E '� W y H Ill r® a OI O try O a. O O O .�u c a y ' tl >. o a F a sa A a A a u � d 0 u a N m O u 9 v U .3 a .L+ ,J u O U v y W Q :3 � tl U c4 u 9 e Q U o w22 v o _ Z ja'j v o o Oe a aaaaac ors - o E 9 - Q ; mss Pd `yo _>' m - L.. Q1 �j v W o CO E; a e o e e e °i E¢ ' 3 N = v � -8 UW ay d o „ i ❑ Eo ❑ -° En 0 .'f[ a 4ta a F" u o F ° > o w,tia — d o Y c a i: 0 n H0 ° E �.�e2 0 ea ca E• ei‘e L ® Ce 0, O� R 21 2 .2 raap y EA 6 0 P. o y ^ .p a L U ra° ' a B w m EE — ea,- v Up o a � <9 u d d ` o w, t -g, 0 Q s�y o `o p C Q c 4. ° �, o c a E .o. �:f:E ° 9 y CO s, .y PS a .+ as y T V r .y U c.z �j a > ''P"e Q 3 o i. T N red y up d O W 7 y Alma t Z` t o o 0 0 0 aoi ' Y is ti " L o °� ° R'i > is to �.i c w U bn 0 m ... — p "a c a3 > s C �a�'G 'c 8 a > > o o y d a N = po tl d o a p t o o p a a a a a a w a a m.— u N o .L, "it Q -5 > C q 0 ° U 41 0 o 0 0 0 0 '‘4,a !die = Q rn En El V H E U m m .E U0 W ° Tao c P. ce p. -41 B I o a I ° o m Ioc, >. h v c m I p z tl 9 Y ° .i ._ E tl > 'v� K° Q Fc (1 tl s k? =• poop ^� = a = a' tl L at O W O W t. 0 0 d ® W ren n fr., . Y ~ O 9 O Y O m s E Oo0 h ti C a. ^ W a ❑ ; E Z .Y fl M M NI N L n, ` .. I e wP. m v a a a i1.8 3o Z, Y i Q 4 2 sO ,a .a €ay «p. O on y m a PF 9 �22 eQ `E 8 S € �� Cm .z c.'c. > qw ° a a, t a = 0 .5 c .E .„ 0 a 0 •a 'a '� 6 \ o r y g �o Y N a•. m E °y e 3 u E <° E ° E g w Y a ms ina Pw ¢ ° e°o in Y c o je y .y r�li • to a Y V Q Ri .Op et 0 z m r Cr 'r, � pmp `' 1 3 w 2 •o ,,r! " c j '�Y' E �Ojv m 8 w a [V lQ Y m .Y. c. Y o Y C, a , 3 B u . r •:: C ° ° o o n' p w• 'e •E U F�" .6°. a '? a `e ,n ° '5 u a o E m m o o c? o ca L c7 a t al a 0 •.a o n C a a aQi az C" Z. E y P" O rn m aC s a a. a, u m 'o E a W 0 ° C eon " u 5 a u°., Z d a a • �, °m ❑ ❑ u T qq o aw q g o e e y o o a+ sw. 'g a " °1 c W a a g v C Q '� > 1u a s .. 0 c a„ P' 2 0 0 fiV a r ° • .Y. C .Y. ° m v. .� s d V 0°D O CJ L % F .O e o g y Z y •a a l° Z w o Q `o q m 'L'O 8 __°0 5 � c v at• to o c • e' p v .9 3 in 0 .3 °oa 2 E e c �° r g N U u y C° U U p C Y 0 a ppy,, a I ° i ° •.Yd • L1 m m E Z 0 Y9 O w .g - O v a U U •.. w 0 2 E a '� . o _ F. I e e a a `o 3 'm J .. L 6 e a a ❑ ❑ a a ❑ ❑ v F ; ° m m? °, w .n a a°e7J a G �2 v, � Y c- e ° a ❑ "� a T' • € 3 ° 0 o .6 3 c n A-5 .r w • 8S. r Z 'W 5 j. _ .m N, X. . o0 0 01 _ w °' ..g LI ._ a en ..en en orl Fy S Y N O O., ..* la, y o y O a, „y I I `o ti 2,` c y n n E ® c i= U °� _ U U Y N g' ,, .�. r yes u o °�' v�El 9 g a rr ,°, Zy W N E L; I�.. a o - m q O N E- a• " '\ - � 9 L �1 Z y O en O Z m Oi Li. 3 O _ n o In V c �D I \ f., .. .. J , G FilV c 4 I R lc 0O ii C• E D �i u O o o ¢ a k' W e w a N O oo O1 co CI F Je a' -le. o E c, 2 a_ guy J e Q r-� 11``,, Go Oa, a .. " w e y ✓ W •p •Y N E-I O N -N r >ki 03 ea J £- 07 )4 ei. fraa •W n i >4 c 4. 2 G 6 ^"''c W .`.� ^ �O N ate., ' :eNn e d m o r�. .a. O '3 �,�Ce �> o 4.n c' .. �` m° mea e A Pw a L. o' 0 o a o 2 • E .5 `El v o N •L. u 3 a; a .. .. •• a ^' y a a •a " c U d a a: Ca Y . e Q 8 I C m o 1' °• 4 C7 o .F E ° a o*.. •o 'E Pa^. °s. g a` m p a I Z Z 0 s o v I « 0 .0 a. a I o Y c Z W e a E m F .� o E xo ,oa 3 ci a v m d E = O - s 3 la o E y Q '5 c E o ^ n '� o 3 0 aa. U° m 0 $ *be, p 41 w rig a ti a w 0 w° 0 c0 3 � co A ❑ ❑ ® ❑ ❑ ❑ °' > 0 G4 e 0 — `°. '' ^. c C 2 u v, v', m v o u u u 7 c E.c Lq o g 'e -. c a: - aa- g 55 m a 5 c'. t12 n W U M ..E.," •00 H t-. m m m m m m ZI a v N = 48E ° . v es cn qi N y y y vyi U T W pep,., pQp,. C U 0-0-0O 0 N o` W W 6 6 2 2 2 2 n 2 L• 0 m C O a l• OU _o 5 • m V ti Q cmp r C 9 O c b/ a -1 O R � °� " R iG t n O u eu 4 0 v .5 .0 7Y E V C L• �Cq N CJ C cri W 0 0 Q N O en r-. O O j T. a a w w v a .H... ti 0 0 0 0 0 Q! 03• = u z 03 s S v v O L d 9 E a © Q O O MI Q .V v N 00 �_ 9P. 0 0 C.) G z 4 0 ,� " o o. 41 b t r _ c L _ O S, Q 9_ p M R u C P. C C W o a E O W N O F N o e e e e e m m- C w ,7, p .a n o v o 0 0 0 0 '$ B 'C _ - a m ❑ a m c O .A 0. Y CO 0 t) W Vj 4'... N 0 y E Q cc co V 0 O 0 a E Q 0 € u z c mo U �' c '.9�� ' i' �. O ❑ .E > v a ❑ ." Y °o -"0.Y V = z Q r U E v o i - u _^. co:: a J a ° w o 0 0.0 CJ _ on i. u v B r e Eor-' aa o p X p F o `0 1 o v ›. " a .0 uO s+u C 0 1-I o D N^ — L.: �. ¢ u p do O V d p] c s' v v 0 i a E. E c o d' a • c A x ❑ d >ns E o N L.B = d C C r� n pm y a W m Cl). " a a a u u .... u u '° m:a "�' .a w Q <v S ' •b 73. z h Y {L G N Cyr O �5>y 'y FSjFjjj 'yy- dl d .i ri V q p N❑n 0 ❑ Y 0 O O OO I V a C C C Q l i 9 E W.O Q Q V U o - n co L L a L L .0 .0 .0 .C G C R A p ‘24 E d m c o W E 0 NI a k• a 3 o o A X N c �' °a E '� 0.ci o€ t a e _ c ` E a O •0•E c � w s CO d "L. 2 r a i4 °1 • U F > U o o ao M W y II O� ° C N 0 r oO oo 0, L0 Q Q z Tic)" v . \ 'o�, 2 ® •W € e n GS' .°p. .P: a .n. " C0 9 0 \ 2 y T O O N N V L C U w �` S .5 C w 0 O a ? C \`` - > 0 x " a I < 0 gv % E O u -c u�0. _•cc' c V 0 C '" 9 " Si E 0 u iE y�/ u d >v u Q C a U a ai t.y Is' E \ Fy-� ,� > V o ` e in Vl 1n Vl VI Vl " fir.. c g o C p i. O. T T T 0 Cr, z 4 u •R N u C � ❑ 3 e— d v,1 c a .�.' 'm m 0 A 0 c A u CID W Q E LL.. E .. E E w " m d ` Q o>. R 9 x A U '" W o a O o E; e e o e o C°' y U Y R m .. v co •� V W r .q � Q W y n.. m u O Of"E ^ V$ T P,-. g r •• 2 " " A C'' c y` m `.0 0i• z • C ® u g m " '�. G . 9g•e a 9m w 0 O ^ O is E m _ c A .. PI::: a" 0. c a. o y 9 q A O `� 'o > C E W 9 0 S PI::I L " " v U \ .N4 a e y¢a � e oNco t9G" e 0 ° 0 .2 O e x. O Q m 5 w 0 C . y pp f a 0 a.� V �. A. v .. is 9 'S V — " !� E y; c CI i 'D " q v it▪ i, a .@ 6 ` 'd 0 0 i .fir 1:;; = A s` 0 0 0 0 0 v a m < p Po 0 i o = A A o ° $ e 'T'"C o c a a a �' .q a " N 4 9.W d e o .6 " O s T Q m 0 `'' U a 0 0 0 0 0 0 .E 9 = A W _ e m p w° > v .uu. c .e y a U U U U U U u y y V ,7 v� v,:'= H 'G U m o .= a u W .E „ c c ' a C4 13 Ndit v > > T .q oc su yE S U xcx e` 2z C m m z EA 0. aF aW ° ° OUa. v O 3 o > z � " o �, z s :. 0,02 U ss — a aF _ x ❑ O Ca 0 W O W w O ❑ u ¢ ® w w m Hello